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Non-Confidential Business Information (Non-CBI)

Certification Test Report RAIS A/S Freestanding Wood Stove Model: Q-Tee II Steel / Q-Tee II Glass

Prepared for:

RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Prepared by:

OMNI-Test Laboratories, Inc. 13327 NE Airport Way Portland, OR 97230 (503) 643-3788

Test Period: Report Date: Report Number:

10/19/2015 – 10/23/2015 November 2015 0138WS016E

All data and information contained in this report are confidential and proprietary to RAIS A/S. Its significance is subject to the adequacy and representative character of the samples and to the comprehensiveness of the tests, examinations, or surveys made. The contents of this report cannot be copied or quoted, except in full, without specific, written authorization from RAIS A/S and OMNI-Test Laboratories, Inc. No use of the OMNI-Test Laboratories, Inc. name, logo, or registered mark (O-TL) is permitted, except as expressly authorized by OMNI-Test Laboratories, Inc. in writing. OMNI-Test Laboratories, Inc.


Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

AUTHORIZED SIGNATORIES This report has been reviewed and approved by the following authorized signatories: Technician:

__________________________ Aaron Kravitz OMNI-Test Laboratories, Inc.

QA Review:

___________________________ Alex Tiegs, QA Administrator OMNI-Test Laboratories, Inc.

Evaluation Decision:

__________________________ Sebastian Button, Testing Supervisor OMNI-Test Laboratories, Inc.

12/31/15 ______________ Issue Date

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

TABLE OF CONTENTS PREFACE ...............................................................................................................(3 pages) 1.

SAMPLING PROCEDURES AND TEST RESULTS .......................................................4 Introduction..........................................................................................................................5 Summary Tables Table 1 - Particulate Emissions Results...............................................................................8 Table 2 - Particulate Emissions Results (First Hour)...........................................................8 Table 3 – B415.1 Efficiency and CO Emissions .................................................................9 Table 4 - Test Facility Conditions .......................................................................................9 Table 5 - Fuel Measurements and Crib Descriptions - Pretest ..........................................10 Table 6 - Fuel Measurements and Crib Descriptions - Test ..............................................10 Table 7 - Dilution Tunnel Gas Measurements and Sampling Data ...................................11 Table 8 – Average Temperature Data ................................................................................11 Table 9 - Pretest Configurations ........................................................................................12 Table 10 - Test Configurations ..........................................................................................12

2.

PHOTOGRAPHS/APPLIANCE DESCRIPTION/DRAWINGS......................................13 Fuel Photographs ...............................................................................................................14 Appliance Description .......................................................................................................18

3.

TEST DATA BY RUN......................................................................................................20 Run 1..................................................................................................................................22 Run 2..................................................................................................................................33 Run 3..................................................................................................................................43 Run 4..................................................................................................................................53 Run 5..................................................................................................................................61 Run 6..................................................................................................................................74 Run 7..................................................................................................................................84

4.

QUALITY ASSURANCE/QUALITY CONTROL ..........................................................95 Sample Analysis................................................................................................................ 97 Calibrations – Methods 28 and 5G ..................................................................................116 Example Calculations ......................................................................................................145

5.

LABELING & OWNER’S MANUAL............................................................................160

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Section 1 Sampling Procedures and Test Results

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

INTRODUCTION RAIS A/S retained OMNI to perform U.S. Environmental Protection Agency (EPA) certification testing on the Q-Tee II Steel wood stove. The Q-Tee II Steel wood stove is a freestanding, noncatalytic-type room heater. The firebox is constructed of mild steel.Usable firebox volume was measured to be 0.90 cubic feet and the stove is vented through a 6” flue collar located at the top of the unit. The testing was performed at OMNI’s facilities. The altitude of the laboratory is 30 feet above sea level. The unit was received in good condition and logged in on 9/16/2015, then assigned and labeled with OMNI ID #2138. OMNI representatives Aaron Kravitz and Sebastian Button conducted the certification testing and completed all testing by 10/23/2015. This report is organized in accordance with the EPA-recommended outline and is summarized in the Table of Contents immediately preceding this section. The results in this report are limited to the item submitted. SAMPLING PROCEDURE The Q-Tee II Steel wood stove was tested in accordance with the U.S. EPA 40 CFR Part 60, Subpart AAA – Standards of Performance for New Residential Wood Heaters using EPA Method 28R, ASTM E2515 and ASTM E2780. Particulate emissions were measured using sampling trains consisting of two filters (front and back). The model Q-Tee II Steel was tested for thermal efficiency and carbon monoxide (CO) emissions in accordance with CSA B415.1-10. SUMMARY OF RESULTS The weighted average emissions of the four valid test runs included in the results indicate a particulate emission rate of 0.9 grams per hour. Three additional test runs were conducted that are not included in the weighted average. Runs number 1 and 5 ended due to ceased combustion prior to complete consumption of the test fuel charge, and run 6’s dual train results variation was outside of prescribed limits. The Q-Tee II Steel results are within the emission limit of 4.5 g/hr for affected facilities manufactured on or after May 15, 2015, or sold at retail after December 31, 2015. The proportionality results for all four valid test runs were acceptable. Quality check results for each test run are presented in Section 2 of this report.

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

INDIVIDUAL RUN SUMMARIES Run 1 -

Attempted category 1 burn rate at primary air setting of 2 mm open. Ceased combustion as evidenced by 30 minutes elapsed with no measureable weight change. See Section 4 for complete data.

Run 2 -

Attempted category 2 burn rate at primary air setting of 5 mm open. Observed burn rate of 1.28 kg/hr (category 3). No sampling anomalies occurred, so this test run is valid for inclusion in the weighted average.

Run 3 -

Attempted category 2 burn rate at primary air setting of 4 mm open. Observed burn rate of 1.07 kg/hr (category 2). No sampling anomalies occurred, so this test run is valid for inclusion in the weighted average.

Run 4 -

Attempted category 4 burn rate at with primary air control fully open. Observed burn rate of 2.51 kg/hr (category 4). No sampling anomalies occurred, so this test run is valid for inclusion in the weighted average.

Run 5 -

Attempted category 1 burn rate at primary air setting of 3 mm open. Ceased combustion as evidenced by 30 minutes elapsed with no measureable weight change. See Section 4 for complete data.

Run 6 -

Attempted category 1 burn rate at primary air setting of 5 mm open. Smaller pretest fuel charge used in order to compensate for higher air setting by creating a cooler average surface temperature at test start. Observed burn rate of 1.28 kg/hr (category 3). Agreement between sampling trains was out of acceptable tolerance, so this test run is not valid for inclusion in the weighted average.

Run 7 -

Attempted category 1 burn rate at primary air setting of 3mm open. The primary air setting was the same as that used for run 5, but a slightly less dense test fuel charge was used in order to prevent ceased combustion. Observed burn rate of 0.87 kg/hr (category 2). Burn rate below 1.00 kg/hr is acceptable for stove unable to operate below 0.80 kg/hr. Primary air setting of 3 mm will be the minimum for production units. No sampling anomalies occurred, so this test run is valid for inclusion in the weighted average.

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

CATEGORY 1 BURN RATE RATIONALE EPA Method 28 section 8.1.1.3.2 states the following: Evidence that a wood heater cannot be operated at a burn rate less than 0.80 kg/hr shall include documentation of two or more attempts to operate the wood heater in burn rate Category 1 and fuel combustion has stopped, or results of two or more test runs demonstrating that the burn rates were greater than 0.80 kg/hr when the air supply controls were adjusted to the lowest possible position or settings… NOTE: After July 1, 1990, if a wood heater cannot be operated at a burn rate less than 0.80 kg/hr, at least one test run with an average burn rate of 1.00 kg/hr or less shall be conducted. The U.S. Environmental Protection Agency Applicability Determination Index, under Control Number WDS-109, states the following regarding this requirement of Method 28: The purpose of this requirement is to ensure that a good-faith effort has been made to achieve a Category 1 burn rate. However, if the air supply control is tamper-proof, EPA will accept one test as adequate documentation that the stove cannot achieve a Category 1 burn rate. Note that this applies only to stoves which do not reach the low burn rate because of limits on the air supply; manufacturers of stoves which cannot sustain a burn rate at lower air settings will still be required to submit documentation of two or more attempts. In all cases, a test series consisting of at least four runs is required. As the Run Notes in Section 3 and Table 1 in Section 1 of this report show, Run 7 was operated at a burn-rate of less than 1.0 kg/hr with the combustion air inlet open 3mm, which corresponds to a cross-sectional air inlet area of 0.24 in2. Production units will feature a fixed stop limiting this area to a minimum of 0.24 in2 in the fully closed setting. See attached drawings of the primary air controls. The air controls for this heater are tamper-proof. When tested in accordance with EPA Method 28 the heater cannot be induced to operate at a burn rate less than 0.80 kg/hr therefore Run 7 fulfills the requirements of the standard. ADDITIONAL MODEL RAIS A/S produces a slightly different model of the Q-Tee II Steel. This model, the Q-Tee II Glass features an additional 22” x 21” glass panel affixed to the front of the loading door. The overall design of the door is unchanged from the tested model, and the same inner glass panel is used. The rest of the unit is identical. Emissions performance is unaffected by this purely aesthetic design change. Therefore, this report covers emissions certification for both models. Complete drawings for the Q-Tee II Steel model, as well as drawings unique to the Q-Tee II Glass model, are included in Section 2 of this report.

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Table 1 – Particulate Emissions

Run

Burn Rate (kg/hr dry)

ASTM E2515 Emissions (g/hr)

1

N/A*

N/A*

2

1.28

1.13

3

1.07

0.55

4

2.51

0.69

5

N/A*

N/A*

6

1.28

2.33†

7 0.87 0.91 Weighted particulate emission average of 4 test runs: 0.9 grams per hour. *No results computed due to ceased combustion prior to test completion † Results excluded from weighted average due to unacceptable sampling train variation.

Table 2 – Particulate Emissions (First Hour)

Run

ASTM E2515 Emissions – First Hour (g/hr)

1

N/A*

2

0.96

3

0.70

4

N/A‡

5

N/A*

6

1.78

7 0.57 *No results computed due to ceased combustion prior to test completion ‡ First hour emissions not computed due to test duration under 60 minutes

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Table 3 – B415.1 Efficiency and CO Emissions

Run

HHV Efficiency (%)

LHV Efficiency (%)

CO Emissions (g/MJ Output)

CO Emissions (g/kg Dry Fuel)

CO Emissions (g/hr)

1

N/A*

N/A*

N/A*

N/A*

N/A*

2

69.5

75.1

4.44

61.12

77.23

3

69.7

75.3

5.60

77.33

82.08

4

65.4

70.7

2.11

27.37

68.51

5

N/A*

N/A*

N/A*

N/A*

N/A*

6

70.5

76.2

5.96

83.26

106.07

7

69.7

75.3

7.99

110.26

95.57

Weighted average HHV efficiency of 4 test runs: 68.6%. *No results computed due to ceased combustion prior to test completion † Results excluded from weighted average due to unacceptable sampling train variation.

Table 4 – Test Facility Conditions Room Temperature (°F)

Barometric Pressure (Hg)

Air Velocity (ft/min)

Run

Before

After

Before

After

Before

After

1

72

N/A*

30.08

N/A*

<50

N/A*

2

70

70

30.34

30.32

<50

<50

3

71

70

30.21

30.19

<50

<50

4

73

74

30.19

30.18

<50

<50

5

71

N/A*

30.24

N/A*

<50

N/A*

6

74

74

30.24

30.22

<50

<50

7 68 69 30.20 30.14 *No data collected due to ceased combustion prior to test completion

<50

<50

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Table 5 – Fuel Measurement and Crib Description Summary – PRETEST Run

Pretest Fuel Weight (Starting weight in lbs)

Pretest Moisture (Dry basis - %)

Coal Bed Weight (lbs)

1

8.7

22.9

1.5

2

7.8

20.7

1.6

3

8.7

21.2

1.6

4

8.1

22.6

1.7

5

10.2

20.2

1.7

6

7.7

22.0

1.5

7

10.5

22.7

1.5

Table 6 – Fuel Measurement and Crib Description Summary – TEST

Run

Test Fuel Wet Basis (lbs)

Firebox Volume (ft3)

Fuel Loading Density Wet Basis (lbs/ft3)

Test Fuel Dry Basis (lbs)

Piece Length (in)

2x4s Used

4x4s Used

1

6.1

0.90

6.78

5.1

14.5

3

0

2

6.4

0.90

7.11

5.3

14.5

3

0

3

6.3

0.90

7.00

5.3

14.5

3

0

4

6.6

0.90

7.33

5.4

14.5

3

0

5

6.8

0.90

7.56

5.6

14.5

3

0

6

6.3

0.90

7.00

5.2

14.5

3

0

7

6.0

0.90

6.67

4.9

14.5

3

0

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Table 7 â&#x20AC;&#x201C; Dilution Tunnel Gas Measurements and Sampling Data Summary Average Dilution Tunnel Gas Measurements Run

Length of Test (min)

Velocity (ft/sec)

Flow Rate (dscf/min)

Temperature (°F)

1

N/A*

N/A*

N/A*

N/A*

2

112

14.13

158.4

91

3

134

14.30

161.3

85

4

59

14.21

150.9

119

5

N/A*

N/A*

N/A*

N/A*

6

111

13.10

146.7

90

7 154 13.44 152.1 *No results computed due to ceased combustion prior to test completion

83

Table 8 - Average Temperature Data Run

Beginning Surface Temperature Averagea

Ending Surface Temperature Averagea

Surface Delta Tb

1

319.2

N/A*

N/A*

2

410.9

319.4

91.5

3

413.1

301.6

111.5

4

392.8

422.6

29.8

5

304.1

6

364.3

N/A* 326.3

N/A* 38.0

7 351.1 270.1 81.0 a. All temperatures are in degrees F. b. Represents the difference between beginning and ending average surface temperatures. *No results computed due to ceased combustion prior to test completion

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Table 9 – Pretest Configuration Run

Combustion Air

Fuel Added

Fuel Removed

Time (min)

1

Open 2mm

None

None

60

2

Open 5mm

None

None

60

3

Open 4mm

None

None

67

4

Fully Open

None

None

84

5

Open 3mm

None

0.2lb @ ET=46:00

61

6

Open 5mm

None

None

60

7

Open 3mm

None

None

62

Table 10 – Test Configurations Run 1

2

3

4

5

6

7

Fuel Loading: Door: Auxilliary Air: Primary Air: Fuel Loading: Door: Auxilliary Air: Primary Air: Fuel Loading: Door: Auxilliary Air: Primary Air: Fuel Loading: Door: Auxilliary Air: Primary Air: Fuel Loading: Door: Auxilliary Air: Primary Air: Fuel Loading: Door: Auxilliary Air: Primary Air: Fuel Loading: Door: Auxilliary Air: Primary Air:

Five-Minute Startup Procedures Completed by ET = 0:15 Closed at ET = 0:25 Fully open until ET = 1:30 , Closed 10mm until ET = 2:00 Fully open until ET= 3:30, Closed slowly until ET =4:30 Completed by ET = 0:15 Closed at ET = 0:20 Fully open until ET = 2:00, Closed 10mm until ET = 3:30 Fully open until ET= 4:30, Closed slowly until ET =5:00 Completed by ET = 0:15 Closed at ET = 0:18 Fully open until ET = 1:30, Closed 10mm until ET = 2:30 Fully open until ET= 4:00, Closed slowly until ET =5:00 Completed by ET = 0:18 Closed at ET = 0:22 Fully open until ET = 1:30, Closed 10mm until ET = 2:30 Set at ET = 2:30 Completed by ET = 0:25 Closed at ET = 0:30 Fully open until ET = 2:00 , Closed 10mm until ET = 3:00 Fully open until ET= 4:30, Closed slowly until ET =5:00 Completed by ET = 0:20 Closed at ET = 0:25 Fully open until ET = 1:30 , Closed 10mm until ET = 2:30 Fully open until ET= 4:00, Closed slowly until ET =5:00 Completed by ET = 0:15 Closed at ET = 0:20 Fully open until ET = 1:30 , Closed 10mm until ET = 2:30 Fully open until ET= 4:00, Closed slowly until ET =5:00

Combustion Air Open 2 mm from fully closed Open 5 mm from fully closed Open 4 mm from fully closed

Fully open

Open 3 mm from fully closed Open 5 mm from fully closed Open 3 mm from fully closed

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Section 2 Photographs/Appliance Description/Drawings

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

RAIS A/S Q-Tee II Steel

Test Dates: 10/19/2015 â&#x20AC;&#x201C; 20/26/2015

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

RAIS A/S Q-Tee II Steel Run 1 – Fuel

Run 1  Newly Loaded Stove

Run 2 – Fuel

Run 2  Newly Loaded Stove

Run 3 – Fuel

Run 3  Newly Loaded Stove

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 4 – Fuel

Run 4  Newly Loaded Stove

Run 5 – Fuel

Run 5  Newly Loaded Stove

Run 6 – Fuel

Run 6  Newly Loaded Stove

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 7 – Fuel

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Run 7  Newly Loaded Stove

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

WOOD HEATER DESCRIPTION Appliance Manufacturer: RAIS A/S Wood Stove Model: Q-Tee II Steel Type: Freestanding, non-catalytic woodstove WOOD HEATER INFORMATION Materials of Construction: The unit is constructed primarily of mild steel. The firebox is lined with vermiculite insulation. The feed door has a 17” x 16” ceramic glass panel and ½” gasket. Air Introduction System: The wood heater has four air introduction systems: primary, secondary, pilot, and auxiliary startup. The secondary and pilot systems are fixed and non-adjustable, while the primary and auxiliary are user-adjustable via a single adjustment handle. The primary air system draws air through the bottom of the unit and into the firebox via an opening across the top of the loading door. The secondary air system draws air through the bottom of the unit to intake holes in the back of the firebox. Air is routed from these holes through the vermiculite firebox lining, with exit holes into the firebox chamber in the rear of the firebox and in the front of the main baffle. The pilot introduces air supplied by the secondary system to the firebox through a ¼” diameter tube located in the lower rear of the firebox. The auxiliary startup air draws air through the bottom of the firebox, and routes it into the firebox through the ash grate. Combustion Control Mechanisms: A single air slide handle controls both the auxiliary air and primary air adjustment. Users are alerted to the point at which auxiliary air is fully closed and primary air fully open by a positive-engagement point midway through the full range of adjustment. Combustor: None. Internal Baffles: The unit features two vermiculite baffles to route flue gas. The main, lower baffle contains secondary air holes, while the upper baffle is solid.

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Other Features: The unit features an ash cleanout grate which empties into a removable cleanout drawer located beneath the firebox. The grate includes a lower “shaker” grate which is operated by a handle that can be accessed only while the loading door is open Flue Outlet: The 6” diameter flue outlet is located in the top of the unit. WOOD HEATER OPERATING INSTRUCTIONS Specific Written Instructions: See Section 4 of this report. All markings and instruction materials were reviewed for content prior to printing.

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Model: Q-Tee II Steel RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Engineering Drawings/Blueprints [Redacted]

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Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Section 3 Test Data by Run

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Page 1 of 1

EPA Weighted Average Emissions EPA Method 28 Client: Stove Model: Test Dates: Project Number: Tracking Number:

Rais Q-Tee II 10/20/15 - 10/23/15 0138WS016E 2138

Weighted Averages

Emissions (g/hr): HHV Efficeincy (%): LHV Efficeincy (%):

0.9 68.6 74.2

Emission Rate Plot

1.20 Particulate Emissions (g/hr)

Status: Final Stove Type: Non-Catalytic Stove

1.00 0.80 0.60 0.40 0.20 0.00

0.00

0.50

1.00

1.50

2.00

2.50

3.00

Burn Rate (kg/hr dry)

Run # Burn Rate (dry kg/hr) Category LHV Efficiency (%) HHV Efficiency (%) Emissions (g/hr) Weighting Factor

7 0.87 2 75.3 69.7 0.91 0.428

25.30%

Run # Burn Rate (dry kg/hr) Category LHV Efficiency (%) HHV Efficiency (%) Emissions (g/hr) Weighting Factor

3 1.07 2 75.3 69.7 0.55 0.328

19.40%

Run # Burn Rate (dry kg/hr) Category LHV Efficiency (%) HHV Efficiency (%) Emissions (g/hr) Weighting Factor

2 1.28 3 75.1 69.5 1.13 0.537

31.71%

Run # Burn Rate (dry kg/hr) Category LHV Efficiency (%) HHV Efficiency (%) Emissions (g/hr) Weighting Factor

4 2.51 4 70.7 65.4 0.69 0.399

23.59%

Document Control No. P-SSF-0008 (EPA Method 28 Weighted Average Emissions).xls, Effective Date: 12/15/2010

Weighted Average Sheet

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Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 1

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Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

1 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 19-Oct-15 13:06

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.08 OMNI Equipment Numbers:

195 1

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34

0.000 0.103 0.219 0.336 0.451 0.567 0.684 0.800 0.915 1.031 1.146 1.261 1.378 1.493 1.607 1.722 1.837 1.951 2.065 2.179 2.294 2.410 2.525 2.641 2.757 2.873 2.989 3.105 3.220 3.336 3.452 3.568 3.684 3.799 3.914

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3) 0.000 0.127 0.261 0.395 0.529 0.663 0.797 0.931 1.064 1.198 1.332 1.464 1.598 1.731 1.864 1.997 2.130 2.263 2.397 2.529 2.662 2.795 2.928 3.061 3.194 3.327 3.460 3.592 3.726 3.859 3.992 4.125 4.258 4.391 4.525

0.10 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.11 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.01 1.23 1.21 1.22 1.22 1.22 1.21 1.22 1.21 1.22 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.21 1.20 1.20 1.21 1.20 1.19 1.21 1.20 1.19 1.21 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.21

75 75 75 75 75 76 76 76 76 76 77 77 77 77 78 78 78 78 78 79 79 79 79 80 80 80 80 80 80 81 81 81 81 81 81

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.037

0.041

0.049

0.039

0.036

0.051

0.044

0.031

0.049

85

85

85

85

85

85

85

85

85

Vstrav

13.71

ft/sec

Vscent

14.87

ft/sec

Fp

0.922

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

13.62 152.4 155.0 N/A N/A 20.37

in. Hg in. Hg

Velocity Traverse Data

30.08 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.370 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

0.55 0.52 0.53 0.52 0.53 0.53 0.53 0.53 0.53 0.53 0.54 0.53 0.54 0.53 0.53 0.54 0.54 0.54 0.53 0.54 0.53 0.54 0.54 0.54 0.54 0.53 0.53 0.53 0.53 0.53 0.53 0.53 0.54 0.53 0.53

0.02 1.32 1.32 1.33 1.33 1.32 1.33 1.33 1.31 1.32 1.32 1.31 1.31 1.31 1.31 1.31 1.30 1.31 1.30 1.30 1.31 1.30 1.30 1.31 1.29 1.30 1.30 1.29 1.30 1.30 1.30 1.31 1.29 1.30 1.30

74 74 74 74 74 74 75 75 75 75 75 75 75 76 76 76 76 77 77 77 77 77 78 78 78 78 78 78 79 79 79 79 79 79 79

0.7 0.7 0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0.7 0.6 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

85 98 102 100 98 93 90 88 87 86 85 84 84 83 83 83 82 82 82 82 82 82 82 81 81 81 81 81 81 80 80 80 80 80 80

Dilution Tunnel Center dP 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049

Page 1 of 6

Pro. Rate 1

Pro. Rate 2

92 104 104 102 103 103 102 101 102 101 101 102 101 100 100 100 99 99 99 100 101 100 101 101 101 101 101 100 100 100 100 100 100 100

99 104 104 104 104 103 103 102 103 103 101 102 101 101 101 101 101 102 100 101 101 101 101 101 101 101 100 101 101 101 101 101 101 101

Scale Weight Reading Change 6.1 6.0 5.8 5.7 5.6 5.4 5.5 5.4 5.4 5.4 5.3 5.3 5.2 5.3 5.2 5.2 5.2 5.1 5.1 5.1 5.0 5.0 4.9 5.0 4.9 4.9 4.8 4.8 4.8 4.8 4.7 4.7 4.7 4.7 4.6

-0.1 -0.2 -0.1 -0.1 -0.2 0.1 -0.1 0 0 -0.1 0 -0.1 0.1 -0.1 0 0 -0.1 0 0 -0.1 0 -0.1 0.1 -0.1 0 -0.1 0 0 0 -0.1 0 0 0 -0.1

Temperature Data (°F) Avg. Stove Surface Temp 319.2 316.1 315.1 316.3 318.0 319.7 320.4 320.6 320.2 319.0 317.5 315.8 314.1 311.9 309.3 307.4 304.8 302.4 299.6 297.5 295.0 292.9 290.6 288.3 286.0 283.9 281.6 279.8 277.8 275.7 274.0 272.1 270.3 268.3 266.6

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

288 327 428 432 414 353 305 277 260 248 240 233 228 224 220 217 213 210 207 204 201 199 197 195 193 191 189 187 186 184 183 181 179 178 176

72 73 73 73 74 73 73 73 73 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 73 73 73 73 73 73 73 73

73 74 75 76 76 75 75 75 75 75 75 75 75 75 75 75 75 75 74 75 75 74 74 75 74 74 74 74 74 74 74 74 74 74 74

73 73 73 73 73 73 74 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73

-0.077 -0.084 -0.097 -0.089 -0.087 -0.079 -0.075 -0.073 -0.071 -0.070 -0.069 -0.068 -0.067 -0.066 -0.066 -0.066 -0.065 -0.064 -0.063 -0.063 -0.062 -0.062 -0.061 -0.061 -0.061 -0.060 -0.059 -0.059 -0.059 -0.058 -0.058 -0.057 -0.057 -0.057 -0.057

1.5 3.6 8.9 8.4 8.6 7.3 3.8 2.1 1.8 1.6 1.5 1.5 1.5 1.5 1.5 1.6 1.6 1.6 1.6 1.7 1.7 1.7 1.7 1.8 1.8 1.8 1.9 1.9 2 2 2 2.1 2.1 2.1 2.2

0.3 0.5 0.3 0.3 0.4 0.7 0.7 0.5 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.8 0.8 0.8 0.8 0.8 0.9 0.9 0.9 0.9 0.9 0.9 1 1 1 1 1.1 1.1 1.1 1.2 1.2

Run 1 - Fire Out.xls

24


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

1 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 19-Oct-15 13:06

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.08 OMNI Equipment Numbers:

195 1

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69

4.031 4.146 4.262 4.378 4.493 4.607 4.723 4.838 4.952 5.066 5.179 5.295 5.412 5.528 5.644 5.760 5.876 5.992 6.109 6.225 6.341 6.457 6.572 6.688 6.805 6.920 7.040 7.157 7.273 7.390 7.506 7.621 7.737 7.853 7.968

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3) 4.657 4.791 4.924 5.057 5.190 5.323 5.456 5.590 5.722 5.856 5.989 6.122 6.255 6.388 6.522 6.655 6.788 6.921 7.055 7.188 7.321 7.455 7.587 7.721 7.854 7.987 8.121 8.254 8.387 8.520 8.653 8.786 8.919 9.052 9.185

0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.11 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.19 1.20 1.20 1.20 1.21 1.20 1.20 1.20 1.20 1.20 1.19 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.19 1.20 1.33 1.20 1.22 1.21 1.21 1.21 1.21 1.21 1.20

81 82 82 82 82 82 82 82 82 82 82 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.037

0.041

0.049

0.039

0.036

0.051

0.044

0.031

0.049

85

85

85

85

85

85

85

85

85

Vstrav

13.71

ft/sec

Vscent

14.87

ft/sec

Fp

0.922

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

13.62 152.4 155.0 N/A N/A 20.37

in. Hg in. Hg

Velocity Traverse Data

30.08 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.370 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.53 0.53 0.53 0.54 0.54 0.53 0.54 0.53 0.53 0.52 0.54 0.53 0.52 0.53 0.52 0.53 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.53 0.52 0.64 0.53 0.53 0.53 0.53 0.53 0.54 0.53 0.53

1.30 1.30 1.30 1.30 1.30 1.30 1.30 1.29 1.30 1.30 1.30 1.30 1.30 1.29 1.30 1.30 1.29 1.30 1.30 1.30 1.30 1.29 1.30 1.30 1.29 1.30 1.30 1.29 1.30 1.29 1.29 1.30 1.29 1.29 1.30

80 80 80 80 80 80 80 80 80 80 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

80 80 80 79 80 79 79 79 79 79 79 79 78 78 78 78 79 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 77 78

0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049

101 99 100 100 99 98 100 99 98 98 98 100 101 100 100 100 100 100 101 100 100 100 99 100 101 99 103 101 100 101 100 99 100 100 99

100 101 100 100 100 100 100 101 100 101 100 100 100 100 101 100 100 100 101 100 100 101 99 101 100 100 101 100 100 100 100 100 100 100 100

Page 2 of 6

Scale Weight Reading Change 4.6 4.6 4.5 4.5 4.5 4.5 4.4 4.4 4.3 4.3 4.3 4.3 4.2 4.2 4.2 4.1 4.1 4.1 4.0 4.0 3.9 3.9 3.9 3.8 3.8 3.8 3.8 3.7 3.6 3.6 3.6 3.5 3.5 3.5 3.4

0 0 -0.1 0 0 0 -0.1 0 -0.1 0 0 0 -0.1 0 0 -0.1 0 0 -0.1 0 -0.1 0 0 -0.1 0 0 0 -0.1 -0.1 0 0 -0.1 0 0 -0.1

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

265.1 263.5 261.9 260.5 258.9 257.4 256.1 254.7 253.5 252.3 251.1 249.7 248.8 247.5 246.5 245.6 244.4 243.3 242.6 241.7 240.5 239.7 239.0 238.2 237.4 237.0 236.1 235.4 235.0 234.3 233.9 233.3 232.8 232.5 232.0

175 174 172 172 170 169 168 167 167 165 165 164 164 163 162 162 161 161 160 160 159 158 158 158 158 158 157 157 157 156 156 155 155 155 155

73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 72 72 72 72 72 72 72 73 74 74 74 73 73 73 73

74 74 74 74 74 74 74 74 74 74 74 74 74 74 73 73 73 73 73 73 73 73 73 73 73 73 73 72 72 72 72 72 72 72 72

73 73 73 72 72 72 72 73 72 73 72 72 72 72 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71

-0.056 -0.056 -0.055 -0.055 -0.055 -0.055 -0.054 -0.054 -0.054 -0.054 -0.054 -0.053 -0.053 -0.053 -0.053 -0.053 -0.053 -0.052 -0.052 -0.052 -0.052 -0.052 -0.051 -0.051 -0.051 -0.051 -0.051 -0.051 -0.051 -0.051 -0.051 -0.051 -0.051 -0.050 -0.050

2.3 2.2 2.3 2.3 2.4 2.4 2.3 2.6 2.5 2.5 2.6 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.7 2.7 2.7 2.9 2.8 2.8 2.9 2.9 3 3.1 3 3.2 3.2 3.1 3.1 3.2 3.1

1.2 1.2 1.2 1.3 1.3 1.3 1.3 1.4 1.4 1.4 1.4 1.4 1.4 1.5 1.5 1.5 1.5 1.5 1.6 1.5 1.5 1.6 1.6 1.6 1.6 1.7 1.7 1.8 1.8 1.9 1.9 1.8 1.8 1.9 1.9

Run 1 - Fire Out.xls

25


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

1 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 19-Oct-15 13:06

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.08 OMNI Equipment Numbers:

195 1

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104

8.083 8.198 8.312 8.428 8.546 8.663 8.779 8.895 9.011 9.127 9.244 9.361 9.477 9.593 9.710 9.825 9.941 10.058 10.174 10.290 10.407 10.523 10.639 10.753 10.869 10.985 11.100 11.214 11.329 11.443 11.560 11.677 11.793 11.909 12.025

9.318 9.451 9.584 9.717 9.849 9.983 10.115 10.248 10.380 10.514 10.646 10.779 10.911 11.044 11.177 11.309 11.442 11.574 11.707 11.840 11.973 12.105 12.237 12.370 12.503 12.636 12.768 12.900 13.033 13.166 13.299 13.430 13.563 13.696 13.829

Control No. P-SSAR-0001

0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.11 0.12 0.11 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.21 1.21 1.20 1.21 1.21 1.21 1.20 1.21 1.21 1.21 1.21 1.19 1.20 1.21 1.21 1.21 1.21 1.21 1.20 1.19 1.21 1.20 1.21 1.21 1.20 1.19 1.21 1.21 1.21 1.21 1.20 1.21 1.20 1.21 1.20

83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 82 82 82 82 82 82

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.037

0.041

0.049

0.039

0.036

0.051

0.044

0.031

0.049

85

85

85

85

85

85

85

85

85

Vstrav

13.71

ft/sec

Vscent

14.87

ft/sec

Fp

0.922

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

13.62 152.4 155.0 N/A N/A 20.37

in. Hg in. Hg

Velocity Traverse Data

30.08 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.370 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.53 0.53 0.53 0.53 0.53 0.53 0.53 0.53 0.52 0.53 0.53 0.53 0.53 0.53 0.53 0.52 0.53 0.53 0.53 0.52 0.52 0.52 0.53 0.53 0.53 0.53 0.52 0.52 0.53 0.52 0.52 0.52 0.52 0.52 0.52

1.28 1.30 1.28 1.29 1.29 1.29 1.29 1.29 1.28 1.29 1.29 1.28 1.29 1.28 1.29 1.29 1.28 1.29 1.28 1.29 1.28 1.29 1.29 1.28 1.29 1.28 1.28 1.28 1.27 1.29 1.27 1.28 1.28 1.28 1.28

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 76 76 76 76 76 76 76 76 76 76 76 76

0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049

99 99 98 100 102 101 100 100 100 100 101 101 100 100 101 99 100 101 100 100 101 100 100 98 100 100 99 98 99 98 101 101 100 100 100

100 100 100 100 99 101 99 100 99 101 99 100 99 100 100 99 100 99 100 100 100 99 99 100 100 100 99 99 100 100 100 98 100 100 100

Page 3 of 6

Scale Weight Reading Change 3.4 3.3 3.3 3.3 3.2 3.2 3.1 3.1 3.0 3.0 3.0 3.2 2.9 2.9 2.8 2.8 2.8 2.7 2.7 2.7 2.7 2.7 2.6 2.6 2.6 2.6 2.5 2.5 2.5 2.5 2.5 2.4 2.4 2.4 2.4

0 -0.1 0 0 -0.1 0 -0.1 0 -0.1 0 0 0.2 -0.3 0 -0.1 0 0 -0.1 0 0 0 0 -0.1 0 0 0 -0.1 0 0 0 0 -0.1 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

231.6 231.4 231.0 230.7 230.3 230.0 229.8 229.6 229.4 229.1 229.0 229.0 228.7 228.9 228.8 228.8 228.6 228.9 228.6 228.4 228.2 228.2 228.0 228.0 227.5 227.5 227.2 226.9 226.8 226.7 226.5 226.4 226.5 226.3 226.1

154 154 154 154 154 154 154 153 153 153 153 152 149 147 145 144 144 143 142 140 139 138 137 137 136 135 135 134 134 134 133 132 132 131 131

73 73 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71

72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 71 71 71 71 71 71 71 71 71 71 71

71 71 71 70 70 70 70 71 71 71 71 71 71 71 71 71 70 71 71 71 71 71 71 71 71 71 71 71 71 70 71 71 71 71 71

-0.050 -0.050 -0.050 -0.050 -0.050 -0.050 -0.050 -0.050 -0.050 -0.050 -0.050 -0.050 -0.049 -0.049 -0.049 -0.048 -0.048 -0.048 -0.048 -0.048 -0.048 -0.047 -0.047 -0.047 -0.046 -0.047 -0.047 -0.047 -0.046 -0.046 -0.046 -0.046 -0.046 -0.046 -0.046

3.1 3.1 3.2 3.1 3.2 3.1 3.2 3.2 3.2 3.3 3.1 3.3 3.1 3 3 2.8 2.7 2.8 2.7 2.6 2.6 2.5 2.5 2.5 2.6 2.6 2.8 3.1 2.9 2.8 2.8 2.7 2.5 2.4 2.3

1.8 1.9 1.9 1.9 1.9 1.8 1.9 1.9 1.9 2 1.8 2 1.8 1.8 1.7 1.6 1.5 1.5 1.4 1.4 1.4 1.3 1.3 1.3 1.3 1.1 1.1 1.1 1 1.1 1 1 1.2 1.2 1.2

Run 1 - Fire Out.xls

26


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

1 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 19-Oct-15 13:06

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.08 OMNI Equipment Numbers:

195 1

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126 127 128 129 130 131 132 133 134 135 136 137 138 139

12.141 12.257 12.374 12.491 12.607 12.723 12.839 12.955 13.071 13.188 13.303 13.420 13.536 13.652 13.767 13.883 13.998 14.113 14.228 14.342 14.456 14.573 14.690 14.806 14.923 15.039 15.154 15.271 15.388 15.504 15.620 15.737 15.853 15.969 16.086

13.961 14.093 14.226 14.359 14.491 14.624 14.756 14.889 15.021 15.154 15.286 15.418 15.551 15.684 15.816 15.949 16.081 16.214 16.346 16.479 16.611 16.743 16.876 17.009 17.141 17.273 17.406 17.539 17.671 17.804 17.936 18.068 18.201 18.334 18.466

Control No. P-SSAR-0001

0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.21 1.21 1.20 1.20 1.21 1.20 1.21 1.21 1.20 1.21 1.20 1.21 1.21 1.21 1.21 1.20 1.20 1.20 1.20 1.21 1.21 1.19 1.21 1.20 1.21 1.21 1.20 1.21 1.20 1.21 1.20 1.21 1.21 1.21 1.21

82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.037

0.041

0.049

0.039

0.036

0.051

0.044

0.031

0.049

85

85

85

85

85

85

85

85

85

Vstrav

13.71

ft/sec

Vscent

14.87

ft/sec

Fp

0.922

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

13.62 152.4 155.0 N/A N/A 20.37

in. Hg in. Hg

Velocity Traverse Data

30.08 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.370 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.52 0.52 0.53 0.53 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.53 0.52 0.53 0.53 0.52 0.53 0.52 0.52 0.52 0.52 0.52 0.52 0.53 0.52 0.52 0.52 0.53 0.53 0.52 0.52 0.53 0.52 0.52 0.52

1.27 1.28 1.28 1.28 1.28 1.29 1.29 1.28 1.28 1.28 1.29 1.28 1.29 1.28 1.28 1.29 1.28 1.29 1.28 1.29 1.29 1.28 1.29 1.28 1.28 1.29 1.28 1.29 1.28 1.29 1.29 1.28 1.28 1.29 1.29

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 75 76 75 76 75 76 76 76 76 76 75 75 75 75 75 75 75

0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049

100 100 101 101 100 100 100 100 100 101 99 101 100 100 99 100 99 99 99 98 98 101 101 100 101 100 99 101 101 100 100 101 100 100 101

99 99 100 100 99 100 99 100 99 100 99 99 100 100 99 100 99 100 99 100 99 99 100 100 99 99 100 100 99 100 99 99 100 100 99

Page 4 of 6

Scale Weight Reading Change 2.4 2.4 2.3 2.3 2.3 2.4 2.3 2.3 2.3 2.3 2.2 2.3 2.3 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.1

0 0 -0.1 0 0 0.1 -0.1 0 0 0 -0.1 0.1 0 -0.1 0 0 0 0 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

225.8 225.7 225.4 225.1 224.6 224.3 223.9 223.6 223.0 222.6 222.4 221.9 221.5 221.1 220.6 220.2 219.5 219.3 218.7 218.1 217.6 217.0 216.7 216.1 215.7 215.3 214.8 214.1 213.7 213.3 212.9 212.6 212.3 211.8 211.3

130 130 130 129 129 129 128 128 127 127 127 126 125 125 125 124 124 124 124 123 123 122 122 121 121 121 121 120 120 121 120 120 120 120 119

71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71

71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71

71 71 71 71 71 70 71 70 70 71 71 71 71 71 70 71 71 70 71 70 71 71 71 71 71 70 70 70 71 70 71 70 70 70 70

-0.046 -0.045 -0.045 -0.045 -0.045 -0.045 -0.045 -0.045 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.042 -0.042 -0.042 -0.042 -0.042

2.4 2.4 2.4 2.3 2.3 2.3 2.4 2.3 2.3 2.3 2.2 2.3 2.2 2.2 2.1 2.1 2.1 2.1 2 2.1 2 2 2.1 2.1 2.1 2.1 2 2 2 2 2.1 1.9 2 2 2

1.2 1.2 1.2 1.1 1.2 1.2 1.2 1.2 1.1 1.2 1.1 1.1 1.1 1.1 1.1 1 1.1 1.1 1 1.1 1 1 1.1 1.1 1.1 1.1 1.1 1.1 1 1.1 1.1 1 1 1.1 1.1

Run 1 - Fire Out.xls

27


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

1 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 19-Oct-15 13:06

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.08 OMNI Equipment Numbers:

195 1

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

140 141 142 143 144 145 146 147 148 149 150 151 152 153 154 155 156 157 158 159 160 161 162 163 164 165 166 167 168 169 170 171 172 173 174

16.202 16.318 16.434 16.551 16.667 16.782 16.899 17.014 17.129 17.245 17.360 17.474 17.588 17.705 17.822 17.938 18.054 18.170 18.286 18.403 18.520 18.637 18.753 18.870 18.986 19.101 19.218 19.335 19.451 19.567 19.684 19.800 19.915 20.032 20.147

18.598 18.731 18.864 18.997 19.129 19.261 19.394 19.526 19.659 19.791 19.924 20.057 20.189 20.322 20.454 20.586 20.719 20.852 20.985 21.117 21.249 21.382 21.515 21.648 21.780 21.912 22.045 22.178 22.310 22.442 22.575 22.707 22.840 22.973 23.105

Control No. P-SSAR-0001

0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.11 0.12 0.12 0.11 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.11

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.21 1.20 1.21 1.20 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.21 1.22 1.21 1.21 1.21

82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.037

0.041

0.049

0.039

0.036

0.051

0.044

0.031

0.049

85

85

85

85

85

85

85

85

85

Vstrav

13.71

ft/sec

Vscent

14.87

ft/sec

Fp

0.922

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

13.62 152.4 155.0 N/A N/A 20.37

in. Hg in. Hg

Velocity Traverse Data

30.08 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.370 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.52 0.52 0.53 0.52 0.53 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.53 0.53 0.52 0.52 0.52 0.53 0.53 0.52 0.53 0.52 0.52 0.53 0.52 0.52 0.52 0.53 0.53 0.52

1.29 1.28 1.29 1.29 1.28 1.29 1.28 1.29 1.28 1.28 1.29 1.28 1.29 1.28 1.28 1.29 1.28 1.29 1.28 1.28 1.29 1.29 1.29 1.28 1.29 1.29 1.28 1.28 1.28 1.28 1.29 1.28 1.28 1.29 1.28

81 81 81 81 81 81 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 81 80 81 81 81 81 81 81 81 81 81

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75

0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049

100 100 100 101 100 99 101 99 99 100 99 98 98 101 101 100 100 100 100 101 101 101 100 101 100 99 101 101 100 100 101 100 99 101 99

99 100 100 100 99 99 100 99 100 99 100 100 99 100 99 99 100 100 100 99 99 100 100 100 99 99 100 100 99 99 100 99 100 100 99

Page 5 of 6

Scale Weight Reading Change 2.1 2.1 2.1 2.0 2.0 2.1 2.1 2.1 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 2.0 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9

0 0 0 -0.1 0 0.1 0 0 -0.1 0 0 0 0 0 0 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 0 0 0 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

210.7 210.1 209.6 209.4 208.7 208.2 207.7 207.2 207.0 206.4 206.2 205.6 205.2 204.7 204.5 203.9 203.5 203.2 202.8 202.5 202.0 201.5 201.1 200.9 200.5 200.2 199.6 199.2 198.7 198.3 198.3 198.0 197.5 197.1 196.9

119 119 118 118 118 118 118 118 118 118 118 118 117 117 117 117 117 117 117 117 116 116 116 116 116 116 115 116 115 115 115 115 115 114 114

71 71 71 71 71 71 71 71 71 71 71 71 70 71 71 71 70 70 70 70 70 70 70 70 70 70 71 70 71 71 71 71 71 71 71

71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71

70 71 71 71 70 70 70 70 70 70 70 70 70 70 71 70 71 70 70 70 70 71 70 71 70 70 71 70 71 70 70 70 70 71 70

-0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041

2 2 2 2 2 2 2 2 2 2 2 2 2.1 2 2 2 2 2 2 2 2 2 2 2 2 2 2.1 2 2.1 2 2.1 2.1 2 2.1 2.2

1.1 1.1 1.1 1.1 1.1 1 1.1 1.1 1.1 1 1 1.1 1.1 1 1.1 1.1 1 1.1 1.1 1 1.1 1.1 1 1 1 1 1.1 1 1.1 1.1 1.1 1.1 1.1 1.1 1.1

Run 1 - Fire Out.xls

28


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

1 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 19-Oct-15 13:06

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.08 OMNI Equipment Numbers:

195 1

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

175 176 177 178 179 180 181 182 183 184 185 186 187 188 189 190 191 192 193 194 195 Avg/Tot

20.262 20.378 20.493 20.607 20.721 20.839 20.956 21.072 21.189 21.305 21.421 21.537 21.655 21.771 21.888 22.004 22.120 22.237 22.353 22.470 22.586 22.586

23.237 23.370 23.503 23.635 23.767 23.900 24.033 24.165 24.298 24.430 24.563 24.695 24.828 24.960 25.093 25.225 25.358 25.490 25.623 25.756 25.888 25.888

Control No. P-SSAR-0001

0.12 0.12 0.11 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.20 1.21 1.21 1.20 1.21 1.21 1.21 1.20 1.22 1.21 1.20 1.21 1.21 1.21 1.20 1.21 1.21 1.21 1.21 1.21 1.21 1.20

82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.037

0.041

0.049

0.039

0.036

0.051

0.044

0.031

0.049

85

85

85

85

85

85

85

85

85

Vstrav

13.71

ft/sec

Vscent

14.87

ft/sec

Fp

0.922

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

13.62 152.4 155.0 N/A N/A 20.37

in. Hg in. Hg

Velocity Traverse Data

30.08 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.370 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.52 0.52 0.52 0.52 0.52 0.53 0.52 0.52 0.52 0.53 0.53 0.53 0.53 0.52 0.52 0.52 0.53 0.52 0.52 0.52 0.52

1.29 1.29 1.28 1.29 1.28 1.29 1.28 1.28 1.29 1.28 1.29 1.29 1.28 1.29 1.28 1.29 1.28 1.29 1.29 1.28 1.29 1.28

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 80

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 78

0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049 0.049

99 100 99 98 98 102 101 100 101 100 100 100 102 100 101 100 100 101 100 101 100 100

99 100 100 99 99 100 100 99 100 99 100 99 100 99 100 99 100 99 100 100 99 100

Page 6 of 6

Scale Weight Reading Change 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9 1.9

0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0

Temperature Data (°F) Avg. Stove Surface Temp 196.6 196.2 196.1 195.7 195.5 195.2 195.1 194.8 194.3 194.1 193.8 193.5 193.2 193.1 192.9 192.5 192.4 192.1 191.8 191.8 191.5 127.7

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

115 114 114 114 114 114 114 114 114 114 114 114 113 113 113 114 113 113 113 113 113

71 71 70 71 71 70 71 70 70 71 71 70 71 70 71 70 70 70 70 70 70 72

71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 72

71 70 71 71 70 70 71 71 71 71 70 71 70 70 71 70 70 71 71 71 70 71

-0.041 -0.041 -0.041 -0.040 -0.041 -0.041 -0.041 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.041 -0.040 -0.040 -0.040 -0.049

2.2 2.3 2.3 2.3 2.2 2.3 2.3 2.3 2.3 2.1 2.3 2.3 2.3 2.3 2.2 2.3 2.2 2.2 2.2 2.3 2.3

1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.1 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2

Run 1 - Fire Out.xls

29


30


31


32


33


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 2

OMNI-Test Laboratories, Inc.

34


OMNI-Test Laboratories, Inc.

Wood Heater Test Results - ASTM E2780 / ASTM E2515 Manufacturer: Model: Project No.: Tracking No.: Run: Test Date:

Burn Rate Average Tunnel Temperature Average Gas Velocity in Dilution Tunnel - vs Average Gas Flow Rate in Dilution Tunnel - Qsd Average Delta p Total Time of Test

RAIS Q-Tee II 0138WS016E 2138 2 10/20/15

1.28 kg/hr dry 91 degrees Fahrenheit 14.13 feet/second 9501.2 dscf/hour 0.056 inches H20 112 minutes

AMBIENT Total Sample Volume - Vm Average Gas Meter Temperature Total Sample Volume (Standard Conditions) - Vmstd Total Particulates - mn Particulate Concentration (dry-standard) - Cr/Cs Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

0.000 cubic feet 70 degrees Fahrenheit 0.000 dscf 0 mg

SAMPLE TRAIN 1 12.893 cubic feet 79 degrees Fahrenheit 12.973 dscf 1.7 mg

SAMPLE TRAIN 2 14.900 cubic feet 77 degrees Fahrenheit 14.941 dscf 1.6 mg

FIRST HOUR FILTER (TRAIN 1) 6.873 cubic feet 78 degrees Fahrenheit 6.935 dscf 0.7 mg

0.000000 grams/dscf

0.00013 grams/dscf

0.00011 grams/dscf

0.00010 grams/dscf

0.00 grams 0.00 grams/hour

2.32 grams 1.25 grams/hour 0.98 g/kg

1.90 grams 1.02 grams/hour 0.80 g/kg

0.96 grams 0.96 grams/hour 0.46 g/kg

Difference from Average Total Particulate Emissions

0.21 grams

0.21 grams

Dual Train Comparison Results Are Acceptable Complete Test Run Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor First Hour Emissions Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

Control No. P-XXXX-XXXX

FINAL AVERAGE RESULTS 2.11 grams 1.13 grams/hour 0.89 grams/kg

0.96 grams 0.96 grams/hour 0.46 grams/kg

Run 2 - Cat III.xls

35


OMNI-Test Laboratories, Inc. Manufacturer: Rais Model: Q-Tee II Date: 10/20/15 Run: 2 Control #: 0138WS016E Test Duration: 112 Output Category: III

Technicians:

A. Kravitz

Test Results in Accordance with CSA B415.1-09 HHV Basis 69.5% 96.1% 72%

LHV Basis 75.1% 96.1% 78.2%

Output Rate (kJ/h) Burn Rate (kg/h) Input (kJ/h)

17,404 1.26 25,032

16,509 2.79 23,746

(Btu/h) (lb/h) (Btu/h)

Test Load Weight (dry kg) MC wet (%) MC dry (%) Particulate (g ) CO (g) Test Duration (h)

2.36 18.77 23.11 0 144 1.87

5.20

dry lb

Particulate 0.00 0.00 0.00 0.00

CO 4.44 61.12 77.23 10.31

Overall Efficiency Combustion Efficiency Heat Transfer Efficiency

Emissions g/MJ Output g/kg Dry Fuel g/h lb/MM Btu Output Air/Fuel Ratio (A/F) VERSION:

2.3

14.43 3/23/2010

36


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

2 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 20-Oct-15 11:31

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.34

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

112 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.34

30.32

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34

0.000 0.102 0.217 0.332 0.445 0.560 0.674 0.788 0.901 1.013 1.129 1.244 1.359 1.473 1.588 1.703 1.818 1.933 2.047 2.162 2.277 2.392 2.507 2.621 2.736 2.851 2.966 3.081 3.195 3.310 3.424 3.538 3.653 3.766 3.880

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.33 "Hg

0.000 0.117 0.250 0.384 0.517 0.650 0.783 0.916 1.049 1.181 1.314 1.446 1.579 1.711 1.843 1.975 2.108 2.240 2.372 2.505 2.637 2.769 2.902 3.035 3.167 3.300 3.432 3.565 3.698 3.830 3.963 4.096 4.229 4.362 4.494

0.10 0.12 0.12 0.11 0.12 0.11 0.11 0.11 0.11 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.11 0.12 0.11 0.11 0.12 0.11 0.11

0.12 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 0.54 1.22 1.23 1.23 1.23 1.21 1.22 1.22 1.22 1.22 1.21 1.20 1.21 1.21 1.21 1.21 1.20 1.20 1.20 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.21 1.20 1.21 1.20 1.21 1.21 1.21 1.21 1.20

73 73 73 73 73 73 73 74 74 74 74 74 75 75 75 75 76 76 76 76 77 77 77 77 77 77 78 78 78 78 78 78 79 79 79

14.13 155.7 158.4

ft/sec. scfm scfm 0 cfm @ -4 0 cfm @ -4 23.11 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.030

0.047

0.054

0.042

0.040

0.051

0.053

0.029

0.056

92

92

92

92

92

92

92

92

92

Vstrav

14.14

ft/sec

Vscent

15.93

ft/sec

Fp

0.888

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.490 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

0.56 0.51 0.51 0.51 0.5 0.51 0.51 0.51 0.51 0.51 0.51 0.51 0.5 0.52 0.51 0.5 0.51 0.51 0.51 0.52 0.52 0.51 0.52 0.52 0.52 0.51 0.51 0.51 0.51 0.52 0.52 0.51 0.51 0.51 0.52

0.03 1.33 1.34 1.34 1.33 1.33 1.32 1.33 1.32 1.32 1.32 1.31 1.32 1.31 1.31 1.31 1.30 1.31 1.31 1.31 1.32 1.30 1.32 1.31 1.31 1.32 1.31 1.32 1.31 1.31 1.32 1.30 1.31 1.30 1.31

71 71 71 71 71 71 71 71 72 72 72 72 72 73 73 73 73 73 73 74 74 74 74 74 75 75 75 75 75 75 76 76 76 76 76

0.7 0.7 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

92 118 130 135 125 116 108 105 102 101 100 99 99 98 98 97 97 97 96 96 96 95 95 95 95 95 95 95 95 95 95 95 96 96 96

Dilution Tunnel Center dP 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056

Page 1 of 4

Pro. Rate 1

Pro. Rate 2

92 105 105 102 103 102 101 100 99 103 102 101 100 101 101 101 101 100 101 101 101 101 100 101 101 101 101 100 101 100 100 100 99 100

91 105 106 104 103 103 102 102 101 102 101 102 101 101 101 101 101 100 101 100 100 101 101 100 101 100 101 101 100 101 101 101 101 100

Scale Weight Reading Change 6.4 6.2 5.9 5.6 5.4 5.1 5.0 4.9 4.8 4.7 4.5 4.4 4.3 4.2 4.0 3.9 3.8 3.7 3.5 3.4 3.3 3.2 3.1 3.0 2.9 2.8 2.7 2.6 2.5 2.4 2.3 2.2 2.1 1.9 1.9

-0.2 -0.3 -0.3 -0.2 -0.3 -0.1 -0.1 -0.1 -0.1 -0.2 -0.1 -0.1 -0.1 -0.2 -0.1 -0.1 -0.1 -0.2 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.2 0

Temperature Data (°F) Avg. Stove Surface Temp 410.9 406.8 407.6 413.9 420.3 426.9 430.6 433.5 434.6 435.4 436.2 436.4 437.4 437.7 437.9 438.8 439.0 439.1 438.9 438.5 438.8 439.3 438.8 439.1 438.7 438.9 439.2 439.6 439.7 441.3 441.4 442.2 444.3 444.7 446.9

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

417 484 676 699 633 562 492 463 452 442 436 432 430 428 426 424 420 420 417 412 407 411 411 408 409 407 405 407 407 415 415 420 426 430 433

67 68 70 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 70 71 71 71 71 71 71 71 71 71

67 71 74 75 75 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 73 73 73 73 73 73 73 73 73 73 74 74 74 74 74

69 70 70 70 71 70 70 70 70 69 69 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 69 69 70 70 71 69 70 70 70

-0.096 -0.106 -0.114 -0.115 -0.108 -0.103 -0.100 -0.098 -0.096 -0.096 -0.096 -0.096 -0.095 -0.094 -0.095 -0.095 -0.094 -0.093 -0.092 -0.092 -0.093 -0.092 -0.092 -0.092 -0.093 -0.092 -0.093 -0.092 -0.091 -0.092 -0.093 -0.093 -0.094 -0.094 -0.094

5.3 4.2 10.3 12.7 12.7 11.3 9.9 9.2 8.9 8.9 9 9.3 9.2 9.4 9.5 9.3 9.3 9.1 9 9.1 9 9.1 9.3 9.5 9.5 9.5 9.6 9.6 9.7 9.8 10 10.3 10.5 10.5 10.5

0.1 0.1 0.6 1.9 1.2 0.4 0.3 0.4 0.4 0.4 0.5 0.4 0.3 0.3 0.3 0.4 0.4 0.4 0.4 0.3 0.3 0.3 0.3 0.3 0.3 0.4 0.3 0.3 0.3 0.4 0.4 0.5 0.5 0.7 0.7

Run 2 - Cat III.xls

37


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

2 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 20-Oct-15 11:31

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.34

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

112 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.34

30.32

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69

3.993 4.108 4.223 4.338 4.455 4.570 4.686 4.801 4.916 5.032 5.148 5.263 5.379 5.494 5.608 5.725 5.840 5.955 6.071 6.187 6.302 6.416 6.531 6.646 6.760 6.873 6.990 7.107 7.223 7.339 7.455 7.570 7.685 7.802 7.918

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.33 "Hg

4.627 4.760 4.893 5.025 5.158 5.291 5.424 5.556 5.689 5.823 5.956 6.089 6.222 6.355 6.488 6.621 6.754 6.888 7.021 7.154 7.287 7.420 7.554 7.687 7.820 7.954 8.087 8.220 8.354 8.487 8.621 8.754 8.887 9.021 9.154

0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.11 0.11 0.11 0.12 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.22 1.21 1.21 1.20 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.22 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.20 1.21 1.22 1.21 1.21 1.21

79 79 79 79 79 80 80 80 80 80 80 80 80 80 80 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

14.13 155.7 158.4

ft/sec. scfm scfm 0 cfm @ -4 0 cfm @ -4 23.11 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.030

0.047

0.054

0.042

0.040

0.051

0.053

0.029

0.056

92

92

92

92

92

92

92

92

92

Vstrav

14.14

ft/sec

Vscent

15.93

ft/sec

Fp

0.888

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.490 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.51 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.53 0.51 0.52 0.51 0.51 0.52 0.51 0.52 0.51 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.51 0.51 0.51 0.52 0.51 0.51 0.52 0.52 0.52 0.52 0.51

1.31 1.31 1.32 1.32 1.30 1.32 1.31 1.32 1.31 1.30 1.32 1.32 1.31 1.32 1.31 1.31 1.32 1.31 1.31 1.32 1.31 1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.32

76 76 77 77 77 77 77 77 77 77 77 78 78 78 78 78 78 78 78 78 78 78 78 78 79 78 79 79 79 79 79 79 79 79 79

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

96 96 96 96 95 95 94 94 93 93 93 92 92 91 91 91 90 90 89 89 88 88 88 88 88 87 87 87 86 86 86 86 86 85 85

0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056

99 100 100 100 102 100 101 100 100 101 101 100 101 100 99 101 100 100 100 100 99 98 99 99 98 98 101 101 100 100 100 99 99 101 100

101 101 100 100 100 100 100 100 100 101 100 100 100 100 100 100 100 100 100 100 100 100 100 100 99 100 99 99 100 99 100 99 99 100 99

Page 2 of 4

Scale Weight Reading Change 1.8 1.6 1.5 1.5 1.4 1.4 1.3 1.2 1.2 1.1 1.1 1.1 1.1 1.0 1.0 1.0 1.0 0.9 0.9 0.9 0.9 0.9 0.9 0.8 0.8 0.8 0.8 0.8 0.8 0.7 0.8 0.7 0.7 0.7 0.7

-0.1 -0.2 -0.1 0 -0.1 0 -0.1 -0.1 0 -0.1 0 0 0 -0.1 0 0 0 -0.1 0 0 0 0 0 -0.1 0 0 0 0 0 -0.1 0.1 -0.1 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

448.6 449.1 449.9 450.9 450.8 449.9 448.7 446.9 445.2 442.4 440.9 437.7 434.5 432.0 428.3 424.9 422.5 419.6 415.7 411.8 408.8 406.3 402.3 400.6 397.2 394.3 391.7 388.7 386.3 384.3 381.9 379.9 377.4 375.3 373.1

433 439 435 426 416 409 399 392 387 377 370 357 347 340 332 325 320 313 310 304 303 299 295 292 286 284 280 278 275 272 271 269 269 265 263

71 71 71 71 71 71 71 71 71 72 71 72 72 72 72 72 72 72 72 72 72 72 72 72 72 71 73 74 74 74 74 74 73 73 73

74 74 74 74 74 74 74 74 74 74 73 74 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 72

70 70 71 70 70 70 70 70 70 71 70 70 70 70 70 70 70 71 70 70 70 70 70 71 70 70 70 70 70 70 70 70 70 70 69

-0.094 -0.094 -0.093 -0.092 -0.092 -0.090 -0.089 -0.088 -0.087 -0.087 -0.085 -0.084 -0.084 -0.083 -0.082 -0.081 -0.080 -0.079 -0.078 -0.078 -0.077 -0.077 -0.076 -0.076 -0.075 -0.074 -0.074 -0.074 -0.073 -0.073 -0.072 -0.071 -0.071 -0.071 -0.071

10.4 10.2 10.2 9.7 9 8.1 7.6 7.7 7.6 7.4 7.1 6.5 6 5.8 5.7 5.6 5.5 5.3 5 5 5 5 5.1 5.1 5.1 5.2 5.1 5.1 5 4.9 5.1 5 5.1 5 5

0.6 0.4 0.3 0.2 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0 0.1 0.1 0.1 0.1 0.1 0.2 0.2 0.2 0.2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.4 0.4

Run 2 - Cat III.xls

38


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

2 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 20-Oct-15 11:31

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.34

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

112 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.34

30.32

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.33 "Hg

70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104

8.034 8.150 8.266 8.381 8.498 8.614 8.729 8.845 8.961 9.076 9.193 9.308 9.423 9.538 9.653 9.768 9.882 9.997 10.111 10.227 10.343 10.459 10.576 10.693 10.809 10.925 11.041 11.156 11.273 11.389 11.505 11.621 11.737 11.853 11.969

9.288 9.422 9.555 9.689 9.822 9.955 10.089 10.223 10.356 10.490 10.623 10.757 10.891 11.024 11.158 11.292 11.425 11.559 11.693 11.826 11.960 12.094 12.227 12.361 12.494 12.628 12.761 12.895 13.029 13.163 13.296 13.430 13.564 13.697 13.831

Control No. P-SSAR-0001

0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.21 1.22 1.21 1.21 1.20 1.21 1.22 1.21 1.21 1.22 1.20 1.22 1.22 1.21 1.22 1.21 1.21 1.22 1.21 1.22 1.22 1.21 1.20 1.22 1.21 1.22 1.22 1.22 1.22 1.22 1.20 1.22 1.21 1.22 1.22

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

14.13 155.7 158.4

ft/sec. scfm scfm 0 cfm @ -4 0 cfm @ -4 23.11 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.030

0.047

0.054

0.042

0.040

0.051

0.053

0.029

0.056

92

92

92

92

92

92

92

92

92

Vstrav

14.14

ft/sec

Vscent

15.93

ft/sec

Fp

0.888

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.490 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.52 0.52 0.52 0.51 0.52 0.52 0.51 0.52 0.51 0.52 0.51 0.52 0.52 0.52 0.52 0.51 0.52 0.52 0.52 0.52 0.51 0.52 0.51 0.52 0.51 0.52 0.52 0.52 0.51 0.51 0.51 0.52 0.52 0.51 0.52

1.32 1.32 1.32 1.32 1.31 1.31 1.32 1.32 1.31 1.32 1.32 1.32 1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.32 1.32 1.32 1.32 1.32 1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.32 1.32 1.31 1.32

79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

85 85 85 84 84 84 84 84 84 84 83 83 83 83 83 83 83 83 83 82 83 82 82 82 82 82 82 82 82 82 82 82 82 82 81

0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056

100 100 100 99 101 100 99 100 100 99 101 99 99 99 99 99 98 99 98 100 100 100 100 100 100 100 100 99 100 100 100 100 100 100 100

100 100 99 100 99 99 100 100 99 100 99 100 100 99 100 100 99 100 100 99 100 100 99 100 99 100 99 100 100 100 99 100 100 99 99

Page 3 of 4

Scale Weight Reading Change 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.4 0.4 0.4 0.4 0.4 0.4 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.2 0.2

0 -0.1 0 0 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 -0.1 0 0 0 0 0 0 -0.1 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

371.6 369.3 366.9 365.3 364.3 361.5 360.8 358.5 356.9 355.8 354.0 352.4 351.0 349.9 348.4 347.5 345.4 344.5 343.4 342.2 341.0 339.8 338.4 337.5 336.3 334.7 334.0 333.3 332.5 331.2 330.6 329.7 328.8 327.0 327.1

261 258 255 256 255 254 250 250 249 246 246 246 245 243 240 238 239 237 238 237 234 234 231 232 232 231 229 229 228 228 225 226 224 225 225

73 73 73 73 72 72 72 72 72 72 72 72 72 72 72 72 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71

72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 71 71 71 71 71 71 71 71 71 71 71 71

70 69 70 69 70 70 70 70 70 70 69 70 70 70 69 69 69 69 70 69 70 70 70 69 70 70 69 69 69 69 69 69 70 69 70

-0.070 -0.070 -0.070 -0.069 -0.069 -0.069 -0.068 -0.068 -0.067 -0.068 -0.067 -0.067 -0.066 -0.067 -0.067 -0.067 -0.066 -0.066 -0.065 -0.065 -0.065 -0.065 -0.065 -0.064 -0.064 -0.064 -0.064 -0.064 -0.064 -0.064 -0.063 -0.063 -0.063 -0.063 -0.063

5 5 4.9 4.9 4.9 4.9 5 5 5 5 4.9 5 4.9 4.9 4.9 4.9 4.8 4.7 4.8 4.7 4.7 4.7 4.6 4.7 4.7 4.8 4.7 4.7 4.7 4.7 4.6 4.6 4.6 4.6 4.6

0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.6 0.6 0.5 0.5 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

Run 2 - Cat III.xls

39


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

2 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 20-Oct-15 11:31

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.34

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

112 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.34

30.32

N/A

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.33 "Hg

105 106 107 108 109 110 111 112 Avg/Tot

12.085 12.201 12.317 12.433 12.548 12.662 12.778 12.893 12.893

13.965 14.098 14.232 14.366 14.499 14.633 14.767 14.900 14.900

Control No. P-SSAR-0001

0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.21 1.20 1.22 1.21 1.22 1.22 1.21 1.21 1.21

81 81 81 81 81 81 81 81 79

14.13 155.7 158.4

ft/sec. scfm scfm 0 cfm @ -4 0 cfm @ -4 23.11 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.030

0.047

0.054

0.042

0.040

0.051

0.053

0.029

0.056

92

92

92

92

92

92

92

92

92

Vstrav

14.14

ft/sec

Vscent

15.93

ft/sec

Fp

0.888

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.490 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.52 0.52 0.51 0.52 0.51 0.51 0.52 0.51

1.32 1.31 1.33 1.31 1.32 1.33 1.31 1.31 1.30

79 79 79 79 79 79 79 79 77

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

82 81 81 81 81 81 81 81 91

0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056

100 100 100 100 99 98 100 99 100

100 99 99 99 99 99 99 99 100

Page 4 of 4

Scale Weight Reading Change 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.0

0 0 0 0 0 0 0 -0.2

Temperature Data (°F) Avg. Stove Surface Temp 325.8 324.5 323.9 323.5 322.6 321.6 320.8 319.4 91.5

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

225 224 224 221 220 218 218 218

71 71 71 71 71 70 70 70 71

71 71 71 71 71 71 71 71 73

69 70 70 70 70 70 69 70 70

-0.063 -0.063 -0.063 -0.063 -0.062 -0.062 -0.063 -0.062 -0.080

4.5 4.5 4.5 4.5 4.4 4.4 4.3 4.3

0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.7

Run 2 - Cat III.xls

40


41


42


43


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 3

OMNI-Test Laboratories, Inc.

44


OMNI-Test Laboratories, Inc.

Wood Heater Test Results - ASTM E2780 / ASTM E2515 Manufacturer: Model: Project No.: Tracking No.: Run: Test Date:

Burn Rate Average Tunnel Temperature Average Gas Velocity in Dilution Tunnel - vs Average Gas Flow Rate in Dilution Tunnel - Qsd Average Delta p Total Time of Test

RAIS Q-Tee II 0138WS016E 2138 3 10/21/15

1.07 kg/hr dry 85 degrees Fahrenheit 14.30 feet/second 9676.7 dscf/hour 0.057 inches H20 134 minutes

AMBIENT Total Sample Volume - Vm Average Gas Meter Temperature Total Sample Volume (Standard Conditions) - Vmstd Total Particulates - mn Particulate Concentration (dry-standard) - Cr/Cs Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

0.000 cubic feet 70 degrees Fahrenheit 0.000 dscf 0 mg

SAMPLE TRAIN 1 15.492 cubic feet 79 degrees Fahrenheit 15.520 dscf 0.8 mg

SAMPLE TRAIN 2 17.869 cubic feet 77 degrees Fahrenheit 17.845 dscf 1.1 mg

FIRST HOUR FILTER (TRAIN 1) 6.898 cubic feet 77 degrees Fahrenheit 6.938 dscf 0.5 mg

0.000000 grams/dscf

0.00005 grams/dscf

0.00006 grams/dscf

0.00007 grams/dscf

0.00 grams 0.00 grams/hour

1.11 grams 0.50 grams/hour 0.47 g/kg

1.33 grams 0.60 grams/hour 0.56 g/kg

0.70 grams 0.70 grams/hour 0.35 g/kg

Difference from Average Total Particulate Emissions

0.11 grams

0.11 grams

Dual Train Comparison Results Are Acceptable Complete Test Run Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor First Hour Emissions Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

Control No. P-XXXX-XXXX

FINAL AVERAGE RESULTS 1.22 grams 0.55 grams/hour 0.51 grams/kg

0.70 grams 0.70 grams/hour 0.35 grams/kg

Run 3 - Cat II.xls

45


OMNI-Test Laboratories, Inc. Manufacturer: Rais Model: Q-Tee II Date: 10/21/15 Run: 3 Control #: 0138WS016E Test Duration: 134 Output Category: II

Technicians:

A. Kravitz

Test Results in Accordance with CSA B415.1-09 HHV Basis 69.7% 94.9% 73%

LHV Basis 75.3% 94.9% 79.4%

Output Rate (kJ/h) Burn Rate (kg/h) Input (kJ/h)

14,657 1.06 21,027

13,903 2.34 19,946

(Btu/h) (lb/h) (Btu/h)

Test Load Weight (dry kg) MC wet (%) MC dry (%) Particulate (g ) CO (g) Test Duration (h)

2.37 17.07 20.58 0 183 2.23

5.22

dry lb

Particulate 0.00 0.00 0.00 0.00

CO 5.60 77.33 82.08 13.01

Overall Efficiency Combustion Efficiency Heat Transfer Efficiency

Emissions g/MJ Output g/kg Dry Fuel g/h lb/MM Btu Output Air/Fuel Ratio (A/F) VERSION:

2.3

14.47 3/23/2010

46


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

3 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 21-Oct-15 09:38

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.21

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

134 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.2

30.19

1

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34

0.000 0.101 0.214 0.329 0.445 0.561 0.675 0.792 0.907 1.023 1.139 1.254 1.369 1.484 1.601 1.715 1.831 1.946 2.060 2.176 2.291 2.406 2.521 2.636 2.751 2.865 2.979 3.093 3.206 3.320 3.435 3.551 3.666 3.781 3.896

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.20 "Hg

0.000 0.121 0.255 0.389 0.522 0.656 0.788 0.923 1.057 1.190 1.324 1.456 1.590 1.723 1.856 1.988 2.121 2.254 2.388 2.520 2.653 2.786 2.919 3.052 3.184 3.317 3.451 3.583 3.716 3.849 3.982 4.115 4.248 4.381 4.514

0.10 0.11 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.11 0.11 0.11 0.11 0.12 0.12 0.12 0.12 0.12

0.12 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.16 1.24 1.23 1.22 1.23 1.22 1.23 1.23 1.22 1.22 1.21 1.22 1.22 1.22 1.20 1.21 1.22 1.22 1.22 1.21 1.21 1.21 1.21 1.22 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.22 1.21

72 72 72 72 72 72 72 73 73 73 73 73 74 74 74 75 75 75 75 75 76 76 76 76 77 77 77 77 77 78 78 78 78 78 78

14.30 154.9 161.3

ft/sec. scfm scfm 0 cfm @ -3 0 cfm @ -4 20.59 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.051

0.055

0.034

0.030

0.048

0.054

0.039

0.055

90

90

90

90

90

90

90

90

90

Vstrav

14.07

ft/sec

Vscent

15.80

ft/sec

Fp

0.891

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.440 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

0.53 0.51 0.51 0.51 0.51 0.52 0.52 0.53 0.52 0.52 0.53 0.52 0.53 0.53 0.53 0.53 0.53 0.54 0.53 0.52 0.54 0.53 0.52 0.53 0.53 0.53 0.53 0.53 0.53 0.54 0.52 0.53 0.53 0.54 0.53

1.21 1.33 1.34 1.34 1.34 1.32 1.34 1.33 1.32 1.33 1.33 1.32 1.32 1.32 1.31 1.32 1.31 1.32 1.31 1.32 1.31 1.31 1.31 1.32 1.30 1.31 1.31 1.32 1.32 1.31 1.31 1.31 1.31 1.31 1.31

70 70 70 70 70 71 71 71 71 71 71 72 72 72 72 72 73 73 73 73 73 74 74 74 74 74 74 75 75 75 75 75 75 75 75

0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0.7 0.7 0.7 0.7 0.6 0.6

90 109 120 116 112 106 99 96 95 94 93 92 92 92 91 91 91 91 90 90 91 90 90 90 90 89 89 89 89 89 89 89 90 90 90

Dilution Tunnel Center dP 0.055 0.055 0.060 0.055 0.056 0.054 0.054 0.054 0.055 0.057 0.059 0.056 0.056 0.057 0.059 0.055 0.055 0.057 0.057 0.059 0.056 0.055 0.058 0.057 0.058 0.057 0.056 0.058 0.057 0.057 0.059 0.057 0.056 0.058 0.055

Page 1 of 4

Pro. Rate 1

Pro. Rate 2

92 100 106 105 107 104 107 104 103 101 102 102 101 101 102 104 101 100 100 102 103 100 101 100 100 101 99 99 99 99 101 101 100 102

96 103 107 105 107 104 106 105 102 101 102 103 102 100 103 103 101 102 99 102 103 100 101 99 101 103 99 101 101 99 101 102 100 103

Scale Weight Reading Change 6.3 6.2 5.9 5.7 5.5 5.3 5.2 5.1 5.0 4.9 4.8 4.7 4.5 4.4 4.3 4.2 4.1 4.0 3.9 3.8 3.7 3.6 3.5 3.4 3.3 3.2 3.1 3.0 2.9 2.8 2.7 2.6 2.5 2.4 2.3

-0.1 -0.3 -0.2 -0.2 -0.2 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.2 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1

Temperature Data (°F) Avg. Stove Surface Temp 413.1 405.4 407.1 422.2 428.5 433.0 435.9 435.9 433.8 430.3 432.0 429.6 431.4 430.7 432.2 440.1 438.4 437.5 438.5 436.6 433.6 435.9 438.3 438.6 440.9 440.8 441.6 442.0 441.9 442.6 442.9 443.3 444.5 445.1 447.8

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

360 476 613 608 580 528 454 422 409 403 401 399 400 403 397 400 397 396 397 396 395 393 387 382 382 382 382 382 388 387 389 393 393 395 397

68 68 69 70 70 70 69 69 69 69 69 69 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 71 71

68 70 72 72 73 73 73 72 72 72 72 72 72 72 72 72 72 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73

71 70 71 71 71 71 71 70 70 71 70 71 71 70 70 70 70 71 71 71 71 71 70 70 71 71 71 70 70 71 71 71 71 71 71

-0.080 -0.106 -0.111 -0.107 -0.106 -0.100 -0.096 -0.094 -0.095 -0.095 -0.093 -0.094 -0.094 -0.093 -0.093 -0.094 -0.093 -0.093 -0.092 -0.093 -0.092 -0.091 -0.091 -0.091 -0.091 -0.091 -0.091 -0.091 -0.090 -0.090 -0.091 -0.092 -0.091 -0.092 -0.092

5.4 3.1 4.6 10.6 11.8 11.6 10.9 10.1 9.4 9 8.9 9.1 9.3 9.4 9.4 9.4 9.4 9.5 9.6 9.8 9.9 9.9 9.9 9.8 9.6 9.5 9.4 9.5 9.6 9.7 9.8 9.9 10.1 10.2 10.2

0.2 0.2 0.5 0.6 0.6 0.5 0.3 0.4 0.5 0.5 0.5 0.5 0.5 0.5 0.6 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.5 0.5 0.4 0.3 0.3 0.3 0.3 0.3 0.4 0.4 0.5 0.5

Run 3 - Cat II.xls

47


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

3 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 21-Oct-15 09:38

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.21

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

134 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.2

30.19

1

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69

4.013 4.129 4.244 4.360 4.475 4.591 4.707 4.822 4.938 5.053 5.168 5.284 5.400 5.515 5.631 5.746 5.860 5.976 6.090 6.204 6.318 6.432 6.549 6.666 6.782 6.898 7.017 7.133 7.249 7.365 7.482 7.598 7.714 7.831 7.947

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.20 "Hg

4.647 4.780 4.913 5.046 5.179 5.312 5.445 5.579 5.711 5.844 5.978 6.111 6.244 6.378 6.511 6.645 6.777 6.911 7.045 7.177 7.311 7.444 7.578 7.711 7.845 7.978 8.112 8.245 8.378 8.512 8.645 8.779 8.912 9.046 9.179

0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.11 0.12 0.11 0.11 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.19 1.20 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.22 1.21 1.22 1.21 1.21 1.21 1.22 1.22 1.22 1.22 1.22 1.20 1.22 1.22 1.22 1.22

78 79 79 79 79 79 79 79 79 80 80 80 80 80 80 80 80 80 80 80 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

14.30 154.9 161.3

ft/sec. scfm scfm 0 cfm @ -3 0 cfm @ -4 20.59 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.051

0.055

0.034

0.030

0.048

0.054

0.039

0.055

90

90

90

90

90

90

90

90

90

Vstrav

14.07

ft/sec

Vscent

15.80

ft/sec

Fp

0.891

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.440 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.53 0.53 0.52 0.52 0.53 0.53 0.53 0.53 0.52 0.53 0.52 0.53 0.53 0.52 0.54 0.53 0.53 0.53 0.53 0.52 0.53 0.53 0.53 0.53 0.52 0.53 0.53 0.53 0.54 0.53 0.53 0.54 0.53 0.53 0.53

1.31 1.31 1.30 1.32 1.31 1.30 1.32 1.31 1.31 1.32 1.31 1.31 1.32 1.30 1.31 1.31 1.31 1.32 1.31 1.32 1.31 1.31 1.31 1.32 1.30 1.32 1.32 1.30 1.31 1.31 1.31 1.31 1.31 1.32 1.31

76 76 76 76 76 76 76 76 77 77 77 77 77 77 77 77 77 77 77 77 77 77 78 78 78 78 78 78 78 78 78 78 78 78 78

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

90 90 90 91 91 92 91 90 90 89 89 89 89 88 88 87 87 86 86 86 86 85 85 84 84 84 84 83 83 83 83 83 83 82 82

0.056 0.057 0.060 0.059 0.059 0.058 0.059 0.057 0.059 0.057 0.057 0.059 0.059 0.056 0.055 0.056 0.056 0.059 0.055 0.058 0.058 0.057 0.059 0.056 0.055 0.057 0.057 0.058 0.056 0.057 0.058 0.060 0.058 0.058 0.060

103 101 98 99 99 100 99 100 99 100 100 99 99 101 103 101 100 99 101 98 98 99 99 102 102 100 103 99 101 100 100 98 99 100 97

102 101 98 99 99 100 99 101 98 100 101 99 99 102 102 102 100 99 103 98 100 100 99 101 102 100 100 99 100 100 99 98 99 99 97

Page 2 of 4

Scale Weight Reading Change 2.2 2.1 2.0 1.9 1.8 1.7 1.6 1.5 1.5 1.4 1.4 1.3 1.3 1.3 1.2 1.2 1.2 1.1 1.1 1.1 1.1 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 0.9 0.9 0.9 0.9 0.9 0.9

-0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 0 -0.1 0 -0.1 0 0 -0.1 0 0 -0.1 0 0 0 -0.1 0 0 0 0 0 0 0 -0.1 0 0 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

449.3 451.3 452.5 454.3 457.1 459.3 459.3 459.8 460.9 460.2 459.2 457.9 454.2 451.1 447.0 443.8 439.5 436.1 433.1 428.8 426.4 423.1 420.0 417.1 413.5 410.5 407.4 404.2 401.0 397.7 395.6 392.0 389.2 386.8 384.0

401 404 413 415 418 416 417 415 405 394 383 372 364 353 344 335 325 317 316 309 307 299 294 290 286 281 278 276 276 272 268 265 260 261 259

71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 72 72 72 72 72 72 72 72 72

73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 72 72 72 72 72 72 72 72 72 72 72 72

71 71 71 70 71 70 71 71 71 71 72 70 71 70 71 71 71 70 71 70 70 71 71 71 71 70 70 70 71 71 71 70 70 70 70

-0.092 -0.092 -0.092 -0.093 -0.094 -0.093 -0.093 -0.092 -0.091 -0.090 -0.089 -0.087 -0.087 -0.086 -0.084 -0.083 -0.082 -0.082 -0.081 -0.080 -0.079 -0.079 -0.078 -0.077 -0.077 -0.075 -0.076 -0.075 -0.074 -0.074 -0.073 -0.073 -0.072 -0.072 -0.071

10.2 10.1 10.1 10.2 10.3 10.3 10.2 10.1 10 9.8 9.5 9 8.5 7.9 7.3 7 6.7 6.4 6.1 5.9 5.8 5.7 5.6 5.5 5.4 5.3 5.2 5.2 5.2 5.2 5.2 5.2 5.2 5.2 5.2

0.6 0.5 0.5 0.5 0.6 0.7 0.7 0.8 0.7 0.6 0.5 0.3 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.2 0.2 0.2 0.2 0.3 0.3 0.3 0.4 0.4 0.4 0.4 0.4 0.5 0.5 0.5 0.5

Run 3 - Cat II.xls

48


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

3 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 21-Oct-15 09:38

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.21

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

134 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.2

30.19

1

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.20 "Hg

70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104

8.063 8.179 8.296 8.412 8.528 8.645 8.761 8.875 8.991 9.107 9.221 9.336 9.451 9.566 9.683 9.800 9.917 10.034 10.150 10.267 10.383 10.499 10.616 10.733 10.849 10.966 11.082 11.198 11.314 11.431 11.548 11.664 11.780 11.895 12.011

9.313 9.447 9.580 9.714 9.847 9.981 10.114 10.248 10.382 10.515 10.649 10.783 10.916 11.050 11.184 11.317 11.451 11.585 11.718 11.852 11.986 12.120 12.253 12.387 12.521 12.654 12.788 12.922 13.055 13.189 13.323 13.457 13.590 13.724 13.858

Control No. P-SSAR-0001

0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.23 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.22 1.21 1.22 1.22 1.22

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

14.30 154.9 161.3

ft/sec. scfm scfm 0 cfm @ -3 0 cfm @ -4 20.59 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.051

0.055

0.034

0.030

0.048

0.054

0.039

0.055

90

90

90

90

90

90

90

90

90

Vstrav

14.07

ft/sec

Vscent

15.80

ft/sec

Fp

0.891

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.440 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.53 0.53 0.53 0.53 0.54 0.54 0.54 0.53 0.53 0.53 0.54 0.53 0.54 0.54 0.53 0.54 0.53 0.53 0.53 0.53 0.53 0.53 0.54 0.53 0.54 0.53 0.53 0.54 0.53 0.54 0.53 0.53 0.53 0.53 0.53

1.31 1.31 1.32 1.31 1.31 1.32 1.31 1.32 1.32 1.31 1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.31 1.31 1.32 1.31 1.31 1.32 1.32 1.31 1.32 1.30 1.32 1.32 1.31 1.31 1.31 1.31 1.32 1.31

78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

82 82 82 82 81 81 81 81 81 80 81 80 80 80 80 80 80 80 80 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79

0.057 0.058 0.058 0.058 0.056 0.058 0.057 0.056 0.057 0.058 0.059 0.057 0.056 0.058 0.056 0.059 0.057 0.056 0.057 0.057 0.058 0.059 0.056 0.057 0.058 0.057 0.057 0.057 0.060 0.060 0.056 0.059 0.059 0.057 0.058

100 99 100 99 101 100 100 99 100 99 97 99 100 98 102 99 101 102 100 101 99 98 101 101 99 101 100 100 97 98 101 98 98 99 99

100 99 99 99 100 99 99 101 100 98 98 100 100 99 101 98 100 101 99 100 99 98 100 100 99 99 100 100 97 97 101 98 97 100 99

Page 3 of 4

Scale Weight Reading Change 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.4

-0.1 0 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 0 -0.1

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

381.4 379.5 376.9 375.0 372.5 370.9 368.3 366.3 364.5 362.3 359.8 357.8 356.9 354.2 352.8 351.7 349.2 347.7 345.8 344.4 343.1 341.9 340.2 339.1 337.8 336.5 335.4 333.9 332.5 331.1 330.4 328.5 327.7 326.6 325.7

256 255 255 250 250 246 246 243 241 240 240 237 236 233 232 230 229 229 226 226 226 226 224 222 222 221 220 220 220 217 216 215 214 214 213

72 71 71 71 71 71 71 71 71 71 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

72 72 72 72 72 72 72 72 72 72 72 72 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71

70 71 70 71 70 71 70 70 70 71 70 70 70 70 70 70 70 70 70 70 70 70 71 71 70 70 71 70 70 71 71 70 70 70 71

-0.071 -0.071 -0.070 -0.070 -0.070 -0.069 -0.069 -0.069 -0.068 -0.068 -0.068 -0.068 -0.067 -0.067 -0.067 -0.067 -0.066 -0.066 -0.066 -0.066 -0.065 -0.065 -0.064 -0.065 -0.064 -0.064 -0.064 -0.064 -0.064 -0.064 -0.063 -0.063 -0.063 -0.063 -0.062

5.2 5.2 5.2 5.2 5.2 5.1 5.1 5 4.9 4.9 4.8 4.7 4.7 4.6 4.6 4.6 4.6 4.6 4.5 4.5 4.4 4.5 4.5 4.5 4.4 4.5 4.5 4.4 4.4 4.4 4.2 4.1 4.1 4.1 4.1

0.5 0.5 0.6 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8

Run 3 - Cat II.xls

49


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

3 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 21-Oct-15 09:38

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.21

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

134 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.2

30.19

1

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.20 "Hg

105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126 127 128 129 130 131 132 133 134 Avg/Tot

12.126 12.241 12.356 12.471 12.588 12.704 12.820 12.937 13.054 13.171 13.288 13.404 13.521 13.637 13.753 13.870 13.988 14.104 14.220 14.337 14.453 14.569 14.685 14.802 14.917 15.032 15.148 15.263 15.378 15.492 15.492

13.991 14.125 14.259 14.392 14.526 14.660 14.793 14.927 15.061 15.194 15.328 15.462 15.596 15.729 15.864 15.997 16.131 16.265 16.399 16.532 16.666 16.800 16.934 17.067 17.201 17.335 17.468 17.602 17.736 17.869 17.869

Control No. P-SSAR-0001

0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.23 1.22 1.22 1.21 1.22 1.23 1.22 1.22 1.22 1.21 1.22 1.22 1.23 1.22 1.22 1.22 1.22 1.22 1.22 1.23 1.22 1.22 1.23 1.22 1.22 1.21 1.23 1.22 1.21 1.22 1.22

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 79

14.30 154.9 161.3

ft/sec. scfm scfm 0 cfm @ -3 0 cfm @ -4 20.59 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.051

0.055

0.034

0.030

0.048

0.054

0.039

0.055

90

90

90

90

90

90

90

90

90

Vstrav

14.07

ft/sec

Vscent

15.80

ft/sec

Fp

0.891

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.440 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.53 0.54 0.53 0.53 0.53 0.53 0.53 0.54 0.53 0.54 0.54 0.53 0.54 0.53 0.53 0.54 0.53 0.53 0.53 0.53 0.52 0.53 0.53 0.54 0.53 0.53 0.54 0.53 0.53 0.53

1.31 1.32 1.31 1.32 1.32 1.32 1.32 1.32 1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.32 1.32 1.31 1.32 1.32 1.31 1.31 1.31 1.31 1.32 1.31 1.31 1.32 1.32 1.32 1.31

79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 77

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

79 79 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 77 77 78 78 78 78 78 78 78 78 85

0.058 0.057 0.056 0.057 0.058 0.057 0.061 0.058 0.058 0.057 0.058 0.059 0.057 0.056 0.057 0.058 0.057 0.060 0.058 0.058 0.058 0.059 0.057 0.058 0.057 0.058 0.057 0.056 0.057 0.058 0.057

98 99 100 99 100 100 96 100 100 100 100 98 100 101 100 100 101 97 99 100 99 98 100 100 99 98 100 100 99 97 100

98 100 101 99 99 100 96 99 99 99 99 98 100 100 100 98 100 97 99 98 99 98 100 98 100 99 99 101 100 98 100

Page 4 of 4

Scale Weight Reading Change 0.5 0.5 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.1 0.1 0.0

0.1 0 -0.1 0 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 -0.1 0.1 -0.1 0 0 0 0 0 0 0 -0.1 0 -0.1

Temperature Data (°F) Avg. Stove Surface Temp 324.7 323.2 322.5 320.9 319.9 318.7 317.7 317.0 316.3 315.1 314.2 313.2 312.9 312.0 311.1 310.5 309.9 309.1 308.2 307.7 307.5 306.9 306.3 306.3 305.3 304.7 303.9 302.8 302.5 301.6 111.5

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

212 214 213 211 209 209 208 207 206 207 206 206 205 204 203 203 203 202 202 202 200 199 198 198 198 198 198 197 196 197

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 72

70 70 71 70 70 70 70 71 70 70 70 71 70 70 70 70 70 71 70 70 70 70 71 71 71 70 70 70 70 70 70

-0.062 -0.062 -0.062 -0.062 -0.063 -0.062 -0.061 -0.061 -0.061 -0.061 -0.061 -0.061 -0.060 -0.061 -0.061 -0.061 -0.061 -0.061 -0.061 -0.061 -0.060 -0.060 -0.060 -0.060 -0.060 -0.059 -0.060 -0.060 -0.059 -0.059 -0.076

4.2 4.2 4.3 4.3 4.3 4.3 4.3 4.4 4.4 4.4 4.4 4.4 4.4 4.5 4.5 4.5 4.6 4.6 4.6 4.5 4.4 4.4 4.2 4.2 4 4 3.9 4 3.9 4

0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.9 0.9 0.9 0.9 1 1 1 0.9 0.9 0.9 0.9 0.9 0.9

Run 3 - Cat II.xls

50


51


52


53


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 4

OMNI-Test Laboratories, Inc.

54


OMNI-Test Laboratories, Inc.

Wood Heater Test Results - ASTM E2780 / ASTM E2515 Manufacturer: Model: Project No.: Tracking No.: Run: Test Date:

Burn Rate Average Tunnel Temperature Average Gas Velocity in Dilution Tunnel - vs Average Gas Flow Rate in Dilution Tunnel - Qsd Average Delta p Total Time of Test

RAIS Q-Tee II 0138WS016E 2138 4 10/21/15

2.51 kg/hr dry 119 degrees Fahrenheit 14.21 feet/second 9051.2 dscf/hour 0.056 inches H20 59 minutes

AMBIENT Total Sample Volume - Vm Average Gas Meter Temperature Total Sample Volume (Standard Conditions) - Vmstd

0.000 cubic feet 74 degrees Fahrenheit 0.000 dscf

Total Particulates - mn Particulate Concentration (dry-standard) - Cr/Cs Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

0 mg

SAMPLE TRAIN 1 6.783 cubic feet 82 degrees Fahrenheit 6.759 dscf 0.5 mg

SAMPLE TRAIN 2 7.790 cubic feet 79 degrees Fahrenheit 7.747 dscf 0.6 mg

FIRST HOUR FILTER (TRAIN 1) 0.000 cubic feet 82 degrees Fahrenheit 0.000 dscf 0.5 mg

0.000000 grams/dscf

0.00007 grams/dscf

0.00008 grams/dscf

#DIV/0! grams/dscf

0.00 grams 0.00 grams/hour

0.66 grams 0.67 grams/hour 0.27 g/kg

0.69 grams 0.70 grams/hour 0.28 g/kg

#DIV/0! grams #DIV/0! grams/hour #DIV/0! g/kg

Difference from Average Total Particulate Emissions

0.02 grams

0.02 grams

Dual Train Comparison Results Are Acceptable Complete Test Run Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor First Hour Emissions Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

Control No. P-XXXX-XXXX

FINAL AVERAGE RESULTS 0.67 grams 0.69 grams/hour 0.27 grams/kg

#DIV/0! #DIV/0! #DIV/0!

grams grams/hour grams/kg

Run 4 - Cat IV.xls

55


OMNI-Test Laboratories, Inc. Manufacturer: Rais Model: Q-Tee II Date: 10/21/15 Run: 4 Control #: 0138WS016E Test Duration: 59 Output Category: IV

Technicians:

A. Kravitz

Test Results in Accordance with CSA B415.1-09 HHV Basis 65.4% 98.5% 66%

LHV Basis 70.7% 98.5% 71.8%

Output Rate (kJ/h) Burn Rate (kg/h) Input (kJ/h)

32,439 2.50 49,595

30,772 5.52 47,047

(Btu/h) (lb/h) (Btu/h)

Test Load Weight (dry kg) MC wet (%) MC dry (%) Particulate (g ) CO (g) Test Duration (h)

2.46 17.79 21.64 0 67 0.98

5.43

dry lb

Particulate 0.00 0.00 0.00 0.00

CO 2.11 27.37 68.51 4.91

Overall Efficiency Combustion Efficiency Heat Transfer Efficiency

Emissions g/MJ Output g/kg Dry Fuel g/h lb/MM Btu Output Air/Fuel Ratio (A/F) VERSION:

2.3

12.76 3/23/2010

56


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

4 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 21-Oct-15 13:46

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.19

OMNI Equipment Numbers:

(1)

Total Sampling Time: Recording Interval:

59 1

min min

Background Sample Volume:

0

cubic feet

1.003

(2)

Middle

End

Average

30.18

30.18

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

(Amb)

Gas Meter 1 (ft3)

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34

0.000 0.103 0.220 0.336 0.453 0.569 0.685 0.802 0.918 1.034 1.150 1.265 1.380 1.496 1.611 1.727 1.842 1.956 2.073 2.188 2.302 2.416 2.530 2.646 2.759 2.873 2.987 3.100 3.216 3.332 3.447 3.562 3.677 3.792 3.908

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.18 "Hg

0.000 0.127 0.261 0.395 0.529 0.663 0.796 0.930 1.062 1.196 1.329 1.461 1.594 1.727 1.859 1.992 2.124 2.256 2.389 2.521 2.653 2.785 2.917 3.048 3.181 3.312 3.444 3.576 3.708 3.839 3.970 4.102 4.234 4.365 4.497

0.10 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.11 0.11 0.11 0.12 0.11 0.11 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.12

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 0.03 1.25 1.24 1.24 1.23 1.23 1.23 1.23 1.22 1.22 1.21 1.22 1.22 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.21 1.20 1.21 1.19 1.20 1.20 1.20 1.20 1.20 1.20 1.20 1.19 1.20 1.20 1.19

77 77 77 77 77 77 77 77 77 78 78 78 78 78 79 79 79 79 80 80 80 80 81 81 81 81 81 82 82 82 82 83 83 83 83

14.21 149.5 150.9

ft/sec. scfm scfm 0 cfm @ -3 0.001 cfm @ -4 21.63 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.027

0.038

0.057

0.042

0.038

0.048

0.050

0.030

0.056

107

107

107

107

107

107

107

107

107

Vstrav

14.06

ft/sec

Vscent

16.19

ft/sec

Fp

0.869

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.440 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

1.51 0.51 0.51 0.5 0.52 0.51 0.51 0.51 0.51 0.52 0.52 0.52 0.52 0.51 0.52 0.52 0.51 0.51 0.52 0.51 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.52 0.51 0.52 0.51 0.52 0.52 0.52

0.52 1.33 1.33 1.34 1.33 1.32 1.33 1.31 1.31 1.32 1.31 1.31 1.31 1.30 1.31 1.30 1.30 1.30 1.29 1.30 1.29 1.29 1.30 1.28 1.29 1.28 1.29 1.28 1.28 1.29 1.27 1.28 1.26 1.28 1.27

75 75 75 75 75 75 75 75 75 75 75 75 76 76 76 76 76 77 77 77 77 77 78 78 78 78 78 79 79 79 79 79 79 80 80

0.8 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

107 115 126 125 120 119 119 120 120 120 122 122 123 124 124 125 126 126 126 127 126 126 127 126 127 126 128 128 129 129 128 128 127 126 125

Dilution Tunnel Center dP 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056

Page 1 of 2

Pro. Rate 1

Pro. Rate 2

90 103 102 103 102 102 103 102 102 102 101 101 102 101 102 101 100 103 101 100 100 100 102 99 100 100 99 102 102 101 101 101 100 101

97 103 103 102 102 101 102 101 102 102 101 102 102 101 102 101 101 102 101 101 101 101 100 102 100 101 101 101 100 100 101 101 100 100

Scale Weight Reading Change 6.6 6.4 6.2 6.0 5.8 5.6 5.4 5.2 5.0 4.7 4.6 4.4 4.1 4.0 3.8 3.6 3.4 3.2 3.1 2.9 2.7 2.5 2.4 2.2 2.0 1.9 1.7 1.6 1.4 1.3 1.2 1.1 1.0 0.9 0.8

-0.2 -0.2 -0.2 -0.2 -0.2 -0.2 -0.2 -0.2 -0.3 -0.1 -0.2 -0.3 -0.1 -0.2 -0.2 -0.2 -0.2 -0.1 -0.2 -0.2 -0.2 -0.1 -0.2 -0.2 -0.1 -0.2 -0.1 -0.2 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1

Temperature Data (°F) Avg. Stove Surface Temp 392.8 390.8 392.6 399.9 407.0 413.4 421.3 428.6 434.9 438.7 444.8 449.4 451.7 455.5 459.4 462.4 466.7 470.3 474.1 477.7 481.1 484.5 486.5 489.6 493.4 499.7 503.2 506.3 511.8 515.6 519.0 520.4 521.1 521.6 519.2

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

384 435 603 609 571 576 578 586 592 598 605 609 613 617 617 618 619 621 624 622 625 620 623 628 628 628 633 633 636 628 617 606 594 582 571

71 71 72 73 73 73 73 74 74 74 74 75 75 75 75 75 76 76 76 76 76 76 76 76 76 77 77 77 77 77 78 78 78 78 78

71 74 76 77 77 78 78 78 79 79 79 79 80 80 80 80 81 81 81 81 81 81 82 82 82 82 82 83 83 83 83 83 83 83 83

74 73 73 73 73 73 73 74 73 73 73 73 73 73 73 74 74 74 74 74 74 74 74 74 73 74 74 75 74 74 75 74 74 74 76

-0.090 -0.100 -0.111 -0.105 -0.105 -0.106 -0.107 -0.107 -0.108 -0.109 -0.109 -0.111 -0.110 -0.110 -0.110 -0.110 -0.110 -0.110 -0.110 -0.110 -0.111 -0.110 -0.110 -0.110 -0.110 -0.110 -0.111 -0.111 -0.111 -0.111 -0.109 -0.109 -0.108 -0.106 -0.106

4.7 3.5 4.2 10.6 12.2 11.9 11 10.6 10.6 10.6 10.6 10.7 10.7 10.8 10.8 10.7 10.6 10.6 10.7 10.7 10.7 10.7 10.6 10.5 10.4 10.3 10.3 10.4 10.5 10.6 10.6 10.4 9.9 9.2 8.4

0.4 0.4 0.4 0.5 0.5 0.5 0.5 0.4 0.2 0.2 0.2 0.2 0.1 0.1 0.1 0 0 0 0 0 0 0 0 0.1 0.1 0.1 0.1 0 0 0.1 0.1 0.1 0.1 0 0

Run 4 - Cat IV.xls

57


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

4 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 21-Oct-15 13:46

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.19

OMNI Equipment Numbers:

(1)

Total Sampling Time: Recording Interval:

59 1

min min

Background Sample Volume:

0

cubic feet

1.003

(2)

Middle

End

Average

30.18

30.18

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

(Amb)

Gas Meter 1 (ft3)

35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 Avg/Tot

4.023 4.138 4.253 4.368 4.484 4.599 4.714 4.829 4.944 5.060 5.175 5.291 5.406 5.520 5.635 5.750 5.864 5.978 6.091 6.206 6.322 6.437 6.553 6.668 6.783 6.783

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.18 "Hg

4.628 4.760 4.891 5.022 5.154 5.285 5.417 5.549 5.681 5.812 5.944 6.075 6.207 6.339 6.471 6.603 6.735 6.866 6.998 7.130 7.262 7.394 7.527 7.658 7.790 7.790

0.12 0.12 0.12 0.12 0.12 0.12 0.12 0.11 0.12 0.12 0.12 0.12 0.11 0.11 0.12 0.12 0.11 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.12 0.11

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.18 1.19 1.19 1.19 1.19 1.19 1.19 1.19 1.20 1.19 1.19 1.19 1.19 1.19 1.19 1.19 1.20 1.19 1.19 1.19 1.20 1.19 1.19 1.19 1.19 1.18

83 84 84 84 84 84 84 84 85 85 85 85 85 85 85 85 85 85 85 85 86 86 86 86 86 82

14.21 149.5 150.9

ft/sec. scfm scfm 0 cfm @ -3 0.001 cfm @ -4 21.63 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.027

0.038

0.057

0.042

0.038

0.048

0.050

0.030

0.056

107

107

107

107

107

107

107

107

107

Vstrav

14.06

ft/sec

Vscent

16.19

ft/sec

Fp

0.869

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.440 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.52 0.51 0.51 0.51 0.52 0.51 0.51 0.51 0.51 0.52 0.51 0.51 0.52 0.51 0.52 0.52 0.52 0.51 0.51 0.52 0.51 0.52 0.52 0.51 0.51

1.28 1.27 1.27 1.27 1.27 1.27 1.27 1.28 1.27 1.28 1.28 1.27 1.28 1.27 1.28 1.27 1.28 1.28 1.27 1.28 1.28 1.28 1.28 1.28 1.28 1.28

80 80 80 80 80 81 81 81 81 81 81 81 81 81 82 82 82 82 82 82 82 82 82 82 82 79

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

122 121 120 119 118 116 115 114 113 113 111 110 109 108 108 108 107 107 107 106 106 105 105 105 104 119

0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056 0.056

100 100 100 100 100 99 99 99 99 100 99 100 99 98 99 99 98 98 97 98 99 98 99 98 98 100

99 100 99 99 100 99 99 99 99 98 99 98 99 99 98 98 98 98 98 98 98 98 99 97 98 100

Page 2 of 2

Scale Weight Reading Change 0.8 0.8 0.7 0.7 0.6 0.6 0.5 0.5 0.5 0.5 0.5 0.4 0.4 0.4 0.4 0.3 0.3 0.3 0.3 0.3 0.2 0.2 0.2 0.2 0.0

0 0 -0.1 0 -0.1 0 -0.1 0 0 0 0 -0.1 0 0 0 -0.1 0 0 0 0 -0.1 0 0 0 -0.2

Temperature Data (°F) Avg. Stove Surface Temp 513.4 508.3 504.5 501.4 496.9 493.6 489.6 484.5 479.9 475.5 471.3 466.8 463.1 459.7 455.6 452.1 449.7 445.7 443.2 440.3 436.3 433.2 430.2 425.0 422.6 29.8

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

559 549 537 532 519 511 500 494 489 482 474 468 463 455 446 446 442 440 433 429 428 423 417 415 412

78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 76

83 83 83 83 83 83 83 83 83 83 83 83 82 82 82 82 82 82 82 82 82 82 81 81 81 81

75 74 74 76 74 74 76 74 74 74 74 74 74 75 75 74 75 75 74 75 74 74 75 75 75 74

-0.104 -0.103 -0.101 -0.101 -0.099 -0.098 -0.098 -0.097 -0.096 -0.095 -0.094 -0.093 -0.093 -0.092 -0.092 -0.091 -0.091 -0.091 -0.090 -0.090 -0.089 -0.089 -0.088 -0.087 -0.087 -0.102

7.7 7.2 6.7 6.3 6 5.8 5.6 5.4 5.2 5.2 5.1 5.1 5.1 5 5 5 5 4.9 4.9 4.6 4.4 4.4 4.4 4.4 4.4

0 0 0 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3

Run 4 - Cat IV.xls

58


59


60


61


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 5

OMNI-Test Laboratories, Inc.

62


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

5 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 09:36

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.24 OMNI Equipment Numbers:

256 1

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34

0.000 0.114 0.247 0.382 0.515 0.649 0.782 0.916 1.049 1.181 1.314 1.447 1.581 1.713 1.845 1.977 2.109 2.240 2.371 2.502 2.635 2.768 2.900 3.034 3.166 3.300 3.432 3.566 3.699 3.832 3.965 4.097 4.230 4.362 4.495

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3) 0.000 0.119 0.254 0.389 0.523 0.657 0.792 0.926 1.061 1.195 1.329 1.463 1.597 1.731 1.865 1.998 2.132 2.266 2.400 2.533 2.667 2.801 2.934 3.068 3.201 3.335 3.469 3.602 3.736 3.869 4.003 4.137 4.270 4.404 4.538

0.11 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.12 0.14 0.14 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.01 1.64 1.64 1.62 1.63 1.62 1.62 1.61 1.62 1.62 1.61 1.61 1.60 1.60 1.60 1.60 1.60 1.60 1.60 1.60 1.60 1.60 1.60 1.59 1.60 1.59 1.59 1.60 1.60 1.58 1.59 1.60 1.60 1.60 1.59

73 73 73 73 73 73 74 74 74 74 74 74 75 75 75 75 76 76 76 76 77 77 77 77 77 78 78 78 78 78 78 79 79 79 79

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

12.93 145.6 148.7 N/A N/A 21.53

in. Hg in. Hg

Velocity Traverse Data

30.24 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

0.3 0.36 0.35 0.35 0.35 0.37 0.36 0.37 0.36 0.38 0.37 0.37 0.37 0.37 0.38 0.37 0.38 0.37 0.37 0.38 0.38 0.37 0.37 0.37 0.38 0.37 0.37 0.37 0.36 0.37 0.37 0.37 0.37 0.38 0.37

0.03 1.35 1.35 1.35 1.36 1.35 1.34 1.35 1.34 1.34 1.34 1.34 1.34 1.34 1.33 1.33 1.33 1.33 1.32 1.33 1.32 1.32 1.33 1.32 1.33 1.33 1.32 1.33 1.33 1.32 1.33 1.32 1.32 1.33 1.32

72 72 72 72 72 72 72 72 73 73 73 73 73 73 74 74 74 74 74 75 75 75 75 75 76 76 76 76 76 76 77 77 77 77 77

0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0.7 0.7

81 94 105 111 103 98 91 88 87 85 84 84 83 83 83 82 81 81 81 80 80 80 79 79 79 78 79 78 78 78 78 78 78 77 78

Dilution Tunnel Center dP 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

Page 1 of 8

Pro. Rate 1

Pro. Rate 2

89 105 107 104 105 103 104 103 102 102 102 103 101 101 101 101 100 100 100 101 101 101 102 101 102 100 102 101 101 101 100 101 100 101

92 105 106 104 104 104 103 103 102 102 102 102 102 102 101 102 102 102 101 102 102 101 102 101 101 101 101 101 101 101 101 100 101 101

Scale Weight Reading Change 6.8 6.8 6.5 6.4 6.2 6.0 6.0 5.9 5.9 5.9 5.8 5.8 5.8 5.7 5.7 5.6 5.6 5.6 5.5 5.5 5.5 5.4 5.4 5.4 5.4 5.3 5.3 5.3 5.3 5.2 5.2 5.2 5.2 5.2 5.1

0 -0.3 -0.1 -0.2 -0.2 0 -0.1 0 0 -0.1 0 0 -0.1 0 -0.1 0 0 -0.1 0 0 -0.1 0 0 0 -0.1 0 0 0 -0.1 0 0 0 0 -0.1

Temperature Data (°F) Avg. Stove Surface Temp 304.1 302.5 302.1 305.1 311.0 316.8 319.8 321.6 322.3 322.5 321.9 320.0 318.3 317.2 315.3 313.5 311.6 309.3 307.4 305.1 303.9 301.4 299.5 297.2 295.1 292.6 291.0 289.1 286.0 284.5 282.5 280.0 278.2 276.6 274.6

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

266 287 436 509 459 409 342 304 282 265 252 244 237 233 229 220 213 211 206 203 200 197 195 193 190 187 186 182 180 178 177 175 173 170 170

69 70 71 72 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71

69 71 72 73 73 73 73 73 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72 72

71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 70 71 71 70

-0.079 -0.084 -0.101 -0.103 -0.093 -0.087 -0.080 -0.077 -0.075 -0.074 -0.072 -0.071 -0.070 -0.069 -0.069 -0.067 -0.066 -0.066 -0.066 -0.064 -0.064 -0.063 -0.063 -0.062 -0.061 -0.061 -0.060 -0.060 -0.059 -0.059 -0.058 -0.058 -0.058 -0.057 -0.057

2.4 4.9 4.2 9.5 10.6 10.9 10.5 9.5 8.4 6 3.5 2.4 2.1 2 2 2 2 1.9 1.8 1.8 1.7 1.7 1.7 1.7 1.7 1.7 1.7 1.7 1.8 1.8 1.8 1.8 1.9 1.9 1.9

0.6 0.2 0.7 0.7 1 0.9 0.6 0.5 0.6 0.7 0.8 0.8 0.8 0.9 0.9 0.9 0.9 0.8 0.7 0.7 0.7 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.8 0.8 0.8 0.8

Run 5 - Fire out.xls

63


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

5 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 09:36

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.24 OMNI Equipment Numbers:

256 1

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69

4.628 4.761 4.892 5.024 5.156 5.288 5.419 5.550 5.684 5.816 5.951 6.083 6.217 6.349 6.483 6.617 6.750 6.883 7.016 7.149 7.281 7.415 7.548 7.681 7.813 7.945 8.080 8.212 8.344 8.474 8.608 8.742 8.875 9.009 9.141

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3) 4.671 4.805 4.939 5.072 5.206 5.340 5.474 5.607 5.741 5.875 6.009 6.143 6.277 6.410 6.544 6.678 6.812 6.946 7.080 7.214 7.348 7.481 7.616 7.749 7.883 8.017 8.150 8.284 8.419 8.551 8.686 8.820 8.953 9.087 9.221

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.13 0.13

1.59 1.59 1.59 1.59 1.60 1.59 1.59 1.59 1.60 1.59 1.59 1.58 1.58 1.60 1.59 1.60 1.58 1.59 1.59 1.59 1.59 1.59 1.59 1.59 1.59 1.59 1.75 1.59 1.59 1.59 1.59 1.59 1.58 1.59 1.59

79 79 79 80 80 80 80 80 80 80 80 80 80 80 80 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

12.93 145.6 148.7 N/A N/A 21.53

in. Hg in. Hg

Velocity Traverse Data

30.24 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.37 0.37 0.37 0.37 0.36 0.37 0.36 0.37 0.36 0.37 0.37 0.37 0.37 0.36 0.37 0.37 0.36 0.37 0.37 0.37 0.36 0.37 0.37 0.36 0.37 0.37 0.52 0.38 0.36 0.37 0.37 0.37 0.36 0.37 0.36

1.32 1.33 1.32 1.32 1.33 1.32 1.32 1.33 1.32 1.32 1.33 1.32 1.32 1.33 1.31 1.32 1.33 1.32 1.32 1.32 1.31 1.33 1.32 1.32 1.32 1.33 1.32 1.33 1.31 1.32 1.32 1.32 1.32 1.32 1.32

77 77 77 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79

0.7 0.7 0.6 0.7 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

77 77 77 77 77 76 76 76 76 76 76 76 76 76 76 76 76 76 76 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

101 101 99 100 100 100 99 99 101 100 102 100 101 100 101 101 100 100 100 100 99 101 100 100 99 99 102 99 99 98 101 101 100 101 99

100 101 101 100 101 101 101 100 101 101 101 101 101 100 101 101 101 101 101 100 100 100 101 100 100 100 100 100 101 99 101 100 100 100 100

Page 2 of 8

Scale Weight Reading Change 5.1 5.1 5.1 5.1 5.0 5.0 4.9 5.0 4.9 4.9 4.9 4.8 4.8 4.8 4.7 4.8 4.7 4.7 4.7 4.6 4.6 4.6 4.6 4.6 4.6 4.5 4.5 4.5 4.5 4.4 4.4 4.4 4.3 4.4 4.3

0 0 0 0 -0.1 0 -0.1 0.1 -0.1 0 0 -0.1 0 0 -0.1 0.1 -0.1 0 0 -0.1 0 0 0 0 0 -0.1 0 0 0 -0.1 0 0 -0.1 0.1 -0.1

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

272.7 270.4 268.8 266.8 265.4 263.4 262.0 259.8 257.8 256.8 255.4 253.2 252.0 250.4 249.0 248.1 246.7 245.2 244.2 242.8 241.7 240.5 239.2 237.8 236.5 235.9 234.9 233.7 233.0 231.9 230.9 229.3 228.8 228.3 227.5

168 166 166 165 164 163 162 160 159 158 157 156 156 155 153 152 152 151 151 150 150 149 148 147 147 147 146 145 144 144 144 143 142 142 142

71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 70 70 70 70 70 70 70 70 71 71 71 71 71 71 71 71

72 72 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 71 70 71 71 71 71 70 71 70

70 70 71 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 69 69 69 69

-0.057 -0.056 -0.056 -0.055 -0.055 -0.055 -0.055 -0.054 -0.054 -0.054 -0.054 -0.053 -0.053 -0.052 -0.052 -0.052 -0.052 -0.052 -0.052 -0.051 -0.051 -0.051 -0.051 -0.051 -0.050 -0.050 -0.050 -0.050 -0.050 -0.049 -0.049 -0.049 -0.049 -0.049 -0.048

1.9 2 2 2 2 2.1 2.1 2.1 2.1 2.1 2.1 2.2 2.2 2.2 2.2 2.3 2.3 2.3 2.3 2.4 2.4 2.4 2.4 2.4 2.4 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5

0.8 0.8 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.9 1 1 1 1 1 1 1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.2 1.2 1.2 1.1 1.1 1.1 1.1 1.1

Run 5 - Fire out.xls

64


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

5 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 09:36

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.24 OMNI Equipment Numbers:

256 1

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104

9.275 9.408 9.542 9.675 9.809 9.942 10.075 10.208 10.340 10.474 10.608 10.740 10.872 11.005 11.137 11.268 11.399 11.530 11.665 11.797 11.932 12.064 12.198 12.331 12.464 12.598 12.730 12.864 12.996 13.129 13.262 13.395 13.528 13.661 13.794

9.354 9.488 9.621 9.755 9.888 10.022 10.156 10.289 10.423 10.557 10.690 10.824 10.958 11.092 11.225 11.359 11.493 11.625 11.759 11.893 12.026 12.160 12.293 12.427 12.560 12.694 12.827 12.961 13.094 13.227 13.361 13.494 13.627 13.761 13.894

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.58 1.59 1.59 1.59 1.59 1.59 1.59 1.59 1.59 1.58 1.60 1.59 1.60 1.58 1.59 1.59 1.59 1.59 1.59 1.58 1.59 1.59 1.59 1.59 1.59 1.59 1.59 1.57 1.59 1.59 1.59 1.58 1.59 1.57 1.59

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

12.93 145.6 148.7 N/A N/A 21.53

in. Hg in. Hg

Velocity Traverse Data

30.24 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.37 0.36 0.37 0.36 0.36 0.37 0.36 0.37 0.37 0.36 0.36 0.37 0.36 0.36 0.36 0.36 0.36 0.36 0.37 0.37 0.36 0.37 0.37 0.36 0.36 0.36 0.36 0.36 0.36 0.37 0.35 0.36 0.37 0.36 0.36

1.32 1.32 1.32 1.32 1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.31 1.33 1.32 1.31 1.33 1.32 1.32 1.32 1.32 1.32 1.32 1.32 1.32 1.32 1.31 1.32 1.32 1.30 1.31 1.31 1.31 1.31 1.31 1.32

79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

75 75 75 75 75 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

101 100 101 100 101 100 100 100 99 101 101 99 99 100 99 99 99 99 102 99 102 99 101 100 100 101 99 101 99 100 100 100 100 100 100

100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 99 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100

Page 3 of 8

Scale Weight Reading Change 4.3 4.3 4.3 4.2 4.2 4.2 4.2 4.1 4.1 4.1 4.1 4.1 4.0 4.0 4.0 4.0 3.9 4.0 3.9 3.9 3.9 3.9 3.8 3.8 3.8 3.7 3.8 3.7 3.7 3.7 3.7 3.7 3.6 3.6 3.6

0 0 0 -0.1 0 0 0 -0.1 0 0 0 0 -0.1 0 0 0 -0.1 0.1 -0.1 0 0 0 -0.1 0 0 -0.1 0.1 -0.1 0 0 0 0 -0.1 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

226.6 226.0 224.8 224.3 223.0 222.5 221.8 221.0 220.5 220.0 218.8 218.4 217.5 217.3 216.6 215.8 215.5 214.5 214.0 213.4 213.1 212.7 212.5 212.1 211.5 211.2 210.8 210.0 210.1 209.6 209.0 208.3 208.3 207.7 207.3

141 140 139 139 138 139 138 138 138 136 137 137 136 136 135 135 135 135 134 133 133 133 133 132 132 131 131 131 131 131 131 130 130 130 129

71 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

69 69 69 70 70 69 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

-0.048 -0.048 -0.049 -0.048 -0.048 -0.048 -0.048 -0.048 -0.048 -0.047 -0.048 -0.047 -0.047 -0.047 -0.047 -0.047 -0.047 -0.047 -0.046 -0.047 -0.046 -0.046 -0.046 -0.047 -0.046 -0.046 -0.046 -0.046 -0.046 -0.046 -0.046 -0.046 -0.046 -0.046 -0.046

2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.6 2.5 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.5 2.5 2.5 2.4 2.4 2.4 2.4 2.3 2.3 2.3

1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.2 1.2 1.2 1.2 1.2 1.2 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1 1

Run 5 - Fire out.xls

65


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

5 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 09:36

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.24 OMNI Equipment Numbers:

256 1

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126 127 128 129 130 131 132 133 134 135 136 137 138 139

13.924 14.058 14.188 14.320 14.450 14.584 14.717 14.850 14.984 15.117 15.250 15.382 15.516 15.648 15.782 15.915 16.048 16.180 16.314 16.446 16.579 16.712 16.842 16.975 17.106 17.238 17.368 17.501 17.634 17.767 17.900 18.033 18.166 18.299 18.432

14.027 14.160 14.294 14.427 14.560 14.693 14.827 14.959 15.093 15.226 15.359 15.492 15.626 15.759 15.892 16.025 16.158 16.292 16.424 16.557 16.691 16.824 16.957 17.090 17.224 17.357 17.490 17.623 17.756 17.889 18.022 18.155 18.288 18.422 18.554

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.59 1.59 1.59 1.58 1.58 1.59 1.59 1.59 1.58 1.59 1.59 1.58 1.58 1.57 1.57 1.59 1.58 1.59 1.58 1.59 1.57 1.59 1.58 1.57 1.59 1.57 1.59 1.58 1.59 1.57 1.59 1.57 1.59 1.58 1.59

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

12.93 145.6 148.7 N/A N/A 21.53

in. Hg in. Hg

Velocity Traverse Data

30.24 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.36 0.36 0.36 0.35 0.36 0.36 0.36 0.36 0.36 0.35 0.36 0.36 0.36 0.35 0.36 0.36 0.36 0.35 0.36 0.36 0.35 0.36 0.36 0.36 0.35 0.36 0.35 0.35 0.35 0.35 0.36 0.35 0.35 0.36 0.35

1.31 1.30 1.31 1.32 1.30 1.32 1.31 1.31 1.31 1.31 1.31 1.31 1.31 1.32 1.30 1.31 1.31 1.31 1.31 1.31 1.30 1.31 1.31 1.30 1.31 1.30 1.31 1.31 1.31 1.31 1.32 1.30 1.31 1.31 1.31

79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

74 74 74 73 74 74 74 74 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

98 101 98 99 98 101 100 100 101 100 100 99 101 99 101 100 100 99 101 99 100 100 98 100 99 99 98 100 100 100 100 100 100 100 100

100 100 100 99 100 100 100 99 100 99 99 99 100 99 99 99 99 100 99 99 100 99 99 99 100 99 99 99 99 99 99 99 99 100 99

Page 4 of 8

Scale Weight Reading Change 3.6 3.6 3.5 3.5 3.5 3.5 3.5 3.4 3.4 3.4 3.4 3.4 3.4 3.4 3.3 3.4 3.3 3.4 3.3 3.3 3.3 3.3 3.2 3.3 3.2 3.2 3.2 3.2 3.2 3.1 3.1 3.2 3.1 3.1 3.1

0 0 -0.1 0 0 0 0 -0.1 0 0 0 0 0 0 -0.1 0.1 -0.1 0.1 -0.1 0 0 0 -0.1 0.1 -0.1 0 0 0 0 -0.1 0 0.1 -0.1 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

207.2 206.8 206.5 205.8 205.6 205.2 204.6 205.0 204.7 204.1 203.8 203.6 203.0 202.8 202.0 202.2 201.9 201.5 201.2 200.5 200.4 200.0 199.9 199.6 199.3 199.0 198.9 198.8 198.3 197.6 197.7 197.3 197.6 196.9 196.9

129 129 129 128 128 128 127 127 126 126 126 126 126 125 125 125 125 124 124 124 123 123 123 122 122 122 122 122 123 122 122 121 121 121 121

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 69 70 69 70 70 70 70 69 70 70 70 70 69 70 69

-0.046 -0.046 -0.046 -0.045 -0.045 -0.045 -0.045 -0.045 -0.045 -0.045 -0.045 -0.045 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.044 -0.043

2.3 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.1 2.2 2.1 2.2 2.2 2.2 2.2 2.3 2.2 2.3 2.3 2.3 2.3 2.3 2.2 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.2 1.2 1.1 1.1 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2

Run 5 - Fire out.xls

66


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

5 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 09:36

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.24 OMNI Equipment Numbers:

256 1

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

140 141 142 143 144 145 146 147 148 149 150 151 152 153 154 155 156 157 158 159 160 161 162 163 164 165 166 167 168 169 170 171 172 173 174

18.564 18.698 18.830 18.964 19.096 19.230 19.362 19.495 19.628 19.759 19.891 20.022 20.153 20.283 20.417 20.548 20.682 20.815 20.948 21.081 21.214 21.347 21.479 21.612 21.745 21.878 22.010 22.143 22.276 22.409 22.541 22.673 22.804 22.936 23.068

18.688 18.821 18.954 19.087 19.221 19.354 19.487 19.620 19.753 19.887 20.019 20.152 20.286 20.419 20.552 20.685 20.818 20.952 21.084 21.218 21.351 21.484 21.617 21.750 21.883 22.017 22.149 22.282 22.415 22.549 22.681 22.814 22.947 23.081 23.213

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.58 1.58 1.58 1.58 1.59 1.57 1.59 1.57 1.59 1.58 1.58 1.58 1.57 1.58 1.58 1.59 1.58 1.58 1.56 1.58 1.58 1.59 1.58 1.58 1.58 1.57 1.58 1.58 1.58 1.57 1.58 1.57 1.58 1.56 1.58

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

12.93 145.6 148.7 N/A N/A 21.53

in. Hg in. Hg

Velocity Traverse Data

30.24 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.35 0.35 0.36 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.36 0.36 0.35 0.35 0.35 0.36 0.35 0.35 0.35 0.36 0.35 0.35 0.35 0.36 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35

1.31 1.31 1.31 1.31 1.31 1.32 1.31 1.31 1.32 1.31 1.31 1.31 1.31 1.31 1.31 1.30 1.32 1.31 1.31 1.31 1.30 1.30 1.31 1.30 1.32 1.31 1.31 1.31 1.30 1.31 1.31 1.30 1.31 1.30 1.31

79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 73 74 73 74

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

99 101 99 101 99 101 99 100 100 99 99 99 99 98 101 99 101 100 100 100 100 100 99 100 100 100 99 100 100 100 99 99 99 99 99

100 99 99 99 100 99 99 99 99 100 99 99 100 99 99 99 99 100 99 100 99 99 99 99 99 100 99 99 99 100 99 99 100 100 99

Page 5 of 8

Scale Weight Reading Change 3.1 3.1 3.1 3.1 3.0 3.0 3.0 3.0 3.0 3.0 3.0 2.9 2.9 2.9 2.9 2.9 2.9 2.9 2.8 2.9 2.8 2.8 2.8 2.8 2.8 2.8 2.8 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.7

0 0 0 0 -0.1 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 -0.1 0.1 -0.1 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

196.6 196.5 196.5 196.2 195.7 195.8 195.3 195.2 195.5 195.0 195.0 194.7 194.3 194.5 194.4 194.3 194.1 194.0 194.0 194.0 193.8 193.8 193.5 193.6 193.6 193.5 193.4 193.5 193.7 193.3 193.3 193.6 193.2 193.3 193.1

121 120 120 120 120 120 120 120 120 120 120 120 120 120 120 120 120 120 120 120 121 121 121 121 121 121 120 120 120 121 120 121 120 120 121

69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

69 69 69 69 70 70 70 69 70 70 69 70 70 70 70 70 70 70 69 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

-0.043 -0.044 -0.043 -0.044 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043

2.3 2.3 2.3 2.3 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.4 2.5 2.4 2.4 2.4

1.2 1.2 1.2 1.2 1.3 1.3 1.3 1.3 1.3 1.3 1.3 1.3 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.4 1.3 1.3 1.3 1.3 1.3

Run 5 - Fire out.xls

67


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

5 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 09:36

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.24 OMNI Equipment Numbers:

256 1

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

175 176 177 178 179 180 181 182 183 184 185 186 187 188 189 190 191 192 193 194 195 196 197 198 199 200 201 202 203 204 205 206 207 208 209

23.198 23.330 23.461 23.596 23.728 23.862 23.994 24.127 24.260 24.393 24.526 24.658 24.791 24.923 25.056 25.188 25.321 25.454 25.586 25.717 25.849 25.980 26.111 26.242 26.374 26.508 26.640 26.774 26.905 27.039 27.172 27.305 27.437 27.571 27.703

23.346 23.479 23.613 23.745 23.878 24.011 24.145 24.277 24.410 24.543 24.676 24.809 24.942 25.075 25.208 25.341 25.474 25.607 25.740 25.873 26.005 26.139 26.272 26.404 26.537 26.670 26.803 26.937 27.069 27.202 27.335 27.468 27.601 27.734 27.867

Control No. P-SSAR-0001

0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.58 1.57 1.58 1.57 1.58 1.58 1.58 1.57 1.58 1.57 1.58 1.58 1.58 1.58 1.57 1.58 1.56 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.57 1.57 1.57 1.57 1.58 1.58

81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 81 82 82 82

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

12.93 145.6 148.7 N/A N/A 21.53

in. Hg in. Hg

Velocity Traverse Data

30.24 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.35 0.36 0.35 0.35 0.36 0.35 0.35 0.35 0.35 0.35 0.34 0.35 0.34 0.34 0.36 0.35 0.36 0.34 0.35 0.34 0.35 0.35 0.35 0.35 0.34 0.34 0.35 0.35 0.35 0.35 0.34 0.35 0.34 0.35 0.35

1.31 1.30 1.31 1.31 1.30 1.31 1.30 1.30 1.31 1.30 1.31 1.31 1.30 1.30 1.30 1.30 1.31 1.30 1.31 1.31 1.30 1.31 1.30 1.30 1.31 1.30 1.30 1.30 1.31 1.30 1.30 1.30 1.31 1.30 1.31

79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 79 80 80 80 80 80 80 80 80 80

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

73 73 73 73 73 74 73 73 73 73 73 74 74 74 74 74 74 74 74 74 74 73 74 74 74 74 74 74 74 74 74 74 74 74 74

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

98 99 99 102 99 101 99 100 100 100 100 99 100 99 100 99 100 100 99 99 99 99 99 99 99 101 99 101 99 101 100 100 99 101 99

99 99 100 99 99 100 100 99 99 99 99 100 100 100 100 100 100 100 100 100 99 100 100 99 100 100 99 100 99 99 99 99 99 99 99

Page 6 of 8

Scale Weight Reading Change 2.7 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.5 2.6 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.4 2.3 2.4 2.4 2.4 2.3 2.3 2.4

0 -0.1 0 0 0 0 0 0 -0.1 0.1 -0.1 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 0 0 0 -0.1 0.1 0 0 -0.1 0 0.1

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

193.2 193.0 192.8 192.9 192.9 192.8 192.7 192.6 192.3 192.2 192.1 192 192 191.5 191.6 191.4 191.6 191.3 191.2 190.7 190.5 190.7 190.1 190 189.8 189.8 189.6 189.4 189.1 188.7 188.9 188.4 188 187.8 187.7

120 120 121 121 120 120 120 120 120 120 119 120 119 119 119 119 120 119 119 119 119 119 119 119 118 118 118 117 117 118 117 118 118 118 118

69 69 69 69 69 69 69 69 69 69 69 69 69 70 69 69 69 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

-0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.043 -0.042 -0.043 -0.043 -0.042 -0.042 -0.043 -0.043 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042 -0.042

2.4 2.4 2.4 2.4 2.4 2.3 2.3 2.3 2.3 2.3 2.3 2.2 2.3 2.2 2.2 2.2 2.2 2.2 2.2 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.2 2.2 2.2 2.2 2.2

1.3 1.3 1.3 1.3 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.1 1.2 1.1 1.1 1.1 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2

Run 5 - Fire out.xls

68


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

5 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 09:36

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.24 OMNI Equipment Numbers:

256 1

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

210 211 212 213 214 215 216 217 218 219 220 221 222 223 224 225 226 227 228 229 230 231 232 233 234 235 236 237 238 239 240 241 242 243 244

27.836 27.968 28.101 28.234 28.366 28.497 28.628 28.761 28.892 29.023 29.153 29.287 29.419 29.553 29.686 29.818 29.952 30.084 30.217 30.349 30.482 30.615 30.747 30.880 31.013 31.145 31.278 31.409 31.541 31.673 31.804 31.934 32.065 32.199 32.331

28.001 28.133 28.266 28.399 28.532 28.665 28.798 28.931 29.064 29.196 29.330 29.463 29.596 29.729 29.862 29.995 30.128 30.261 30.394 30.527 30.660 30.793 30.926 31.059 31.193 31.325 31.458 31.591 31.725 31.858 31.990 32.124 32.257 32.389 32.523

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.56 1.58 1.58 1.58 1.58 1.58 1.58 1.56 1.58 1.57 1.58 1.58 1.58 1.57 1.58 1.56 1.58 1.58 1.58 1.58 1.56 1.58 1.56 1.58 1.58 1.58 1.58 1.57 1.58 1.58 1.58 1.58 1.58 1.57 1.57

82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

12.93 145.6 148.7 N/A N/A 21.53

in. Hg in. Hg

Velocity Traverse Data

30.24 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.35 0.34 0.35 0.34 0.35 0.35 0.34 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.36 0.35 0.35 0.35 0.34 0.36 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.35 0.34 0.35

1.30 1.30 1.31 1.30 1.30 1.30 1.30 1.31 1.30 1.30 1.31 1.30 1.31 1.31 1.30 1.30 1.30 1.30 1.31 1.30 1.30 1.31 1.30 1.31 1.30 1.31 1.31 1.30 1.30 1.31 1.30 1.31 1.30 1.30 1.30

80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

100 99 100 100 99 98 98 100 98 98 98 101 99 101 100 99 101 99 100 99 100 100 99 100 100 99 100 98 99 99 98 98 98 101 99

100 99 99 99 99 99 99 99 99 99 100 99 99 99 99 99 99 99 99 99 99 99 99 99 100 99 99 99 100 99 99 100 99 99 100

Page 7 of 8

Scale Weight Reading Change 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.3 2.2 2.2 2.2 2.2 2.3 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2 2.2

-0.1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 -0.1 0 0 0 0.1 -0.1 0 0 0 0 0 0 0 0 0 0 0 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

187.6 187.5 187.1 187.2 186.9 186.7 186.6 186.5 186.1 186.1 186 186.1 185.6 185.6 185.3 184.9 184.7 184.8 184.3 184 183.8 183.5 183.1 182.9 182.5 182.3 182 181.8 181.5 181.2 180.9 180.6 180 179.7 179.4

117 118 117 117 116 115 115 114 114 113 113 113 113 113 113 112 112 112 112 111 111 112 112 112 111 111 111 111 110 110 110 110 110 110 110

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 71 71 71 71 71 71 71

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

-0.042 -0.042 -0.042 -0.042 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.041 -0.040 -0.041 -0.041 -0.041 -0.040 -0.040 -0.041 -0.041 -0.041 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040

2.2 2.2 2.2 2.2 2.1 2.1 2.1 2 2 1.9 1.9 1.8 1.8 1.8 1.8 1.7 1.7 1.7 1.7 1.7 1.7 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6

1.2 1.2 1.2 1.2 1.2 1.2 1.1 1.1 1 1 1 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8

Run 5 - Fire out.xls

69


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

5 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 09:36

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin

Total Sampling Time: Recording Interval: Background Sample Volume:

(1) Middle

1.003

(2)

End

Average

30.24 OMNI Equipment Numbers:

256 1

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

245 246 247 248 249 250 251 252 253 254 255 256 Avg/Tot

32.465 32.597 32.730 32.863 32.996 33.129 33.262 33.394 33.527 33.659 33.791 33.924 33.924

32.656 32.789 32.922 33.055 33.188 33.322 33.454 33.587 33.721 33.854 33.987 34.120 34.120

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

1.57 1.57 1.58 1.58 1.58 1.58 1.57 1.57 1.58 1.58 1.58 1.57 1.58

82 82 82 82 82 82 82 82 82 82 82 82 80

ft/sec. scfm scfm cfm @ N/A cfm @ N/A Dry Basis %

Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Orifice Meter 1 dH 1 Temp ("H2O) (°F)

12.93 145.6 148.7 N/A N/A 21.53

in. Hg in. Hg

Velocity Traverse Data

30.24 "Hg

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.35 0.35 0.34 0.35 0.35 0.35 0.35 0.34 0.35 0.35 0.35 0.35

1.30 1.30 1.31 1.30 1.31 1.29 1.30 1.30 1.30 1.30 1.31 1.30 1.31

80 80 80 80 80 80 80 80 80 80 80 80 78

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

74 74 74 74 74 74 74 74 74 74 73 74 75

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

101 99 100 100 100 100 100 99 100 99 99 100 100

99 99 99 99 99 100 99 99 100 99 99 99 100

Page 8 of 8

Scale Weight Reading Change 2.2 2.2 2.2 2.2 2.1 2.2 2.2 2.2 2.2 2.2 2.2 2.2

0 0 0 0 -0.1 0.1 0 0 0 0 0 0

Temperature Data (°F) Avg. Stove Surface Temp 179.1 178.8 178.5 178.4 178 177.7 177.5 176.8 176.5 176 175.8 175.6 128.5

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

110 109 109 109 109 109 109 110 111 111 111 109

70 70 70 70 70 70 70 70 70 70 70 70 70

71 71 71 71 71 71 71 71 71 71 70 70 70

70 70 70 70 71 71 70 70 70 70 70 70 70

-0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.040 -0.048

1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.6

0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8

Run 5 - Fire out.xls

70


71


72


73


74


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 6

OMNI-Test Laboratories, Inc.

75


OMNI-Test Laboratories, Inc.

Wood Heater Test Results - ASTM E2780 / ASTM E2515 Manufacturer: Model: Project No.: Tracking No.: Run: Test Date:

Burn Rate Average Tunnel Temperature Average Gas Velocity in Dilution Tunnel - vs Average Gas Flow Rate in Dilution Tunnel - Qsd Average Delta p Total Time of Test

RAIS Q-Tee II 0138WS016E 2138 6 10/22/15

1.28 kg/hr dry 90 degrees Fahrenheit 13.10 feet/second 8802.2 dscf/hour 0.048 inches H20 111 minutes

AMBIENT Total Sample Volume - Vm Average Gas Meter Temperature Total Sample Volume (Standard Conditions) - Vmstd Total Particulates - mn Particulate Concentration (dry-standard) - Cr/Cs Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

0.000 cubic feet 74 degrees Fahrenheit 0.000 dscf 0 mg

SAMPLE TRAIN 1 14.679 cubic feet 84 degrees Fahrenheit 14.612 dscf 3.1 mg

SAMPLE TRAIN 2

FIRST HOUR FILTER (TRAIN 1)

14.897 cubic feet 81 degrees Fahrenheit 14.780 dscf 4.7 mg

7.902 cubic feet 82 degrees Fahrenheit 7.893 dscf 1.6 mg

0.000000 grams/dscf

0.00021 grams/dscf

0.00032 grams/dscf

0.00020 grams/dscf

0.00 grams 0.00 grams/hour

3.45 grams 1.87 grams/hour 1.46 g/kg

5.18 grams 2.80 grams/hour 2.19 g/kg

1.78 grams 1.78 grams/hour 0.87 g/kg

Difference from Average Total Particulate Emissions

0.86 grams

0.86 grams

Dual Train Comparison Results Are Not Acceptable Complete Test Run Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor First Hour Emissions Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

Control No. P-XXXX-XXXX

FINAL AVERAGE RESULTS 4.32 grams 2.33 grams/hour 1.83 grams/kg

1.78 grams 1.78 grams/hour 0.87 grams/kg

Run 6 - Cat III.xls

76


OMNI-Test Laboratories, Inc. Manufacturer: Rais Model: Q-Tee II Date: 10/22/15 Run: 6 Control #: 0138WS016E Test Duration: 111 Output Category: III

Technicians:

A. Kravitz

Test Results in Accordance with CSA B415.1-09 HHV Basis 70.5% 94.3% 75%

LHV Basis 76.2% 94.3% 80.7%

Output Rate (kJ/h) Burn Rate (kg/h) Input (kJ/h)

17,787 1.27 25,237

16,873 2.81 23,940

(Btu/h) (lb/h) (Btu/h)

Test Load Weight (dry kg) MC wet (%) MC dry (%) Particulate (g ) CO (g) Test Duration (h)

2.36 17.55 21.29 0 196 1.85

5.19

dry lb

Particulate 0.00 0.00 0.00 0.00

CO 5.96 83.26 106.07 13.86

Overall Efficiency Combustion Efficiency Heat Transfer Efficiency

Emissions g/MJ Output g/kg Dry Fuel g/h lb/MM Btu Output Air/Fuel Ratio (A/F) VERSION:

2.3

13.76 3/23/2010

77


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

6 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 16:59

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.24

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

111 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.23

30.22

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34

0.000 0.119 0.252 0.384 0.515 0.646 0.778 0.908 1.040 1.171 1.305 1.436 1.570 1.701 1.834 1.965 2.098 2.229 2.361 2.493 2.626 2.757 2.889 3.021 3.153 3.284 3.415 3.546 3.677 3.807 3.938 4.068 4.200 4.333 4.465

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.23 "Hg

0.000 0.118 0.253 0.388 0.524 0.659 0.793 0.928 1.063 1.198 1.332 1.466 1.601 1.735 1.869 2.003 2.137 2.270 2.404 2.538 2.672 2.806 2.940 3.073 3.207 3.341 3.474 3.608 3.742 3.876 4.009 4.143 4.277 4.411 4.545

0.12 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.12 0.14 0.14 0.14 0.14 0.13 0.14 0.14 0.14 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 0.57 1.60 1.61 1.61 1.60 1.59 1.58 1.59 1.57 1.59 1.58 1.58 1.58 1.57 1.57 1.57 1.57 1.57 1.57 1.57 1.56 1.57 1.57 1.57 1.55 1.56 1.56 1.56 1.57 1.56 1.55 1.57 1.56 1.56 1.56

77 77 77 77 77 77 78 78 78 78 78 78 79 79 79 79 80 80 80 80 80 81 81 81 81 81 82 82 82 82 82 83 83 83 83

13.10 145.6 146.7

ft/sec. scfm scfm 0 cfm @ -6 0 cfm @ -4 21.29 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

0.42 0.33 0.32 0.34 0.34 0.33 0.33 0.35 0.34 0.35 0.34 0.35 0.34 0.35 0.35 0.34 0.35 0.35 0.35 0.34 0.35 0.34 0.35 0.35 0.35 0.35 0.34 0.35 0.35 0.36 0.36 0.36 0.36 0.35 0.36

0.02 1.36 1.35 1.36 1.36 1.35 1.34 1.35 1.34 1.34 1.33 1.34 1.33 1.32 1.33 1.32 1.32 1.33 1.32 1.32 1.32 1.32 1.32 1.32 1.32 1.32 1.32 1.31 1.32 1.32 1.31 1.32 1.31 1.31 1.32

76 76 76 76 76 76 76 76 76 76 77 77 77 77 77 77 78 78 78 78 78 78 79 79 79 79 79 79 80 80 80 80 80 80 80

0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

81 112 125 124 117 111 104 100 98 97 96 95 95 94 94 94 94 94 94 94 94 93 94 93 93 94 93 93 93 93 93 93 93 92 92

Dilution Tunnel Center dP 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

Page 1 of 4

Pro. Rate 1

Pro. Rate 2

93 105 104 103 102 102 100 102 101 103 101 103 100 102 100 102 100 101 101 102 100 101 101 101 100 100 100 100 99 100 99 100 101 100

91 105 105 105 103 102 102 102 102 101 101 102 101 101 101 101 100 101 101 101 101 101 100 100 101 100 100 100 100 100 100 100 100 100

Scale Weight Reading Change 6.3 5.9 5.7 5.4 5.2 5.1 4.9 4.8 4.7 4.6 4.5 4.3 4.2 4.1 4.0 3.8 3.7 3.6 3.5 3.4 3.3 3.1 3.0 2.9 2.8 2.7 2.6 2.5 2.5 2.3 2.3 2.2 2.1 2.0 1.9

-0.4 -0.2 -0.3 -0.2 -0.1 -0.2 -0.1 -0.1 -0.1 -0.1 -0.2 -0.1 -0.1 -0.1 -0.2 -0.1 -0.1 -0.1 -0.1 -0.1 -0.2 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 0 -0.2 0 -0.1 -0.1 -0.1 -0.1

Temperature Data (°F) Avg. Stove Surface Temp 364.3 361.6 362.4 367.9 372.0 377.6 382.1 385.6 386.0 386.5 385.7 385.7 384.7 383.8 383.9 383.6 384.1 385.4 386.8 388.3 389.5 391.6 393.7 394.8 397.0 399.0 400.5 402.9 403.6 405.8 407.0 408.6 409.9 411.1 412.6

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

366 427 575 587 543 498 432 395 376 365 358 355 349 346 348 351 351 355 355 361 366 368 366 368 369 368 372 374 372 370 366 368 365 365 364

73 74 75 75 75 75 75 75 75 75 75 75 75 75 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76

73 75 77 77 78 78 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77

74 74 74 74 74 74 74 74 74 74 73 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74

-0.093 -0.102 -0.108 -0.104 -0.103 -0.097 -0.093 -0.090 -0.089 -0.089 -0.088 -0.087 -0.088 -0.086 -0.088 -0.088 -0.087 -0.088 -0.088 -0.088 -0.089 -0.089 -0.088 -0.088 -0.089 -0.089 -0.088 -0.089 -0.088 -0.087 -0.088 -0.088 -0.087 -0.087 -0.086

5.4 5.3 5.2 11.5 12.6 12.3 11.1 10.2 9.2 8.3 7.5 7 6.9 7 7.3 7.4 7.7 8.2 8.9 9.3 9.5 9.8 9.9 9.9 9.9 9.9 10.1 10.3 10.2 10 9.9 9.8 9.8 9.8 9.7

0.7 0.1 0.4 0.5 0.7 0.6 0.4 0.5 0.9 1.2 1.4 1.4 1.5 1.5 1.5 1.6 1.6 1.5 1.2 1 0.9 0.8 0.7 0.6 0.5 0.5 0.5 0.5 0.4 0.3 0.3 0.2 0.2 0.2 0.2

Run 6 - Cat III.xls

78


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

6 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 16:59

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.24

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

111 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.23

30.22

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69

4.598 4.730 4.863 4.994 5.127 5.259 5.392 5.524 5.656 5.788 5.921 6.053 6.185 6.317 6.448 6.580 6.711 6.842 6.972 7.104 7.237 7.370 7.503 7.636 7.768 7.902 8.038 8.171 8.304 8.437 8.570 8.702 8.835 8.968 9.102

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.23 "Hg

4.679 4.812 4.947 5.081 5.214 5.349 5.483 5.616 5.751 5.885 6.019 6.153 6.288 6.421 6.556 6.690 6.824 6.959 7.093 7.227 7.362 7.496 7.631 7.765 7.899 8.034 8.168 8.303 8.438 8.572 8.707 8.842 8.976 9.110 9.245

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.13 0.14 0.14 0.13 0.14 0.14 0.13 0.13 0.14

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.56 1.56 1.57 1.56 1.57 1.57 1.56 1.57 1.56 1.57 1.55 1.56 1.56 1.57 1.56 1.57 1.56 1.57 1.56 1.56 1.56 1.57 1.57 1.56 1.56 1.56 1.57 1.57 1.57 1.57 1.57 1.57 1.57 1.57 1.56

83 83 84 84 84 84 84 84 84 84 84 84 85 85 85 85 85 85 85 85 85 85 85 85 85 85 85 85 85 85 85 85 86 86 86

13.10 145.6 146.7

ft/sec. scfm scfm 0 cfm @ -6 0 cfm @ -4 21.29 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.36 0.35 0.36 0.35 0.34 0.35 0.35 0.35 0.36 0.35 0.35 0.36 0.35 0.36 0.36 0.35 0.35 0.35 0.36 0.36 0.35 0.35 0.36 0.36 0.36 0.35 0.35 0.37 0.35 0.37 0.36 0.36 0.37 0.36 0.37

1.32 1.31 1.32 1.32 1.31 1.32 1.32 1.31 1.32 1.31 1.31 1.32 1.32 1.31 1.32 1.31 1.31 1.32 1.32 1.32 1.32 1.33 1.32 1.32 1.32 1.32 1.32 1.33 1.32 1.32 1.33 1.33 1.31 1.32 1.32

81 81 81 81 81 81 81 81 81 81 81 81 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82 82

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

92 92 92 92 92 92 92 92 92 92 91 91 91 90 90 90 89 89 89 89 88 88 88 87 88 87 87 87 87 86 86 86 86 85 86

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

101 100 101 99 101 100 101 100 100 100 101 100 100 100 99 100 99 99 98 100 100 100 100 100 99 101 102 100 100 100 100 99 100 100 101

100 99 101 100 99 101 100 99 101 100 100 100 100 99 100 100 100 100 100 100 100 99 100 99 99 100 99 100 100 99 100 100 99 99 100

Page 2 of 4

Scale Weight Reading Change 1.8 1.8 1.7 1.6 1.6 1.5 1.4 1.3 1.3 1.2 1.2 1.1 1.1 1.1 1.1 1.0 1.0 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.8 0.8 0.8 0.7 0.8 0.8 0.7 0.7 0.7 0.7 0.7

-0.1 0 -0.1 -0.1 0 -0.1 -0.1 -0.1 0 -0.1 0 -0.1 0 0 0 -0.1 0 -0.1 0 0 0 0 0 0 -0.1 0 0 -0.1 0.1 0 -0.1 0 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

413.2 414.0 414.9 415.9 416.8 417.3 417.8 418.1 418.5 418.7 418.7 418.6 417.3 416.5 414.1 412.5 409.7 408.1 405.6 402.9 401.0 398.2 396.0 393.9 391.6 389.0 387.3 384.6 382.6 380.2 378.0 375.8 373.5 371.1 369.7

362 363 358 358 358 357 357 353 349 346 342 338 332 325 320 316 310 307 302 297 295 289 286 284 281 279 275 272 267 266 264 263 261 257 255

76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 75 75 75 75 75 75 75 75 75 75 75 75

77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76 76

74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 75 74 74 74 75 74 74 75 74 75 75 75 75 74 75 75 75 75 74

-0.087 -0.086 -0.086 -0.086 -0.085 -0.086 -0.086 -0.085 -0.084 -0.083 -0.083 -0.083 -0.082 -0.081 -0.081 -0.080 -0.079 -0.078 -0.078 -0.077 -0.076 -0.076 -0.074 -0.075 -0.074 -0.074 -0.074 -0.073 -0.072 -0.072 -0.071 -0.071 -0.071 -0.071 -0.070

9.5 9.4 9.4 9.4 9.3 9.2 9.2 9.3 9.3 9.2 8.5 8 7.7 7.6 7.3 7.1 7 6.8 6.7 6.4 6.1 5.9 5.9 5.8 5.7 5.4 5.3 5.3 5.3 5.2 5.3 5.2 5.2 5.2 5.2

0.2 0.2 0.2 0.2 0.2 0.2 0.1 0.1 0.1 0.2 0.2 0.2 0.1 0.1 0 0 0.1 0.1 0.1 0.1 0.1 0.1 0.2 0.2 0.2 0.3 0.4 0.4 0.4 0.4 0.5 0.5 0.5 0.5 0.5

Run 6 - Cat III.xls

79


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

6 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 16:59

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.24

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

111 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.23

30.22

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.23 "Hg

70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104

9.234 9.367 9.498 9.631 9.762 9.893 10.024 10.156 10.291 10.424 10.558 10.691 10.824 10.958 11.090 11.224 11.356 11.490 11.623 11.756 11.889 12.023 12.156 12.288 12.420 12.552 12.684 12.815 12.947 13.079 13.213 13.346 13.479 13.613 13.745

9.379 9.514 9.648 9.783 9.917 10.052 10.187 10.321 10.456 10.591 10.725 10.859 10.994 11.128 11.263 11.398 11.532 11.667 11.801 11.936 12.070 12.205 12.340 12.474 12.609 12.744 12.878 13.013 13.147 13.282 13.417 13.551 13.686 13.820 13.955

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.14 0.13 0.14 0.13 0.14 0.14 0.13 0.14 0.14 0.13 0.13 0.14 0.13 0.14 0.14 0.13 0.14 0.13 0.14 0.13 0.14 0.14 0.13 0.14 0.14 0.13 0.14 0.13 0.14 0.14 0.13 0.14 0.13 0.14

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.58 1.57 1.57 1.57 1.57 1.57 1.58 1.57 1.56 1.57 1.57 1.57 1.55 1.57 1.57 1.57 1.57 1.56 1.57 1.57 1.58 1.57 1.58 1.56 1.57 1.58 1.56 1.58 1.57 1.58 1.58 1.58 1.58 1.57 1.57

86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86 86

13.10 145.6 146.7

ft/sec. scfm scfm 0 cfm @ -6 0 cfm @ -4 21.29 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.37 0.36 0.36 0.37 0.36 0.36 0.36 0.36 0.36 0.36 0.36 0.36 0.36 0.35 0.37 0.37 0.36 0.37 0.36 0.36 0.37 0.36 0.37 0.37 0.36 0.37 0.36 0.36 0.37 0.37 0.37 0.35 0.37 0.36 0.36

1.31 1.32 1.33 1.32 1.32 1.33 1.32 1.33 1.32 1.31 1.31 1.33 1.32 1.31 1.32 1.33 1.32 1.32 1.33 1.33 1.32 1.33 1.32 1.32 1.32 1.31 1.31 1.32 1.33 1.32 1.33 1.33 1.32 1.33 1.33

83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 83 82 82 82 82 82 82 82 82 82 82 82 82

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

85 85 85 85 85 84 85 85 84 84 84 84 84 84 84 84 84 84 84 83 83 83 83 83 83 83 83 83 83 83 83 83 83 82 83

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

99 100 98 100 98 98 98 99 101 100 100 100 100 100 99 100 99 100 100 100 100 100 100 99 99 99 99 98 99 99 100 100 100 100 99

99 100 99 100 99 100 100 99 100 100 99 99 100 99 100 100 99 100 99 100 99 100 100 99 100 100 99 100 99 100 100 99 100 99 100

Page 3 of 4

Scale Weight Reading Change 0.7 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.2 0.2 0.2

0 0 -0.1 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 -0.1 0 0 0 0 0 0 -0.1 0 0 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

368.4 366.8 364.8 363.2 360.9 359.9 358.2 357.0 355.4 354.1 352.5 351.1 350.3 348.4 347.4 346.7 344.6 343.7 343.2 341.8 341.0 340.0 339.1 338.2 337.5 337.0 335.8 335.2 334.1 333.8 333.2 332.4 331.2 331.1 330.4

254 252 250 250 248 247 244 244 243 241 241 238 237 235 234 234 233 231 230 230 230 227 227 225 225 226 225 225 226 225 225 222 224 222 222

75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74 74

76 76 76 76 76 76 76 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75 75

75 74 75 74 74 75 74 74 74 74 74 74 74 75 75 74 74 75 74 74 74 75 75 74 74 74 75 74 74 74 74 74 74 74 74

-0.070 -0.069 -0.069 -0.069 -0.069 -0.069 -0.068 -0.068 -0.068 -0.067 -0.067 -0.067 -0.067 -0.066 -0.066 -0.066 -0.066 -0.066 -0.065 -0.065 -0.065 -0.064 -0.065 -0.065 -0.064 -0.064 -0.064 -0.064 -0.064 -0.064 -0.064 -0.064 -0.064 -0.064 -0.063

5.2 5.2 5.2 5.1 5.1 5.1 5.1 5.1 5.1 5.1 5.1 5 5 5 5.1 5.1 5.1 5.1 5.1 5.2 5.2 5.2 5.2 5.2 5.2 5.2 5.1 5.1 5.1 5.2 5.2 5.2 5.1 5.1 5

0.5 0.5 0.5 0.5 0.5 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.8

Run 6 - Cat III.xls

80


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

6 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 22-Oct-15 16:59

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.24

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

111 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.23

30.22

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.23 "Hg

105 106 107 108 109 110 111 Avg/Tot

13.880 14.013 14.147 14.280 14.414 14.547 14.679 14.679

14.090 14.224 14.359 14.494 14.628 14.762 14.897 14.897

Control No. P-SSAR-0001

0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.14 0.13 0.14 0.14 0.13 0.13 0.14 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.57 1.58 1.57 1.58 1.57 1.58 1.58 1.56

86 86 86 86 86 86 86 84

13.10 145.6 146.7

ft/sec. scfm scfm 0 cfm @ -6 0 cfm @ -4 21.29 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.032

0.036

0.049

0.036

0.033

0.041

0.046

0.024

0.048

81

81

81

81

81

81

81

81

81

Vstrav

13.00

ft/sec

Vscent

14.63

ft/sec

Fp

0.889

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.400 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.36 0.36 0.37 0.37 0.36 0.35 0.35

1.32 1.33 1.32 1.31 1.31 1.33 1.33 1.31

82 82 82 82 82 83 83 81

0.6 0.6 0.6 0.6 0.6 0.6 0.6

83 82 83 82 83 82 82 90

0.048 0.048 0.048 0.048 0.048 0.048 0.048 0.048

101 99 100 99 100 99 99 100

100 99 100 100 99 99 99 100

Page 4 of 4

Scale Weight Reading Change 0.2 0.2 0.2 0.2 0.1 0.1 0.0

0 0 0 0 -0.1 0 -0.1

Temperature Data (°F) Avg. Stove Surface Temp 330.2 328.9 329.0 328.1 327.5 327.0 326.3 38.0

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

220 222 221 218 218 217 218

74 74 74 74 74 74 74 75

75 75 75 75 75 75 75 76

74 74 74 74 74 74 74 74

-0.063 -0.063 -0.063 -0.063 -0.063 -0.062 -0.062 -0.077

5 5 5.1 5 4.9 4.9 4.8

0.8 0.8 0.7 0.7 0.7 0.7 0.7

Run 6 - Cat III.xls

81


82


83


84


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Run 7

OMNI-Test Laboratories, Inc.

85


OMNI-Test Laboratories, Inc.

Wood Heater Test Results - ASTM E2780 / ASTM E2515 Manufacturer: Model: Project No.: Tracking No.: Run: Test Date:

Burn Rate Average Tunnel Temperature Average Gas Velocity in Dilution Tunnel - vs Average Gas Flow Rate in Dilution Tunnel - Qsd Average Delta p Total Time of Test

RAIS Q-Tee II 0138WS016E 2138 7 10/23/15

0.87 kg/hr dry 83 degrees Fahrenheit 13.44 feet/second 9123.1 dscf/hour 0.054 inches H20 154 minutes

AMBIENT Total Sample Volume - Vm Average Gas Meter Temperature Total Sample Volume (Standard Conditions) - Vmstd Total Particulates - mn Particulate Concentration (dry-standard) - Cr/Cs Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

0.000 cubic feet 69 degrees Fahrenheit 0.000 dscf 0 mg

SAMPLE TRAIN 1 20.372 cubic feet 78 degrees Fahrenheit 20.439 dscf 2.5 mg

SAMPLE TRAIN 2 20.669 cubic feet 76 degrees Fahrenheit 20.644 dscf 1.6 mg

FIRST HOUR FILTER (TRAIN 1) 7.904 cubic feet 75 degrees Fahrenheit 7.974 dscf 0.5 mg

0.000000 grams/dscf

0.00012 grams/dscf

0.00008 grams/dscf

0.00006 grams/dscf

0.00 grams 0.00 grams/hour

2.86 grams 1.12 grams/hour 1.28 g/kg

1.81 grams 0.71 grams/hour 0.81 g/kg

0.57 grams 0.57 grams/hour 0.31 g/kg

Difference from Average Total Particulate Emissions

0.52 grams

0.52 grams

Dual Train Comparison Results Are Acceptable Complete Test Run Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor First Hour Emissions Total Particulate Emissions - ET Particulate Emission Rate Emissisons Factor

Control No. P-XXXX-XXXX

FINAL AVERAGE RESULTS 2.34 grams 0.91 grams/hour 1.05 grams/kg

0.57 grams 0.57 grams/hour 0.31 grams/kg

Run 7 - Cat I.xls

86


OMNI-Test Laboratories, Inc. Manufacturer: Rais Model: Q-Tee II Date: 10/23/15 Run: 7 Control #: 0138WS016E Test Duration: 154 Output Category: I

Technicians:

A. Kravitz S. Button

Test Results in Accordance with CSA B415.1-09 HHV Basis 69.7% 92.7% 75%

LHV Basis 75.3% 92.7% 81.2%

Output Rate (kJ/h) Burn Rate (kg/h) Input (kJ/h)

11,969 0.87 17,171

11,354 1.91 16,288

(Btu/h) (lb/h) (Btu/h)

Test Load Weight (dry kg) MC wet (%) MC dry (%) Particulate (g ) CO (g) Test Duration (h)

2.22 18.28 22.37 0 245 2.57

4.90

dry lb

Particulate 0.00 0.00 0.00 0.00

CO 7.99 110.26 95.57 18.56

Overall Efficiency Combustion Efficiency Heat Transfer Efficiency

Emissions g/MJ Output g/kg Dry Fuel g/h lb/MM Btu Output Air/Fuel Ratio (A/F) VERSION:

2.3

14.65 3/23/2010

87


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

7 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 23-Oct-15 10:46

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.20

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

154 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.17

30.14

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34

0.000 0.125 0.258 0.390 0.521 0.652 0.783 0.914 1.045 1.175 1.306 1.438 1.571 1.703 1.835 1.967 2.099 2.231 2.364 2.495 2.628 2.759 2.891 3.023 3.155 3.287 3.418 3.549 3.680 3.811 3.941 4.071 4.203 4.334 4.468

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.17 "Hg

0.000 0.126 0.261 0.396 0.529 0.664 0.799 0.933 1.067 1.201 1.335 1.469 1.604 1.737 1.872 2.005 2.139 2.273 2.407 2.541 2.674 2.809 2.942 3.076 3.210 3.343 3.477 3.611 3.744 3.878 4.012 4.145 4.279 4.413 4.547

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.14 0.14 0.13 0.14 0.14 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.03 1.60 1.60 1.60 1.60 1.59 1.59 1.59 1.59 1.59 1.59 1.57 1.58 1.57 1.58 1.58 1.58 1.57 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.57 1.58 1.58 1.58 1.58 1.58 1.57 1.58 1.57

69 69 70 70 70 70 70 70 71 71 71 72 72 72 72 73 73 73 73 74 74 74 74 75 75 75 75 76 76 76 76 76 76 77 77

13.44 148.2 152.1

ft/sec. scfm scfm 0 cfm @ -5 0 cfm @ -4 22.37 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.034

0.058

0.048

0.027

0.024

0.054

0.053

0.022

0.054

89

89

89

89

89

89

89

89

89

Vstrav

13.51

ft/sec

Vscent

15.64

ft/sec

Fp

0.864

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.417 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

0.38 0.34 0.35 0.34 0.35 0.35 0.35 0.35 0.35 0.36 0.36 0.37 0.36 0.35 0.36 0.36 0.36 0.37 0.37 0.36 0.35 0.37 0.36 0.36 0.37 0.36 0.36 0.37 0.36 0.36 0.36 0.37 0.37 0.37 0.35

0.50 1.34 1.35 1.35 1.35 1.35 1.35 1.35 1.35 1.35 1.33 1.34 1.34 1.33 1.34 1.34 1.32 1.34 1.33 1.32 1.34 1.32 1.33 1.34 1.32 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.32 1.32

68 68 68 69 69 69 69 69 69 69 70 70 70 70 71 71 71 71 72 72 72 72 72 73 73 73 73 74 74 74 74 74 74 75 75

0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7

89 106 122 127 123 112 100 96 93 91 90 89 89 88 88 87 87 87 87 87 86 86 87 87 87 86 86 86 86 86 86 86 86 86 86

Dilution Tunnel Center dP 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054

Page 1 of 5

Pro. Rate 1

Pro. Rate 2

98 106 105 104 103 102 102 101 100 101 102 102 101 101 101 101 101 102 100 102 100 101 101 101 101 100 100 100 100 99 99 101 100 102

97 106 106 104 105 104 102 102 102 102 102 102 101 102 100 101 101 101 101 100 102 100 101 101 100 101 101 100 101 101 100 101 100 100

Scale Weight Reading Change 6.0 6.0 5.8 5.5 5.3 5.2 5.0 5.0 4.9 4.8 4.7 4.6 4.5 4.4 4.3 4.2 4.1 4.0 3.9 3.8 3.7 3.6 3.5 3.5 3.3 3.2 3.2 3.0 3.0 2.9 2.8 2.7 2.6 2.6 2.5

0 -0.2 -0.3 -0.2 -0.1 -0.2 0 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 -0.1 0 -0.2 -0.1 0 -0.2 0 -0.1 -0.1 -0.1 -0.1 0 -0.1

Temperature Data (°F) Avg. Stove Surface Temp 351.1 346.9 348.9 355.7 367.7 375.8 382.3 384.1 385.9 383.7 380.4 377.1 374.5 371.9 370.8 369.8 369.8 369.7 369.2 369.3 369.9 370.6 371.2 371.9 373.1 374.3 376.1 377.5 378.2 379.1 380.6 380.7 382.2 383.1 383.8

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

285 371 526 578 550 507 427 387 361 344 332 325 317 316 312 306 307 307 308 311 312 315 320 323 324 324 322 323 323 324 325 325 323 322 321

68 69 70 71 70 70 70 70 70 69 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70

66 64 62 62 62 62 63 63 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64 64

68 69 69 69 69 69 69 69 69 69 68 68 68 68 69 68 68 68 68 68 69 69 69 69 69 68 68 69 69 69 69 69 69 69 69

-0.075 -0.103 -0.108 -0.109 -0.104 -0.099 -0.093 -0.090 -0.089 -0.088 -0.088 -0.087 -0.086 -0.085 -0.085 -0.085 -0.085 -0.085 -0.085 -0.085 -0.085 -0.084 -0.086 -0.086 -0.086 -0.086 -0.086 -0.085 -0.084 -0.084 -0.086 -0.086 -0.085 -0.085 -0.085

5.4 5.2 3.2 6.2 10 10.9 11.5 11.8 11.4 10.1 8.8 8 7.7 7.6 7.6 7.6 7.6 7.7 7.8 8.1 8.6 9 9.3 9.7 10 10.1 10 9.9 9.8 9.7 9.8 10 10.1 10 9.9

0.4 0.5 0.4 0.5 0.8 0.9 0.8 0.6 0.5 0.6 0.8 0.9 1 1.1 1.1 1.2 1.3 1.4 1.4 1.3 1.1 0.9 0.9 0.9 0.7 0.6 0.5 0.5 0.5 0.5 0.5 0.5 0.4 0.4 0.3

Run 7 - Cat I.xls

88


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

7 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 23-Oct-15 10:46

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.20

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

154 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.17

30.14

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69

4.599 4.733 4.865 4.998 5.130 5.263 5.395 5.528 5.660 5.792 5.924 6.057 6.189 6.321 6.452 6.583 6.715 6.844 6.975 7.106 7.240 7.372 7.506 7.638 7.771 7.904 8.037 8.170 8.302 8.435 8.568 8.700 8.832 8.966 9.098

Control No. P-SSAR-0001

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.17 "Hg

4.680 4.815 4.949 5.082 5.217 5.351 5.484 5.618 5.753 5.886 6.021 6.155 6.288 6.423 6.557 6.691 6.825 6.959 7.094 7.228 7.362 7.496 7.631 7.765 7.899 8.034 8.168 8.302 8.437 8.570 8.705 8.839 8.973 9.108 9.242

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.58 1.57 1.58 1.57 1.58 1.57 1.58 1.57 1.58 1.58 1.58 1.56 1.57 1.56 1.58 1.56 1.58 1.58 1.57 1.58 1.57 1.56 1.56 1.58 1.58 1.58 1.57 1.58 1.57 1.58 1.58 1.58 1.58 1.57 1.58

77 77 77 77 78 78 78 78 78 78 78 78 79 79 79 79 79 79 79 79 79 79 79 79 79 80 80 80 80 80 80 80 80 80 80

13.44 148.2 152.1

ft/sec. scfm scfm 0 cfm @ -5 0 cfm @ -4 22.37 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.034

0.058

0.048

0.027

0.024

0.054

0.053

0.022

0.054

89

89

89

89

89

89

89

89

89

Vstrav

13.51

ft/sec

Vscent

15.64

ft/sec

Fp

0.864

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.417 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.36 0.37 0.36 0.36 0.36 0.36 0.36 0.37 0.37 0.36 0.37 0.36 0.36 0.36 0.36 0.36 0.37 0.37 0.36 0.36 0.36 0.37 0.36 0.37 0.36 0.37 0.36 0.36 0.37 0.36 0.36 0.37 0.36 0.35 0.36

1.33 1.33 1.33 1.33 1.32 1.32 1.33 1.33 1.32 1.33 1.32 1.32 1.33 1.32 1.33 1.33 1.33 1.32 1.33 1.33 1.33 1.33 1.33 1.32 1.33 1.33 1.32 1.33 1.33 1.32 1.33 1.32 1.32 1.33 1.33

75 75 75 75 75 76 76 76 76 76 76 76 76 76 76 76 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 78 78 78

0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0.7 0.6 0.7 0.7 0.7 0.6 0.7 0.6 0.6 0.7 0.6 0.6 0.6 0.7

86 87 87 86 87 87 87 87 88 87 86 87 87 86 86 85 85 84 84 84 84 83 84 84 84 83 83 83 82 82 82 82 82 82 82

0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054

100 102 100 101 100 101 100 101 100 100 100 101 100 100 99 99 100 98 99 99 101 100 101 100 101 100 100 100 99 100 100 99 99 101 99

100 101 100 100 101 100 100 100 101 100 101 100 100 101 100 100 100 100 101 100 100 100 101 100 100 100 100 100 100 99 100 100 99 100 99

Page 2 of 5

Scale Weight Reading Change 2.4 2.3 2.2 2.1 2.1 2.0 1.9 1.8 1.7 1.6 1.6 1.5 1.5 1.4 1.4 1.3 1.3 1.2 1.2 1.2 1.2 1.1 1.1 1.1 1.1 1.1 1.1 1.1 1.0 1.0 1.0 1.0 1.0 0.9 0.9

-0.1 -0.1 -0.1 -0.1 0 -0.1 -0.1 -0.1 -0.1 -0.1 0 -0.1 0 -0.1 0 -0.1 0 -0.1 0 0 0 -0.1 0 0 0 0 0 0 -0.1 0 0 0 0 -0.1 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

384.4 385.2 386.3 387.9 389.5 391.0 392.5 394.8 396.4 398.4 399.8 401.6 402.4 402.9 402.4 401.7 399.4 397.5 395.4 393.7 391.6 389.5 387.3 385.0 382.8 379.7 376.8 374.4 372.0 369.7 366.8 364.3 361.6 359.7 357.3

322 321 326 325 327 329 330 329 330 332 331 327 322 319 312 307 302 299 296 288 283 279 274 271 268 264 261 259 257 251 248 247 247 243 241

70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 71 71 72 71 71 71 71 71 71

64 64 64 64 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65 65

69 69 69 68 68 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69

-0.084 -0.085 -0.085 -0.085 -0.085 -0.085 -0.086 -0.085 -0.085 -0.085 -0.085 -0.084 -0.084 -0.083 -0.081 -0.081 -0.080 -0.080 -0.079 -0.078 -0.078 -0.076 -0.076 -0.075 -0.075 -0.074 -0.074 -0.073 -0.073 -0.072 -0.072 -0.071 -0.071 -0.070 -0.070

10.1 10.3 10.5 10.6 10.5 10.4 10.3 10.5 10.6 10.5 10.2 9.9 9.5 9.2 8.6 7.9 7.4 7.2 7.1 7.1 7 6.6 6.1 5.9 5.7 5.7 5.7 5.5 5.5 5.4 5.3 5.3 5.2 5.3 5.3

0.3 0.3 0.4 0.4 0.4 0.5 0.4 0.5 0.6 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0.1 0.2 0.2 0.3 0.1 0.1 0.1 0.1 0.2 0.3 0.4 0.5 0.5 0.5 0.5 0.6 0.6 0.6 0.6

Run 7 - Cat I.xls

89


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

7 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 23-Oct-15 10:46

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.20

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

154 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.17

30.14

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.17 "Hg

70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104

9.231 9.362 9.494 9.626 9.756 9.887 10.020 10.153 10.286 10.420 10.552 10.686 10.818 10.952 11.085 11.218 11.351 11.484 11.616 11.748 11.882 12.014 12.147 12.279 12.411 12.542 12.674 12.805 12.937 13.070 13.202 13.337 13.469 13.603 13.735

9.376 9.511 9.645 9.779 9.914 10.048 10.182 10.317 10.451 10.586 10.720 10.854 10.989 11.123 11.258 11.392 11.526 11.661 11.796 11.929 12.064 12.199 12.333 12.467 12.601 12.736 12.870 13.004 13.139 13.273 13.407 13.542 13.676 13.811 13.946

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13

0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.14 0.13 0.14 0.14 0.13 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.14 0.14

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.57 1.57 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.57 1.57 1.56 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.56 1.58 1.56 1.58 1.58 1.58 1.57 1.58 1.56 1.58 1.58 1.58 1.58 1.57 1.58

80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 80 81 80 80 80 80 80 80

13.44 148.2 152.1

ft/sec. scfm scfm 0 cfm @ -5 0 cfm @ -4 22.37 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.034

0.058

0.048

0.027

0.024

0.054

0.053

0.022

0.054

89

89

89

89

89

89

89

89

89

Vstrav

13.51

ft/sec

Vscent

15.64

ft/sec

Fp

0.864

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.417 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.36 0.37 0.37 0.36 0.36 0.37 0.37 0.36 0.37 0.36 0.36 0.36 0.36 0.37 0.36 0.37 0.36 0.37 0.37 0.36 0.37 0.37 0.37 0.36 0.35 0.37 0.37 0.36 0.37 0.37 0.37 0.37 0.37 0.36 0.36

1.32 1.32 1.33 1.32 1.32 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.33 1.32 1.33 1.33 1.32 1.33 1.33 1.32 1.32 1.33 1.32 1.32 1.33 1.33 1.33 1.33 1.33

78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

81 81 81 81 81 81 80 80 80 80 80 80 80 80 80 79 79 79 79 79 79 79 79 79 79 79 78 79 78 79 78 79 78 78 78

0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054

100 99 99 99 98 99 100 100 100 101 99 101 99 101 100 100 100 100 99 99 101 99 100 99 99 98 99 98 99 100 99 101 99 101 99

99 100 99 99 100 99 99 100 99 100 99 99 100 99 100 99 99 100 100 98 100 100 99 99 99 100 99 99 100 99 99 100 99 100 100

Page 3 of 5

Scale Weight Reading Change 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.8 0.8 0.8 0.8 0.8 0.8 0.7 0.8 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0.7 0.6 0.6 0.6 0.6 0.6 0.5

0 0 0 0 0 0 0 0 -0.1 0 0 0 0 0 -0.1 0.1 -0.1 0 0 0 0 0 0 0 0 0 0 -0.1 0.1 -0.1 0 0 0 0 -0.1

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

354.8 352.4 350.5 348.3 346.6 344.8 342.9 341.0 339.0 337.7 335.7 334.3 333.2 331.3 330.1 328.7 327.2 325.8 324.5 323.7 322.3 320.7 319.6 318.6 317.1 315.9 314.7 314.0 313.0 311.8 310.8 309.8 308.9 307.9 307.1

238 236 235 234 231 229 228 226 223 224 222 220 219 217 217 216 215 214 215 212 212 212 211 210 209 208 207 207 207 205 204 203 202 201 201

71 71 70 70 70 70 70 70 70 70 70 70 70 70 70 70 70 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69

65 65 65 65 65 65 65 65 65 65 65 65 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 65 65 65 66 66 66

69 69 69 69 69 69 69 69 69 69 69 69 70 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69

-0.069 -0.069 -0.068 -0.068 -0.068 -0.067 -0.067 -0.067 -0.066 -0.066 -0.066 -0.065 -0.065 -0.065 -0.065 -0.064 -0.064 -0.064 -0.064 -0.063 -0.064 -0.063 -0.063 -0.063 -0.062 -0.062 -0.062 -0.062 -0.061 -0.062 -0.061 -0.061 -0.061 -0.061 -0.061

5.2 5.2 5.2 5.1 5.1 5.1 5.2 5.2 5.2 5.1 5.1 5 5 5 5 5 4.9 4.9 5 5 4.9 4.9 4.8 4.8 4.8 4.9 4.8 4.9 4.9 4.8 4.8 4.8 4.8 4.8 4.7

0.6 0.6 0.6 0.7 0.7 0.6 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.7 0.8 0.8 0.9 0.8 0.8 0.8 0.8 0.8 0.8 0.7 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.9 0.8 0.9

Run 7 - Cat I.xls

90


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

7 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 23-Oct-15 10:46

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.20

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

154 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.17

30.14

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.17 "Hg

105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126 127 128 129 130 131 132 133 134 135 136 137 138 139

13.869 14.002 14.136 14.268 14.401 14.534 14.666 14.800 14.933 15.066 15.198 15.330 15.461 15.593 15.724 15.855 15.988 16.120 16.255 16.387 16.523 16.656 16.789 16.923 17.055 17.188 17.321 17.455 17.587 17.720 17.853 17.986 18.119 18.251 18.382

14.080 14.214 14.349 14.483 14.618 14.752 14.886 15.021 15.155 15.289 15.424 15.558 15.693 15.827 15.961 16.096 16.230 16.365 16.499 16.633 16.770 16.905 17.039 17.173 17.308 17.442 17.577 17.711 17.845 17.980 18.114 18.249 18.383 18.517 18.652

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.14 0.14 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.14 0.13 0.13 0.13 0.13 0.14

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.58 1.58 1.57 1.58 1.58 1.58 1.58 1.57 1.57 1.58 1.58 1.58 1.58 1.58 1.58 1.58 1.57 1.58 1.56 1.58 1.57 1.58 1.58 1.58 1.58 1.57 1.57 1.56 1.58 1.58 1.58 1.57 1.58 1.56 1.58

80 80 80 80 80 80 81 80 80 80 81 81 81 81 81 81 80 80 80 81 81 81 81 80 80 81 81 81 81 81 81 81 81 81 81

13.44 148.2 152.1

ft/sec. scfm scfm 0 cfm @ -5 0 cfm @ -4 22.37 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.034

0.058

0.048

0.027

0.024

0.054

0.053

0.022

0.054

89

89

89

89

89

89

89

89

89

Vstrav

13.51

ft/sec

Vscent

15.64

ft/sec

Fp

0.864

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.417 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.36 0.36 0.37 0.36 0.37 0.37 0.37 0.36 0.36 0.36 0.37 0.37 0.36 0.36 0.37 0.36 0.36 0.37 0.37 0.37 0.36 0.37 0.36 0.36 0.37 0.36 0.37 0.36 0.37 0.35 0.36 0.36 0.37 0.37 0.36

1.33 1.33 1.32 1.32 1.33 1.32 1.32 1.33 1.34 1.32 1.32 1.33 1.33 1.32 1.33 1.32 1.33 1.33 1.32 1.33 1.33 1.33 1.32 1.33 1.33 1.32 1.32 1.33 1.33 1.32 1.33 1.32 1.33 1.33 1.33

78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 79 78 78 78 78 78 78 78 78

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 77

0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054

101 100 101 99 100 100 99 101 100 100 99 99 98 99 98 98 100 99 101 99 102 100 100 100 99 100 100 100 99 100 100 100 100 99 98

99 99 100 99 100 99 99 100 99 99 100 99 100 99 99 100 99 100 99 99 101 100 99 99 100 99 100 99 99 100 99 100 99 99 100

Page 4 of 5

Scale Weight Reading Change 0.6 0.6 0.5 0.6 0.5 0.5 0.5 0.5 0.5 0.4 0.5 0.4 0.4 0.5 0.4 0.4 0.4 0.4 0.4 0.4 0.3 0.4 0.3 0.4 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.3

0.1 0 -0.1 0.1 -0.1 0 0 0 0 -0.1 0.1 -0.1 0 0.1 -0.1 0 0 0 0 0 -0.1 0.1 -0.1 0.1 -0.1 0 0 0 0 0 0 0 -0.1 0.1 0

Temperature Data (°F)

"H2O °F

Stack Gas Data

Avg. Stove Surface Temp

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

305.6 305.1 304.3 303.5 302.6 301.5 300.5 299.5 298.8 298.3 297.4 296.6 295.8 295.0 294.1 293.1 292.9 292.1 291.4 290.9 290.2 289.7 289.3 288.7 288.1 287.7 287.2 286.1 286.0 284.9 284.3 284.1 283.3 282.7 281.8

200 199 198 198 197 197 196 195 194 193 193 193 192 190 191 191 192 190 190 189 190 190 188 187 187 187 187 186 186 185 186 183 183 182 183

69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69

66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 66 67 67 67 66 66 66 66 67 67 66

69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 68

-0.060 -0.061 -0.060 -0.060 -0.060 -0.060 -0.060 -0.059 -0.060 -0.059 -0.059 -0.059 -0.059 -0.059 -0.059 -0.059 -0.059 -0.059 -0.058 -0.058 -0.058 -0.058 -0.059 -0.058 -0.058 -0.058 -0.058 -0.058 -0.058 -0.058 -0.058 -0.057 -0.057 -0.057 -0.057

4.7 4.5 4.5 4.5 4.5 4.4 4.5 4.6 4.7 4.7 4.7 4.7 4.7 4.6 4.7 4.7 4.6 4.6 4.8 4.8 4.7 4.6 4.5 4.3 4.2 4.1 4 4 4 4 3.9 3.9 3.9 3.8 3.7

0.8 0.9 0.9 0.9 0.9 0.9 0.9 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.8 0.9 0.9 0.9 1 1 1 1 1.1 1.1 1.1 1.1 1.1 1.1 1.2 1.2

Run 7 - Cat I.xls

91


OMNI-Test Laboratories, Inc.

Wood Heater Test Data - ASTM E2780 / ASTM E2515 Run:

7 Manufacturer: Model: Tracking No.: Project No.: Test Date: Beginning Clock Time:

RAIS Q-Tee II 2138 0138WS016E 23-Oct-15 10:46

Meter Box Y Factor:

1.011

Barometric Pressure:

Begin 30.20

OMNI Equipment Numbers:

Total Sampling Time: Recording Interval:

154 1

Background Sample Volume:

(1)

1.003

(2)

Middle

End

Average

30.17

30.14

0

0

PM Control Modules: Dilution Tunnel MW(dry): Dilution Tunnel MW(wet): Dilution Tunnel H2O: Dilution Tunnel Static: Tunnel Area: Pitot Tube Cp:

min min cubic feet

(Amb)

Gas Meter 1 (ft3)

Gas Sample Meter 2 Rate 1 (cfm) (ft3)

30.17 "Hg

140 141 142 143 144 145 146 147 148 149 150 151 152 153 154 Avg/Tot

18.513 18.645 18.776 18.908 19.041 19.175 19.308 19.441 19.574 19.707 19.840 19.972 20.106 20.238 20.372 20.372

18.786 18.921 19.055 19.189 19.324 19.459 19.593 19.728 19.862 19.997 20.131 20.265 20.400 20.535 20.669 20.669

Control No. P-SSAR-0001

0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13 0.13

0.13 0.13 0.13 0.13 0.14 0.13 0.13 0.14 0.13 0.14 0.13 0.13 0.13 0.14 0.13 0.13

Orifice Meter 1 dH 1 Temp ("H2O) (°F) 1.58 1.56 1.58 1.58 1.58 1.58 1.58 1.57 1.58 1.58 1.58 1.58 1.57 1.57 1.57 1.57

81 81 81 81 81 81 80 80 80 80 80 80 80 80 80 78

13.44 148.2 152.1

ft/sec. scfm scfm 0 cfm @ -5 0 cfm @ -4 22.37 Dry Basis %

in. Hg in. Hg

Velocity Traverse Data Pt.2

Pt.3

Pt.4

Pt.5

Pt.6

Pt.7

Pt.8

Center

Initial dP 0.034

0.058

0.048

0.027

0.024

0.054

0.053

0.022

0.054

89

89

89

89

89

89

89

89

89

Vstrav

13.51

ft/sec

Vscent

15.64

ft/sec

Fp

0.864

Temp:

23, 131, 132, 209, 283A, 291, 296-T54, 371, 372, 340, 410, 419, 431, 559

Sample Rate 2 (cfm)

lb/lb-mole Avg. Tunnel Velocity: lb/lb-mole Intial Tunnel Flow: percent Average Tunnel Flow: "H2O Post-Test Leak Check (1): ft2 Post-Test Leak Check (2): Average Test Piece Fuel Moisture:

Pt.1

Fuel Weight (lb)

Particulate Sampling Data Elapsed Time (min)

371/372 29.00 28.78 2.00 -0.417 0.19635 0.99

Meter 1 Vacuum ("Hg)

Orifice dH 2 ("H2O)

Meter 2 Temp (°F)

Meter 2 Vacuum ("Hg)

Dilution Tunnel (°F)

Dilution Tunnel Center dP

Pro. Rate 1

Pro. Rate 2

0.36 0.36 0.36 0.37 0.37 0.36 0.37 0.37 0.36 0.37 0.37 0.36 0.36 0.36 0.37

1.32 1.33 1.33 1.33 1.34 1.33 1.33 1.34 1.33 1.33 1.32 1.33 1.33 1.32 1.33 1.32

78 78 78 78 78 78 78 78 78 78 78 78 78 78 78 76

0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.6

77 77 77 77 77 77 77 77 77 77 77 77 77 77 77 83

0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054 0.054

98 99 98 99 100 100 100 100 100 100 100 99 100 99 100 100

99 100 99 99 100 100 99 100 99 100 99 99 100 100 99 100

Page 5 of 5

Scale Weight Reading Change 0.2 0.3 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.1 0.2 0.1 0.2 0.2 0.0

-0.1 0.1 -0.1 0 0 0 0 0 0 -0.1 0.1 -0.1 0.1 0 -0.2

Temperature Data (°F) Avg. Stove Surface Temp 281.2 280.8 280.0 278.9 278.4 277.3 276.8 275.7 275.1 274.1 273.7 273.1 271.6 271.2 270.1 81.0

"H2O °F

Stack Gas Data

Stack

Filter 1

Filter 2

Ambient

Draft ("H2O)

CO2 (%)

CO (%)

182 182 182 181 181 180 179 179 178 177 176 175 174 174 174

69 69 69 69 69 69 69 69 69 69 69 69 69 69 69 70

66 66 66 66 65 65 65 65 66 66 66 66 66 66 66 65

69 69 68 68 68 68 68 68 69 69 69 69 69 69 69 69

-0.057 -0.057 -0.057 -0.056 -0.057 -0.056 -0.056 -0.056 -0.056 -0.056 -0.056 -0.056 -0.055 -0.055 -0.056 -0.071

3.8 3.7 3.6 3.5 3.6 3.5 3.3 3.1 3.1 3.1 3.1 3.1 3.1 3.2 3.2

1.2 1.2 1.2 1.3 1.2 1.3 1.3 1.4 1.4 1.4 1.4 1.4 1.3 1.3 1.3

Run 7 - Cat I.xls

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Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Section 4 Quality Assurance/Quality Control

OMNI-Test Laboratories, Inc.

96


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

QUALITY ASSURANCE/QUALITY CONTROL OMNI follows the guidelines of ISO/IEC 17025, “General Requirements for the Competence of Testing and Calibration Laboratories,” and the quality assurance/quality control (QA/QC) procedures found in OMNI’s Quality Assurance Manual. OMNI’s scope of accreditation includes, but is not limited to, the following:    

ANSI (American National Standards Institute) for certification of product to safety standards. To perform product safety testing by the International Accreditation Service, Inc. (formerly ICBO ES) under accreditation as a testing laboratory designated TL-130. To perform product safety testing as a “Certification Organization” by the Standards Council of Canada (SCC). Serving as a testing laboratory for the certification of wood heaters by the U.S. Environmental Protection Agency.

This report is issued within the scope of OMNI’s accreditation. Accreditation certificates are available upon request. The manufacturing facilities and quality control system for the production of the Q-Tee II at RAIS A/S were evaluated to determine if sufficient to maintain conformance with OMNI’s requirements for product certification. OMNI has concluded that the manufacturing facilities, processes, and quality control system are adequate to produce the appliance congruous with the standards and model codes to which it was evaluated. This report shall not be reproduced, except in full, without the written approval of OMNI-Test Laboratories, Inc.

OMNI-Test Laboratories, Inc.

97


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Sample Analysis

Analysis Worksheets Tared Filter, Probe, and O-Ring Data

OMNI-Test Laboratories, Inc.

98


OMNI-Test Laboratories, Inc.

Wood Heater Lab Data - ASTM E2780 / ASTM E2515

Manufacturer: Model: Tracking No.: Project No.: Run #: Date:

RAIS Q-Tee II 2138 0138WS016E 2 10/20/15

TRAIN 1 (First Hour emissions) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Equipment Numbers:

Reagent Filter Filter Probe Seals

Filter, Probe or Dish # C204

Sub-Total TRAIN 1 (Post First Hour Change-out) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Train 1 Aggregate

A. B. C. D.

Sample Component

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Final, mg 121.8

Weights Tare, mg Particulate, mg 121.1 0.7 0.0 0.0 0.0

Total Particulate, mg:

Filter, Probe or Dish # Final, mg C205 121.7 C206 121.4 18 114409.0 R342 3415.4 Sub-Total

TRAIN 2

23, 131, 291

Weights Tare, mg Particulate, mg 121.6 0.1 121.5 -0.1 114408.8 0.2 3414.6 0.8

Total Particulate, mg:

1.0

Total Particulate, mg:

1.7

Filter, Probe or Dish # Final, mg C207 121.2 C208 121.0 24 114135.9 R346 4312.6

Weights Tare, mg Particulate, mg 120.8 0.4 121.1 -0.1 114135.8 0.1 4311.4 1.2

Total Particulate, mg: AMBIENT

Sample Component

A. Front filter catch*

Reagent Filter

Filter # or Probe # N/A

0.7

Final, mg

1.6

Weights Tare, mg Particulate, mg 0.0

Total Particulate, mg:

0.0

*Particulate catch that results in a negative number, is assumed to be zero for probes and seals, negative numbers for filters are assumed to be part of the seal weight.

Component A. Front filter catch B. Rear filter catch C. Probe catch

Control No. P-XXXX-XXXX

Equations: Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg

99 Run 2 - Cat III.xls


100


OMNI-Test Laboratories, Inc.

Wood Heater Lab Data - ASTM E2780 / ASTM E2515

Manufacturer: Model: Tracking No.: Project No.: Run #: Date:

RAIS Q-Tee II 2138 0138WS016E 3 10/21/15

TRAIN 1 (First Hour emissions) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Equipment Numbers:

Reagent Filter Filter Probe Seals

Filter, Probe or Dish # Final, mg C209 121.8

Sub-Total TRAIN 1 (Post First Hour Change-out) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Train 1 Aggregate

A. B. C. D.

Sample Component

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Weights Tare, mg Particulate, mg 121.3 0.5 0.0 0.0 0.0

Total Particulate, mg:

Filter, Probe or Dish # Final, mg C210 120.9 C211 120.6 28 114766.8 R347 3425.4 Sub-Total

TRAIN 2

23, 131, 291

Weights Tare, mg Particulate, mg 120.5 0.4 120.8 -0.2 114766.7 0.1 3425.5 0.0

Total Particulate, mg:

0.3

Total Particulate, mg:

0.8

Filter, Probe or Dish # Final, mg C212 121.7 C213 120.9 31 114376.7 R350 3377.1

Weights Tare, mg Particulate, mg 120.9 0.8 120.8 0.1 114376.5 0.2 3377.3 0.0

Total Particulate, mg: AMBIENT

Sample Component

A. Front filter catch*

Reagent Filter

Filter # or Probe # N/A

0.5

Final, mg

1.1

Weights Tare, mg Particulate, mg 0.0

Total Particulate, mg:

0.0

*Particulate catch that results in a negative number, is assumed to be zero for probes and seals, negative numbers for filters are assumed to be part of the seal weight.

Component A. Front filter catch B. Rear filter catch C. Probe catch

Control No. P-XXXX-XXXX

Equations: Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg

101 Run 3 - Cat II.xls


102


OMNI-Test Laboratories, Inc.

Wood Heater Lab Data - ASTM E2780 / ASTM E2515

Manufacturer: Model: Tracking No.: Project No.: Run #: Date:

RAIS Q-Tee II 2138 0138WS016E 4 10/21/15

TRAIN 1 (First Hour emissions) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Equipment Numbers:

Reagent Filter Filter Probe Seals

Filter, Probe or Dish # Final, mg C214 120.5 C216 120.2 32 114747.7 R357 3614.0 Sub-Total

TRAIN 1 (Post First Hour Change-out) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Train 1 Aggregate

A. B. C. D.

Sample Component

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Weights Tare, mg Particulate, mg 120.7 -0.2 120.7 -0.5 114747.7 0.0 3612.8 1.2

Total Particulate, mg:

Filter, Probe or Dish # Final, mg

Sub-Total

TRAIN 2

23, 131, 291

Weights Tare, mg Particulate, mg 0.0 0.0 0.0 0.0

Total Particulate, mg:

0.0

Total Particulate, mg:

0.5

Filter, Probe or Dish # Final, mg C217 120.3 C218 120.2 53 122931.1 R358 3298.2

Weights Tare, mg Particulate, mg 119.9 0.4 120.8 -0.6 122930.9 0.2 3297.6 0.6

Total Particulate, mg: AMBIENT

Sample Component

A. Front filter catch*

Reagent Filter

Filter # or Probe # N/A

0.5

Final, mg

0.6

Weights Tare, mg Particulate, mg 0.0

Total Particulate, mg:

0.0

*Particulate catch that results in a negative number, is assumed to be zero for probes and seals, negative numbers for filters are assumed to be part of the seal weight.

Component A. Front filter catch B. Rear filter catch C. Probe catch

Control No. P-XXXX-XXXX

Equations: Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg

103 Run 4 - Cat IV.xls


104


OMNI-Test Laboratories, Inc.

Wood Heater Lab Data - ASTM E2780 / ASTM E2515

Manufacturer: Model: Tracking No.: Project No.: Run #: Date:

RAIS Q-Tee II 2138 0138WS016E 6 10/22/15

TRAIN 1 (First Hour emissions) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Equipment Numbers:

Reagent Filter Filter Probe Seals

Filter, Probe or Dish # Final, mg C228 122.0

Sub-Total TRAIN 1 (Post First Hour Change-out) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Train 1 Aggregate

A. B. C. D.

Sample Component

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Weights Tare, mg Particulate, mg 120.4 1.6 0.0 0.0 0.0

Total Particulate, mg:

Filter, Probe or Dish # Final, mg C229 121.1 C230 121.8 56 123075.5 R379 3391.1 Sub-Total

TRAIN 2

23, 131, 291

Weights Tare, mg Particulate, mg 120.8 0.3 121.5 0.3 123075.2 0.3 3390.5 0.6

Total Particulate, mg:

1.5

Total Particulate, mg:

3.1

Filter, Probe or Dish # Final, mg C231 123.1 C232 120.2 62 123018.3 R380 4175.4

Weights Tare, mg Particulate, mg 121.8 1.3 120.1 0.1 123018.0 0.3 4172.4 3.0

Total Particulate, mg: AMBIENT

Sample Component

A. Front filter catch*

Reagent Filter

Filter # or Probe # N/A

1.6

Final, mg

4.7

Weights Tare, mg Particulate, mg 0.0

Total Particulate, mg:

0.0

*Particulate catch that results in a negative number, is assumed to be zero for probes and seals, negative numbers for filters are assumed to be part of the seal weight.

Component A. Front filter catch B. Rear filter catch C. Probe catch

Control No. P-XXXX-XXXX

Equations: Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg

105 Run 6 - Cat III.xls


106


OMNI-Test Laboratories, Inc.

Wood Heater Lab Data - ASTM E2780 / ASTM E2515

Manufacturer: Model: Tracking No.: Project No.: Run #: Date:

RAIS Q-Tee II 2138 0138WS016E 7 10/23/15

TRAIN 1 (First Hour emissions) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Equipment Numbers:

Reagent Filter Filter Probe Seals

Filter, Probe or Dish # Final, mg C263 119.8

Sub-Total TRAIN 1 (Post First Hour Change-out) Sample Component B. C. D. E.

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Train 1 Aggregate

A. B. C. D.

Sample Component

Front filter catch Rear filter catch Probe catch* Filter seals catch*

Reagent Filter Filter Probe Seals

Weights Tare, mg Particulate, mg 119.3 0.5 0.0 0.0 0.0

Total Particulate, mg:

Filter, Probe or Dish # Final, mg C264 119.6 C265 120.5 65 122186.7 R381 3379.2 Sub-Total

TRAIN 2

23, 131, 291

Weights Tare, mg Particulate, mg 119.4 0.2 120.2 0.3 122186.7 0.0 3377.7 1.5

Total Particulate, mg:

2.0

Total Particulate, mg:

2.5

Filter, Probe or Dish # Final, mg C266 120.0 C267 120.3 66 123174.0 R382 4320.7

Weights Tare, mg Particulate, mg 119.6 0.4 120.1 0.2 123173.9 0.1 4319.8 0.9

Total Particulate, mg: AMBIENT

Sample Component

A. Front filter catch*

Reagent Filter

Filter # or Probe # N/A

0.5

Final, mg

1.6

Weights Tare, mg Particulate, mg 0.0

Total Particulate, mg:

0.0

*Particulate catch that results in a negative number, is assumed to be zero for probes and seals, negative numbers for filters are assumed to be part of the seal weight.

Component A. Front filter catch B. Rear filter catch C. Probe catch

Control No. P-XXXX-XXXX

Equations: Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg Final (mg) - Tare (mg) = Particulate, mg

107 Run 7 - Cat I.xls


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Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Calibrations Methods EPA 28R, ASTM E2515, ASTM E2780 ID #

Lab Name/Purpose

Log Name

Attachment Type

23

Scale-Analytical Balance

Mettler Analytical Balance

Calibration Certificate

131

500 mg Weight

Ohaus Weight Standard, 500 mg

Calibration Certificate

132

10 lb Weight

Weight Standard, 10 lb.

Calibration Certificate

209

Barometer

Barometer â&#x20AC;&#x201C; Princo

Manual Cover

283A

Weight Set

Ohaus Weight Standard Set

Calibration Certificate

288

Scale â&#x20AC;&#x201C; 1000lb

Weight-Tronix Digital Weight Meter

Calibration Certificate

291

Thermohygrometer

Omega Digital Thermohygrometer

Calibration Certificate

296-T54

Tape Measure

Stanley Tape Measure

Calibration Log

340

Wood Moisture Meter

Moisture Meter - Delmhorst

See Test Run Notes

Sample Box / Dry Gas Meter Sample Box / Dry Gas Meter

Apex Automated Emissions Sampling Box Apex Automated Emissions Sampling Box

410

Microtector

Dwyer Microtector

Manual, Photograph

419

Combustion Gas Analyzer

Infrared Gas Analyzer

Manual, See Test Run Notes

431

Moisture Meter Calibrator

Delmhorst Moisture Content Calibrator

Calibration Log

559

Vaneometer

Dwyer Vaneometer

Manual

371 372

OMNI-Test Laboratories, Inc.

Calibration Log Calibration Log

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118


119


120


121


122


123


124


125


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127


128


129


130


131


132


133


134


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Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Example Calculations

OMNI-Test Laboratories, Inc.

145


OMNI-Test Laboratories, Inc. Equations and Sample Calculations – ASTM E2779 & E2515 Manufacturer: Model: Run: Category:

RAIS Q-Tee II 3 II

Equations used to calculate the parameters listed below are described in this appendix. Sample calculations are provided for each equation. The raw data and printout results from a sample run are also provided for comparison to the sample calculations.

MSdb – Weight of test fuel spacers, dry basis, kg MCdb– Weight of test fuel crib, excluding nails and spacers, dry basis, kg DCdb - Density of fuel crib, excluding spacers and nails, dry basis, lbs/ft3 MFTAdb - Total weight of fuel crib excluding nails, dry basis, kg BR – Dry burn rate, kg/hr Vs – Average gas velocity in the dilution tunnel, ft/sec Qsd – Average gas flow rate in dilution tunnel, dscf/hr Vm(std) – Volume of gas sampled, corrected to dry standard conditions, dscf mn – Total particulate matter collected, mg Cs - Concentration of particulate matter in tunnel gas, dry basis, corrected to standard conditions, g/dscf ET – Total particulate emissions, g PR - Proportional rate variation PMR – Particulate emissions for test run, g/hr PMF – Particulate emission factor for test run, g/dry kg of fuel burned

Control No. P-XXXX-XXXX

Run 3 - Cat146 II.xls


OMNI-Test Laboratories, Inc. MSdb â&#x20AC;&#x201C; Weight of test fuel spacers, dry basis, kg ASTM E2780 equation (1) MSdb = (MSwb )(100/(100 + FMS))

Where, FMS

=

average fuel moisture of test fuel spacers, % dry basis

MSwb

=

weight of test fuel spacers, wet basis, kg

Sample Calculation: FMS = 16.5 % MSwb = 1.2 lbs 0.4536 = Conversion factor from lbs to kg

MSdb MSdb =

= [( 1.2 x 0.4536) (100/(100 + 16.5 ) 0.5 kg

Control No. P-XXXX-XXXX

Run 3 - Cat147 II.xls


OMNI-Test Laboratories, Inc. MCdb– Weight of test fuel crib, excluding nails and spacers, dry basis, kg ASTM E2780 equation (2) MCdb = Σ[(MCPnwb)(100/(100 + FMCPn))]

Where, MCPnwb

=

weight of each test fuel piece n in fuel crib, excluding nails and spacers, wet basis, kg

FMCPn

=

Average fuel moisture of test fuel n in fuel crib, % dry basis

Sample Calculation (test fuel piece 1): MCPnwb =

1.4

FMCPn = 22.7 = 1.4 (100/(100+ 22.7 ) = 1.1 lbs Total crib weight, excluding spacers =4.24 lbs MCdb =

Control No. P-XXXX-XXXX

1.92 kg

Run 3 - Cat148 II.xls


OMNI-Test Laboratories, Inc. DCdb - Density of fuel crib, excluding spacers and nails, dry basis, lbs/ft3 ASTM E2780 equation (3) DCdb = MCdb/VC Where,

VC

3 = Volume of fuel crib, ft

Sample calculation: VC

=

228

in3

3 3 1728 = conversion from in to ft

DCdb

= 4.24 / 228 * 1728 =

32.1

lbs/ft3

Control No. P-XXXX-XXXX

Run 3 - Cat149 II.xls


OMNI-Test Laboratories, Inc. MFTAdb - Total weight of fuel crib excluding nails, dry basis, kg ASTM E2780 equation (4) MFTAdb = MSdb + MCdb Sample calculation: MFTAdb = 0.47 + 1.92 = 2.39 kg

Control No. P-XXXX-XXXX

Run 3 - Cat150 II.xls


OMNI-Test Laboratories, Inc. BR – dry burn rate, kg/hr ASTM E2780 equation (5) BR

=

60 MFTAdb θ

Where, θ

= Total length of test run, min

Sample Calculation: MBdb = 2.39 θ

kg

= 134

min

60 x 2.39 BR

=

BR

=

134 1.07

kg/hr

*The

the av

was v

the we

Control No. P-XXXX-XXXX

Run 3 - Cat151 II.xls


OMNI-Test Laboratories, Inc. Vs – Average gas velocity in the dilution tunnel, ft/sec ASTM E2515 equations (9)

vs  FP  kp  Cp  ( P )avg 

Ts(avg) Ps  Ms

Where: Vstrav

, ASTM E2515 Equation (1)

Fp

=

Adjustment factor for center of tunnel pitot tube placement, Fp =

vscent

=

Dilution tunnel velocity calculated after the multi-point pitot traverse at the center, ft/sec

vstrav

=

Dilution tunnel velocity calculated after the multi-point pitot traverse, ft/sec

kp

=

Pitot tube constant, 85.49

Cp

=

Pitot tube coefficient: 0.99, unitless

ΔP*

=

Velocity pressure in the dilution tunnel, in H2O

Ts

=

Absolute average gas temperature in the dilution tunnel, °R; (°R = °F + 460)

Ps

=

Absolute average gas static pressure in diltuion tunnel, = P bar + Pg , in Hg

Pbar

=

Barometric pressure at test site, in. Hg

Pg

=

Static pressure of tunnel, in. H20; (in Hg = in H20/13.6)

Ms

=

**The dilution tunnel wet molecular weight; Ms = 28.78 assuming a dry weight of 29 lb/lb-mole

Vscent

Sample calculation:

Fp =

14.07 15.80

Vs = 0.891

=

0.891

x 85.49 x

0.99

x

0.239 x

(

(

84.9

+

30.20

+

460 -0.44 13.6

)x

28.78

)

1/2

Vs = 14.30 ft/s

*The ASTM test standard mistakenly has the square root of the average delta p instead of the average of the square root of delta p. The current EPA Method 2 is also incorrect. This was verified by Mike Toney at EPA. **The ASTM test standard mistakenly identifies Ms as the dry molecular weight. It should be the wet molecular weight as indicated in EPA Method 2.

Control No. P-XXXX-XXXX

Run 3 - Cat152 II.xls


OMNI-Test Laboratories, Inc. Qsd – Average gas flow rate in dilution tunnel, dscf/hr ASTM E2515 equation (3)

Qsd  3600  (1  Bws )  v s  A 

Tstd P  s Ts ( avg ) Pstd

Where: 3600

=

Conversion from seconds to hours (ASTM method uses 60 to convert in minutes)

Bws

=

Water vapor in gas stream, proportion by volume; assume 2%

A

=

Cross sectional area of dilution tunnel, ft2

Tstd

=

Standard absolute temperature, 528 °R

Ps

=

Absolute average gas static pressure in diltuion tunnel, = Pbar + Pg , in Hg

Ts(avg)

=

Absolute average gas temperature in the dilution tunnel, °R; (°R = °F + 460)

Pstd

=

Standard absolute pressure, 29.92 in Hg

Sample calculation: Qsd = 3600 x (1 - 0.02) x

14.30 x

0.196

x

528 84.9 + 460

30.2 + x

-0.44 13.6

29.92

Qsd = 9676.7 dscf/hr

Control No. P-XXXX-XXXX

Run 3 - Cat153 II.xls


OMNI-Test Laboratories, Inc. Vm(std) – Volume of Gas Sampled Corrected to Dry Standard Conditions, dscf ASTM E2515 equation (6)

Where: K1

=

17.64 °R/in. Hg

Vm

=

Volume of gas sample measured at the dry gas meter, dcf

Y

=

Dry gas meter calibration factor, dimensionless

Pbar

=

Barometric pressure at the testing site, in. Hg

∆H

=

Average pressure differential across the orifice meter, in. H2O

Tm

=

Absolute average dry gas meter temperature, °R

Sample Calculation: Using equation for Train 1: Vm(std) =

17.64

x 15.492 x

1.011

x

( (

30.2 + 79.2 +

1.22 13.6 460

)

)

Vm(std) = 15.520 dscf Using equation for Train 2: Vm(std) =

17.64

x 17.869 x

1.003

x

( (

30.2 + 76.8 +

1.31 13.6 460

)

)

Vm(std) = 17.845 dscf Using equation for ambient train: Vm(std) =

17.64

x

0.00

x

1

x

( (

Vm(std) =

0

30.2 + 70.5 +

0.00 13.6 460

)

)

dscf

Control No. P-XXXX-XXXX

Run 3 - Cat154 II.xls


OMNI-Test Laboratories, Inc. mn – Total Particulate Matter Collected, mg ASTM E2515 Equation (12)

 m

p

mp

=

mass of particulate matter from probe, mg

mf

=

mass of particulate matter from filters, mg

mg

=

mass of particulate matter from filter seals, mg

m

n

 mf  mg

Where:

Sample Calculation: Using equation for Train 1 (first hour): mn =

0.0

+

mn =

0.5

mg

0.5

+

0.0

Using equation for Train 1 (post-first hour): mn =

0.0

+

mn =

0.2

mg

0.2

+

0.0

+

0.2

Train 1 aggregate: mn =

0.5

+

mn =

0.7

mg

0.2

Using equation for Train 2: mn =

0

+

mn =

1.1

mg

0.9

Control No. P-XXXX-XXXX

Run 3 - Cat155 II.xls


OMNI-Test Laboratories, Inc. Cs - Concentration of particulate matter in tunnel gas, dry basis, corrected to standard conditions, g/dscf ASTM E2515 equation (13)

Cs ď&#x20AC;˝ K2 ď&#x201A;´

mn V m ( std

)

Where: K2

=

Constant, 0.001 g/mg

mn

=

Total mass of particulate matter collected in the sampling train, mg

Vm(std)

=

Volume of gas sampled corrected to dry standard conditions, dscf

Sample calculation: For Train 1: Cs =

0.001 x

0.7 15.52

Cs = 0.00005 g/dscf For Train 2 Cs =

0.001 x

1.1 17.85

Cs = 0.00006 g/dscf For Ambient Train Cr =

Cr =

0.001 x

0

0.0 0 g/dscf

Control No. P-XXXX-XXXX

Run 3 - Cat156 II.xls


OMNI-Test Laboratories, Inc. ET – Total Particulate Emissions, g ASTM E2515 equation (15)

E T  c s  c r   Q std   Where: Cs

=

Concentration of particulate matter in tunnel gas, g/dscf

Cr

=

Concentration particulate matter room air, g/dscf

Qstd

=

Average dilution tunnel gas flow rate, dscf/hr

θ

=

Total time of test run, minutes

Sample calculation: For Train 1 ET = ( 0.000045 - 0 ET =

0.97

)x

9676.7

x

)x

9676.7

x

134 /60

g

For Train 2 ET = ( 0.000062 - 0 ET =

1.33

g

1.15

g

134

/60

Average E=

Total emission values shall not differ by more than 7.5% from the total average emissions 7.5% of the average =

0.09

Train 1 difference =

0.18

Train 2 difference =

0.18

Control No. P-XXXX-XXXX

Run 3 - Cat157 II.xls


OMNI-Test Laboratories, Inc. PR - Proportional Rate Variation ASTM E2515 equation (16)

   V mi  V s  T m  T si  PR     100   i  V m  V si  T mi  T s  Where: θ

= Total sampling time, min

θi

= Length of recording interval, min

Vmi

= Volume of gas sample measured by the dry gas meter during the “ith” time interval, dcf

Vm

= Volume of gas sample as measured by dry gas meter, dcf

Vsi

= Average gas velocity in the dilution tunnel during the "ith" time interval, ft/sec

Vs

= Average gas velocity in the dilution tunnel, ft/sec

Tmi

o = Absolute average dry gas meter temperature during the "ith" time interval, R

Tm

o = Absolute average dry gas meter temperature, R

Tsi

o = Absolute average gas temperature in the dilution tunnel during the "ith" time interval, R

Ts

o = Absolute average gas temperature in the dilution tunnel, R

Sample calculation (for the first 1 minute interval of Train 1): PR =

PR =

(

134 x 1

x

0.101

x

14.30

x(

109.0 + 460 ) x ( 79.2 + 460

)

15.49

x

14.31

x(

84.9

)

+ 460 ) x ( 72.0 + 460

)

x 100

92 %

Control No. P-XXXX-XXXX

Run 3 - Cat158 II.xls


OMNI-Test Laboratories, Inc. PMR – Particulate emissions for test run, g/hr ASTM E2780 equation (6) PMR = 60 (ET/θ)

Where, ET = Tota particulate emissions, grams θ = Total length of full intergrated test run, min Sample Calculation: ET (Dual train average) = θ =

1.15 g 134 min

PMR = 60 x ( 1.15 / 134 )

PMR

= 0.52

Control No. P-XXXX-XXXX

g/hr

Run 3 - Cat159 II.xls


OMNI-Test Laboratories, Inc. PMF â&#x20AC;&#x201C; Particulate emission factor for test run, g/dry kg of fuel burned ASTM E2780 equation (7) PMF = ET/MFTAdb

Sample Calculation: ET (Dual train average) = MBdb =

2.39 kg

PMF =

1.15 / 2.39

PMF =

Control No. P-XXXX-XXXX

1.15 g

0.48

g/kg

Run 3 - Cat160 II.xls


Model: Q-Tee II RAIS A/S Industrivej 20, Vangen DK-9900 Frederikshavn Denmark

Section 5 Labeling & Ownerâ&#x20AC;&#x2122;s Manual

OMNI-Test Laboratories, Inc.

161


Manufactured by:

RAIS A/S Industrivej 20, DK-9900 Frederikshavn, Denmark Model: Q-Tee II USA Solid Fuel Room Heater

Report No. #

For Use With Solid Wood Fuel Only Month Mois

Year Année

Clearances to combustible surfaces

**Rear/Top vent option Ceiling

Adjacent wall

FLOOR PROTECTOR 8"

8" C

8"

**

D

Adjacent wall

E

Side wall

B

Back wall

Made in Denmark Fabriqué au Danemark

Serial no. N° de série

16"

Date of manufacture Date of fabrication

Model Modéle

A

Tested to: UL 1482 ULC S627-00

C

Front Floor protection for Canada: 30" (76 cm) from unit to front of floor protector. MINIMUM CLEARANCES

Écartement minimum

A: SIDEWALL TO UNIT 15 B: BACKWALL TO UNIT 15 C: CORNERWALL TO UNIT 13 D: CEILING TO APPLIANCE E: FRONT WALL / FURNISHING:

A: Mur latéral - Appareil B: Mur arriére - Appareil C: Mur de coin - Appareil D: Plafond - Lappareil E: Distance meuble devant

FLOOR PROTECTION: NON COMBUSTIBLE MATERIAL 1" THICK (K-VALUE = 0,84 ((BTU*IN)/(FT2*HR*°F))) ** Not Tested - NFPA Guidelines in USA, CAN/CSA B365-M91 in Canada Floor protection must be non-combustible material extending beneath the stove, and to the front and sides from door opening and to the rear as indicated. The floor protection needed on the floor when used WITHOUT the base is required to have thermal protection with an R value of 3.19 Btu*in/Hrs*ft2*°F (equal to 0.46 w/mk in SI units). with the base, the floor protection is not required to have thermal protection (R=0)

Floor Protector must be under connector pipe and 2" (5 cm) to the side for a thru-the wall configuration. U.S. ENVIRONMENTAL PROTECTION AGENCY Certified to comply  with 2020 particulate emission standards using crib wood.  0.9  g/hr, Method 28R This wood heater needs periodic inspection and repair for proper operation.  Consult the owner's manual for further information. It is against federal  regulations to operate this wood heater in a manner inconsistent with the  operating instructions in the owner's manual.

** Non testé - NFPA Guidelines au USA, CAN/CSA B365-M91 au Canada La protection de sol doit être au moins de 3/8 inch matériel non combustible placé sous le foyer s'étendant vers l'avant, les côtés les ouvertures et l'arriére comme induqué. 162


US English

User Manual Q-Tee II USA

USER MANUAL / M A N U A L D â&#x20AC;&#x2122; U T I L I S AT I O N Q-Tee II USA

163

1


FIRE ENVIRONMENTALLY FRIENDLY!

5 Eco-friendly advices for sensible heating - common sense both environmentally and economically. 1. Effective lighting. Use small pieces of wood (fir tree) and a suitable fire lighter, for example paraffined wood wool/sawdust. Open the air damper, so plenty of air is fed to the stove and the gases from the heated wood can burn rapidly. 2. Light the fire with only little wood at a time - this gives the best combustion. Remember plenty of air for every time new wood is added. 3. When the flames are diminished, adjust the air damper so that the air supply is reduced. 4. When only glowing embers remain, air flow can be reduced further, so heating demand is just covered. With a lower air supply the charcoal will burn slower and the heat loss through the chimney is reduced.

RECYCLING: The oven is wrapped in packaging that is recyclable. This must be disposed of according to national rules regarding the disposal of waste. The glass can not be reused. The glass should be discarded along with the residual waste from ceramics and porcelain. Pyrex glass has a higher melting temperature and therefore can not be reused. If discarded you make an important positive contribution to the environment.

164

We cannot be held responsible for any misprints

5. Use only dry wood - ie. wood with a humidity of 15 to 20%.


US English

User Manual Q-Tee II USA

Q-Tee II USA OMNI report no. : # Revision :1 Date (DMY) : 11-11-2015

INTRODUCTION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4 WARRANTY . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4 SPECIFICATIONS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5 CONVECTION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6 GLASS AND REPLACEMENT OF GLASS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6 CHIMNEY . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7-8 INSTALLATION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 9 NAME TAG . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 10-11 CLEARANCES TO COMBUSTIBLE WALLS . . . . . . . . . . . . . . . . . . . . . . . . . . . 12-13 CLEARANCES TO NON-COMBUSTIBLE WALLS . . . . . . . . . . . . . . . . . . . . . . . . . . 14 FLOOR PROTECTION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14 FIREWOOD . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15 DRYING AND STORING . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15 ADJUSTING THE COMBUSTION AIR . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16 USING THE STOVE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 17 ADJUSTING THE AIR CONTROL . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 17 CONTROL . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 17 FIRST FIRE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 18 LIGHTING AND STOKING . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19-20 FUEL CAUTION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 21 CARE AND MAINTENANCE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 21 CLEANING THE SMOKE/BAFFLE SYSTEM . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 22 DISPOSAL OF ASHES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 23 TROUBLE SHOOTING . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 24 SPARE PART DRAWING . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 26-27

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User Manual Q-Tee II USA

Introduction Congratulations on the purchase of your new RAIS woodburning stove. A RAIS woodburning stove is more than just a source of heat, it is a symbol of the emphasis you put on decorating your home with superiorly designed high-quality products. PLEASE READ THIS ENTIRE MANUAL BEFORE YOU INSTALL AND USE YOUR NEW RAIS STOVE. FAILURE TO FOLLOW INSTRUCTIONS MAY RESULT IN PROPERTY DAMAGE, BODILY INJURY, OR EVEN DEATH.SAVE THIS MANUAL AND KEEP IT HANDY FOR EASY REFERRAL. “DO NOT INSTALL IN A MOBILE HOME” “WARNING: Do not overfire. If the stovetop or chimney connector pipe glow red, you are overfiring”. Safety and environmental testing The Stove have been tested by OMNI-Test Laboratories, Inc. 13327 NE Airport Way, Portland, OR 97230 USA and are listed to UL 1482 and ULC S627. It is also EPA certified.. For future reference, please write down the production number of your RAIS woodburning stove here. The number must be stated in all inquiries or complaints concerning this product.

Warranty

We offer a five-year warranty on your RAIS stove. The warranty covers any defects in materials or workmanship. However, it does not cover damage from misuse or neglect, and the glass, gaskets and firebricks are not covered either.

Distributor: Date:

4

166


US English

User Manual Q-Tee II USA

U.S. ENVIRONMENTAL PROTECTION AGENCY Certified to comply with 2020 particulate emission standards using crib wood. 0.9 g/hr, Method 28R This wood heater needs periodic inspection and repair for proper operation. It is against federal regulations to operate this wood heater in a manner inconsistent with operating instructions in this manual. This wood heater has a manufacturer-set minimum low burn rate that must not be altered. It is against federal regulations to alter this setting or otherwise operate this wood heater in a manner inconsistent with operating instructions in this manual.

Specifications: RAIS Q-Tee II USA Weight of Stove Weight of stove with socket

275 lbs (125 kg) 324 lbs (147 kg)

Stove exterior: Width/depth/height (inches)

22.9 / 16.1 / 23.5

Firebox interior Width/depth/height (inches)

17.5 / 10.9 / 10.4

Heating capacity at -20°C/-4°F

App.

m² /

Square Feet

Recommended amount of wood when fueling (kg) wood: 2-3 logs of wood of app. 25-33cm Intermittent operation: Flue gas mass flow: Flue gas temperature:

Refuelling should be undertaken within 60 minutes. grams per second °C /

°F

Single wall connector stove pipe:

6” (15 cm)

Chimney pipe - class A, UL-103 HT:

6” (15 cm)

Optimal thermal output :

kBTU (

kW)

Min./Max. output (kW):

kBTU (

kW)

Minimum stove draft pressure at above output:

0.048”WC (12 Pa)

Tested EPA emission particulate rate: 167

5


US English

User Manual Q-Tee II USA

Convection All RAIS stoves are convection stoves, which means that the sides of the stove never get too hot. Convection works by pulling cold air into the system at the base of the stove and up through the convection duct that is located along the combustion chamber of the stove. The heated air is released from the top of the stove, creating rapid air circulation in the room.

Glass and replacement of glass. All RAIS stoves supplied with RobaxÂŽ glass in the door. RobaxÂŽ glass is a ceramic glass type suitable for stoves. The glass is installed from RAIS as an integral part of the door and stove. Inspect the glass for cracks prior to the first fire. Abuse may cause damage to the glass and door. Do not strike the door or glass nor slam the door Do not build the fire close to the glass or opening. Do not use the stove if the glass is broken - contact your local authorized dealer. In case of broken glass during use of stove - let the stove slowly burn the remaining firewood under supervision. Do not close the chimney baffle if installed. Contact you local authorized dealer The glass is supplied as an integral part of the door for spare part. The RobaxÂŽ glass may only be replaced by genuine spare parts from RAIS. Do not use substitute material. Replacement of the glass as separate component is only for authorized personnel.

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User Manual Q-Tee II USA

Chimney RAIS stoves must be installed using a Class A UL 103 HT approved factory-built chimney system or a code-approved masonry chimney with a flue liner. In Canada, the installation must conform to CAN/CSA-B365. The chimney must extend through the roof at least 3’ (1m), and 2’ (.6m) above any structure within 10’ (3m). The condition and height of the chimney are very important for optimal use of the stove and we recommend a total minimum height of 10’ (3m). Note the chimney connector pipe should not pass through an attic, roof space, closet, concealed space, floor or ceiling. Do not connect this stove to a chimney flue or air distribution duct or any system serving another appliance.

Each chimney connector or stove pipe section, must be installed to each other with the crimped end toward the stove. This prevents any amount of condensed or liquid creosote from running down the outside of the pipe or the stove top.

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US English

User Manual Q-Tee II USA

Required Installation Components:

A. B. C. D.

B. E.

F.

A. Chimney Cap B. Insulated Chimney C. Storm Collar D. Roof Flashing E. Ceiling Support Box or Joist Shield/Firestop Spacer F. Chimney Connector For venting vertically into a Class A chimney, a single wall pipe (at least 24 gauge) may be used in the room where the stove is installed. Refer to the manufacturer’s instructions for the connection to the listed chimney. The chimney/stove pipe must not be smaller than 6” (15cm) in diameter. For venting directly into a masonry chimney or through a thimble, the top of the single wall pipe must be at least 18” (46cm) below a combustible ceiling and must conform to NFPA 211 guidelines and methods. Please see the diagram to the left.

Chimney Flue

Connector Pipe 18” (46cm) below ceiling

Min. 2” (5cm)

Insulated Chimney Min. 2” (5cm)

Masonry

For rear venting or other unlisted configurations, consult the local building codes and follow the NFPA 211 guidelines. If the stovepipe is fitted with a baffle, it must be manually operated, visibly placed for ease of use, and must not close completely. Consult your chimney expert if you have any questions. Important note: Please ensure that there is easy access to the chimney cleanout door.

170

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User Manual Q-Tee II USA

If this stove is not installed properly, a home fire may result. To reduce this risk, please

follow the directions for installation carefully.

Installation Precautions and Specifications Before installation, remember to consult your local building inspector or fire marshal to determine the need to obtain a permit. Also enquire about restrictions and installation inspection requirements in your area. If utilizing an existing chimney, it is recommended that a professional mason or stove installer do a complete check-up of the chimney, liner, and flue beforehand. In order for the stove to work and draw properly, sufficient air supply is important. Be especially aware of any mechanical fans (e.g. kitchen or bathroom exhaust systems) that may affect the proper draw. Do not use grates, andirons, or other fuel support methods. Build fire directly on hearth. Make sure that the floor and the sub-floor of the room in which the stove is installed is designed to carry the extra weight of the stove. The floor protector plate must be made of a non-combustible material. The floor protection plate must lie under the stove and extend 16” (41cm) (18” (45cm) in Canada) in front of the stove door, 8” (20cm) beyond the sides of the fuel-loading door, and under the pipe and 2” (5cm) beyond each side for back venting. In Canada, an 8” (20cm) floor protection is required beyond the sides of the stove and in the back of the stove (0” in the back for the US). The floor protection needed on the floor when used WITHOUT the base is required to have thermal protection with an R value of 3.19 Btu*in/Hrs*ft2*°F (equal to 0.46 w/mk in SI units) When deciding where to install your stove, the heat distribution to other rooms should be taken into consideration. Put the stove at a safe distance from combustible materials; see the references at the name tag of the stove.

171

9


Date of manufacture Date of fabrication

C

Adjacent wall

Month Mois

A: Mur latéral - Appareil B: Mur arriére - Appareil C: Mur de coin - Appareil D: Plafond - Lappareil E: Distance meuble devant

172

Floor protection must be non-combustible material extending beneath the stove, and to the front and sides from door opening and to the rear as indicated. The floor protection needed on the floor when used WITHOUT the base is required to have thermal protection with an R value of 3.19 Btu*in/Hrs*ft2*°F (equal to 0.46 w/mk in SI units). with the base, the floor protection is not required to have thermal protection (R=0)

** Not Tested - NFPA Guidelines in USA, CAN/CSA B365-M91 in Canada

NON COMBUSTIBLE MATERIAL 1" THICK (K-VALUE = 0,84 ((BTU*IN)/(FT2*HR*°F)))

FLOOR PROTECTION:

Tested to: UL 1482 ULC S627-00

Serial no. N° de série

8"

Front

8"

Floor Protector must be under connector pipe and 2" (5 cm) to the side for a thru-the wall configuration.

Floor protection for Canada: 30" (76 cm) from unit to front of floor protector.

8"

FLOOR PROTECTOR

Made in Denmark Fabriqué au Danemark

Report No. #

La protection de sol doit être au moins de 3/8 inch matériel non combustible placé sous le foyer s'étendant vers l'avant, les côtés les ouvertures et l'arriére comme induqué.

** Non testé - NFPA Guidelines au USA, CAN/CSA B365-M91 au Canada

This wood heater needs periodic inspection and repair for proper operation.  Consult the owner's manual for further information. It is against federal  regulations to operate this wood heater in a manner inconsistent with the  operating instructions in the owner's manual.

U.S. ENVIRONMENTAL PROTECTION AGENCY Certified to comply  with 2020 particulate emission standards using crib wood.  0.9  g/hr, Method 28R

**

**Rear/Top vent option Ceiling

Year Année

For Use With Solid Wood Fuel Only

A: SIDEWALL TO UNIT 15 B: BACKWALL TO UNIT 15 C: CORNERWALL TO UNIT 13 D: CEILING TO APPLIANCE E: FRONT WALL / FURNISHING:

Side wall

Écartement minimum

E

MINIMUM CLEARANCES

A

Back wall

B

Clearances to combustible surfaces

Model Modéle

Adjacent wall

Model: Q-Tee II USA Solid Fuel Room Heater

Industrivej 20, DK-9900 Frederikshavn, Denmark

RAIS A/S

C

Manufactured by:

D

10

16"

US English User Manual Q-Tee II USA


US English

User Manual Q-Tee II USA

173

11


US English

User Manual Q-Tee II USA

Clearance to combustible walls To find out whether the wall by which the stove is to be placed is combustible or not, please contact your architect or the local building authorities. If the floor is combustible, the stove must be placed on a non-combustible plate such as steel, glass or stone.

Ref.

Description

Minimum clearence

A

Sidewall to unit

B

Backwall to unit

C

Cornerwall to unit

D

Ceiling to appliance

E

Frontwall/furnishing Industrivej Industrivej 20,20, DK-9900 DK-9900 Frederikshavn, Frederikshavn, Denmark Denmark

Manufactured by:by: Manufactured

RAIS RAISA/S A/S

Model: Model: Q-Tee Q-Tee II USA II USA Solid Solid Fuel Fuel Room Room Heater Heater

ForFor Use Use With With Solid Solid W Date Date of of manufacture manufacture Date Date of of fabrication fabrication

Model Model ModĂŠle ModĂŠle

Month Month Mois Mois

Clearances Clearances to tocombustible combustiblesurfaces surfaces

Adjacent wall Adjacent wall

B B E E

Side wall Side wall AA

C C

Adjacent Adjacent wall wall

Back wall Back wall

CC

174

12


US English

User Manual Q-Tee II USA

**Rear/Top vent option Ceiling

**: Please refer to NFPA guidelines in USA and CAN/CSA B365-M91 in Canada.

FLO

D

**

Flo Ca from

Flo con sid 175

13


US English

User Manual Q-Tee II USA

Clearance to non-combustible wall We recommend a minimum clearance to non-combustible material of at least 2” (50 mm) so that cleaning is easy. The cleaning door should be accessible at all times. Clearances may only be reduced by means approved by the regulatory authority.

Floor protection Floor protection must be non-combustible material extending beneath the stove, and to the front and sides from door opening and to rear as indicated.

Report No. #

Floor protection for Canada: 18” (45 cm) from unit to front of floor protector. Floor protector must be under connector pipe an 2” (5 cm) to the side for a thru-the Made in Denmark Serial no. wall configuration.

Fabriqué au Danemark

N° de série

option

FLOOR PROTECTOR 8"

8" 16"

8"

Front Floor protection for Canada: 30" (76 cm) from unit to front of floor protector.

14

Floor Protector must be under connector pipe and 2" (5 cm) to176the side for a thru-the wall configuration.


User Manual Q-Tee II USA

US English

Firewood Only burn wood that has been seasoned for at least one full year (two years is better). If the wood has not been seasoned or dried, energy will be lost in evaporating the water held in the wood. Furthermore, condensation or creosote might occur in the stove and pipe when damp wood is burnt. Freshly cut wood contains approx. 60-70% water and is completely unsuited for burning. Log size should be about 2” (5 cm) less than the width of the firebox

NEVER burn trash (plastic and other types of artificial materials emit harmful gases), driftwood, treated or painted wood, artificial logs or non-seasoned wood. All types of wood heat equally per pound; however, the density of wood is not the same as is shown in the table below, where the combustible value of wood dried for two years with a moisture of 15-20% is taken into account. See table to the left.

Drying and storage Wood to be used for burning in a stove should be dried for two years to ensure optimal burning. Here are some storage tips: • Cut and split the wood before storing. • Keep the woodpile in a dry sunny place, protected from the rain. Do not cover the pile with plastic, because that prevents the wood from drying properly. • Stack the wood with enough space between the rows to ensure good air circulation. • Bring the logs inside the house two-three days prior to use. Wood type

Dry wood In comparison kg/m³ to beech

Beech and oak

580

100 %

Ash

570

98 %

Maple

540

93 %

Birch

510

88 %

Mountain pine

480

83 %

clearances or within the space

Fir

390

67 %

required for charging and

Poplar

380

65 %

Do not store solid fuel within space heater installation

ash removal. 177

15


US English

User Manual Q-Tee II USA

Adjusting the combustion air All RAIS stoves are equipped with an easy-to-use handle for adjusting the air control. For the various positions of the control please see the following illustrations. To ensure proper combustion process it is very important to supply the correct quantity of air at the right time and place. The adjustment range made from factory may not be altered for increasing firing for any reason. Primary air is defined as combustion air for burning the mass of wood and stimulates production of volatile gases. Secondary air is used to burn off the gases at high temperatures (above 1,000°F/540°C) and to keep the glass free of soot. The secondary air is let through the air control beneath the combustion chamber and is heated through the side channels, which is then directed to the glass. The warm air runs along the glass, keeping it free of soot. At the very back of the combustion chamber there is a tertiary channel at the top that helps to combust the remaining gases. When positioning the air control between Pos. 1 and 2 optimum utilization of the energy contents of the wood is obtained, because of sufficient oxygen for combustion. When the flames burn bright and yellow, the control has been adjusted correctly. Finding the correct position takes some trial and error, but is easy to find. Never close the air control completely when using the stove. A typical error is to close the control too soon, because the heat gets too intense. This results in the appearance of a dark cloud of smoke from the chimney and that means the energy value of the wood is not being used properly. It is important for proper control of the fire that the instructions in the manual are followed and the stove door normally is kept closed. It is also necessary to keep the seals in a good condition.

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REMEMBER THE STOVE IS HOT WHILE IN OPERATION, SO KEEP CHILDREN, CLOTING, AND FURNITURE AWAY. CONTACT WITH A STOVE WHEN BURNING MAY CAUSE SKIN BURNS. Using the stove Only use wood as fuel as described in the firewood section of this manual.

Adjusting the air control There are three different positions for air control: Position 1: The damper is almost closed meaning that there is a minimal air intake.

Position 2: Pull the handle out to the first stop. This position provides full secondary air intake. In the event of ordinary combustion the handle is to be adjusted to the interval between pos. 1 and 2. When the flames are clear and yellow, the damper has been adjusted correctly resulting in slow/optimal combustion.

Position 3: Pull the handle all the way out. The damper is fully open and provides full primary and secondary air intake. This position is for the kindling phase and is not used in connection with normal operation.

Control If the ashes are white and the combustion chamber walls not covered with soot, the air adjustment has been correct and the wood sufficiently dry. 179

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First Fire Your new RAIS should be broken into gently for top performance and to prevent paint damage, cracks in the firebrick, and excessive wear and tear. Start with a small fire (never overload the firebox) to allow the materials to get accustomed to the higher temperatures, and then gradually increase the intensity. Use up to a maximum of two logs. For the first few fires you may detect a strange smell that comes from heat treating the paint and materials. This is normal and will soon disappear. Just ensure there is plenty of fresh air in the room. Furthermore, during the initial heating up and cooling down, the metal may emanate some clicking sounds due to being exposed to the large differences in temperature. This is normal as well. For wood to burn properly, the right amount of air has to be supplied at the right time and place.

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Lighting and Stoking To light the stove, use alcohol briquettes or similar, as well as approx. 2 kg of firewood, split into kindling sticks. Set the air damper to the fully open position. Be carefull not to place the firewood too close to the opening and glass.

TIPS before firing up: Open a door or window close to the wood burning stove. If there is wind in the stove coming from the chimney, it is advisable to place a curled-up piece of newspaper between the upper baffle plate and the chimney, set the paper on fire, and wait until you hear a â&#x20AC;&#x153;rumblingâ&#x20AC;? noise in the chimney. This means that there definitely is a draught in the chimney and you avoid smoke in the room.

Light the fire and shut the door, leaving an open gap of approx. 10-15 mm.

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US English

User Manual Q-Tee II USA When the flames are clear - after approx. 5-10 min. - close the door.

After approx. 10-20 min. - when you have a good bed of glowing embers - add 2-3 pieces of wood. Be carefull not to place the firewood too close to the opening and glass. Leave the door ajar until the fire has caught on properly - close the door.

After approx. 5 min. - or when the flames are clear and stable - close the damper gradually. It is recommendable to have a layer of ash of approx. 20 mm, as it has an insulating effect.

Note! During operation the door should always remain shut.

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Fuel caution Do not burn trash (plastic and other artificial materials emit harmful gases), driftwood, treated wood, artificial logs, or non-seasoned wood. Never use gasoline, gasoline-type lantern fuel, kerosene, charcoal lighter fluid, naphtha, engine oil, or similar liquids to start or freshen up a fire in your RAIS stove. Keep all such liquids well away form the stove while it is in use.

Care and maintenance You should have your chimney and stove checked once every two months during the heating season or at least once a year by a professional chimney sweep and cleaned as needed. When cleaning the stove carefully inspect the seals for damage. The seals should be in good conditions and without damage. When cleaning, checking or repairing, the stove must be cold. If the glass has been covered in soot, here is a simple piece of advice: • Dampen a piece of paper or newspaper, dip it into the cold ashes and rub the sootcovered glass. • Use another piece of paper to polish the glass. • A good commercial glass cleaner can also be used. • Do not use abrasive cleaners. The outer surfaces can be wiped with a soft, dry rag and if needed a small amount of mild detergent. NEVER scrub the surfaces. Cleaning the soapstone: Day-to-day cleaning can be made with a damp rag. If necessary the soapstone can be carefully cleaned with some paint-thinner from the hardware store. For difficult stains that cannot be dissolved by the paint-thinner, lightly sand them. Cleaning the combustion chamber: Rake out the ashes and store them in a metal container with a tight-fitting lid until cooled completely before throwing them in the trash can. Other waste shall not be placed in this container. Remember NEVER to clean all ashes from the combustion chamber. Leave about a 3/4” layer for better combustion. 183

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Cleaning of smoke chicane

Remove the smoke converter plate by tilting it to one side and turning it a little slantwise. Pull out the plate carefully.

Then remove the smoke impediment by lifting it up and moving it forward. Carefully lift out the smoke impediment.

There is now an unblocked view of the smoke discharge. Remove dirt and dust, and mount the parts in reverse order.

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User Manual Q-Tee II USA

US English

Creosote

Formation and Need for Removal When wood is burned slowly, it produces tar and other organic vapors, which combine with expelled moisture to form creosote.

The creosote vapors condense in the relatively cool chimney flue of a slow-burning fire. As a result, creosote residue accumulates on the flue lining. When ignited, this creosote makes an extremely hot fire. The chimney and chimney connector should be inspected at least once every two months during the heating season to determine if a creosote buildup has occurred.

If creosote

has accumulated, it should be removed to reduce the risk of a chimney fire.

DISPOSAL OF ASHES ASHES SHOULD BE PLACED IN A METAL CONTAINER WITH A TIGHTFITTING LID. THE CLOSED CONTAINER OF ASHES SHOULD BE PLACED ON A NONCOMBUSTIBLE FLOOR OR ON THE GROUND, WELL AWAY FROM ALL COMBUSTIBLE MATERIALS, PENDING FINAL DISPOSAL. IF THE ASHES ARE DISPOSED OF BY BURIAL IN SOIL OR OTHERWISE LOCALLY DISPERSED, THEY SHOULD BE RETAINED IN THE CLOSED CONTAINER UNTIL ALL EMBERS HAVE THOROUGHLY COOLED. OTHER WASTE SHALL NOT BE PLACED IN THIS CONTAINER. The firebox lining is made out of vermiculite slab insulation (skamol), which protects the outer steel plates from overheating. With time small cracks might appear; this is normal. If it breaks however, it must be replaced. Vermiculite is a porous, high-insulated material and must therefore be handled with care.

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Trouble Shooting Smoke seeping through the door: • Not enough draft in the chimney (<12 Pa) • Check if there are any obstructions in the chimney or the wind pipe • Check whether the kitchen exhaust fan is in use and if so, turn it off and open the window for a short period of time Soot on the glass: • The wood is too damp • Make sure that the stove is sufficiently heated up before closing the door • The air control has been set too low The stove burns too quickly: • Gasket may not be tight, please check and replace if necessary • Chimney draft maybe too high >22 Pa, if this is the case, please install a damper The stove is burning too slowly: • Not sufficient amount of firewood • Not enough air is getting into the stove • Blocked chimney • Leaking chimney • Leak between chimney and pipe If the problems continue we recommend contacting your chimney sweep or your local RAIS dealer. Chimney fire, soot fire or creosote fire: In case of a fire in the chimney quickly close all doors, dampers, vents and call your local fire department. NEVER use water to extinguish the fire.

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Spare parts Q-Tee II USA If spare parts other than those recommended by RAIS are used, the warranty is voided. All replaceable parts can be bought as spare parts from your RAIS distributor. For reference see spare parts drawing Q-Tee II (front of the user manual).

Pos. PCS.

Item number.

Description

1

1

8382090

Steel door

2

1

8381090

Glass door

3

1

838052490

Cover Q-Tee II

4

1

8392200

Fire brick set

5

1

8383800

Shaking grate

6

1

8384001

Ash pan

7

1

838121090

Air guiding plate

8

1

839121190

Turbo plate (steel door)

9

1

839121490

Turbo plate (glass door)

10

1

8381301

Smoke chicane

11

1

61-110

Flue collar for USA- England - 6â&#x20AC;?

12

1

8380990

Air damper

13

1

838040590

High socket complete

14

1

8385500

Seal set

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10

11

4

5

1 2

7

8

9

14 13

12 6 3

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CHAUFFEZ EN RESPECTANT L’ENVIRONNEMENT!

5 conseils pour une combustion raisonnable et respectueuse - une question de bon sens aussi bien pour l’environnement que pour votre porte-monnaie

1. Allumage efficace. Utiliser des brindilles, du petit bois bien sec et éventuellement un peu de papier journal. Ouvrir le volet d’air primaire pour assurer un apport d’air suffisant pour la combustion rapide des gaz dégagés par le bois qui chauffe. 2. Ne charger que peu de bois à la fois - cela assure une meilleure combustion. Ne pas oublier que l’apport d’air doit être suffisant à chaque fois que vous rechargez du bois dans le poêle. 3. Lorsque les flammes se sont apaisées, il est nécessaire d’ajuster le volet pour réduire l’arrivée d’air. 4. Lorsqu’il ne reste que des braises dans le foyer, l’alimentation d’air peut être encore réduite pour convenir précisément au besoin de chaleur. Une réduction de l’alimentation en air entraine une combustion plus lente des braises ainsi qu’une réduction de la perte de chaleur par le conduit de cheminée. 5. N’utiliser que du bois bien sec - c’est-à-dire avec un taux d’humidité d’environ 15 à 22 %.

Le verre ne peut pas être recyclé. Le verre doit être jeté avec les déchets résiduels de la céramique et de la porcelaine. Le verre résistant à la chaleur a une température de fusion plus élevé et ne peut donc pas être réutilisé. Veillant à ce que le verre résistant à la chaleur ne finisse pas parmi les produits repris, est une aide et une contribution importante à l’environnement.

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Sous réserve d’erreurs typographiques.

Le four est emballé dans l’emballage de récupération. L’emballage doit être emporté selon la réglementation nationale concernant l’élimination des déchets.


Français canadien

Manuel d’utilisation des modèles Q-Tee II USA

Q-Tee II USA Rapport OMNI n0.: # Révision : 1 Date : 11-11-2015

INTRODUCTION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 30 GARANTIE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 30 SPECIFICATIONS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 31 CONVECTION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 32 VITRE ET REMPLACEMENT DE LA VITRE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 32 CHEMINEE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 33-34 INSTALLATION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 35 ETIQUETTE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 36-37 DISTANCES A DES PAROIS COMBUSTIBLES . . . . . . . . . . . . . . . . . . . . . . . . . 38-39 DISTANCES A DES PAROIS NON COMBUSTIBLES . . . . . . . . . . . . . . . . . . . . . . . . . 40 PROTECTION DE SOL . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 40 BOIS A BRULER . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 41 SECHAGE ET STOCKAGE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 41 REGLAGE DE LA COMBUSTION D’AIR . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 42 UTILISATION DU POELE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 43 REGLAGE DE L’ARRIVEE D’AIR . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 43 CONTROLE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 43 PREMIER FEU . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 45 ALLUMAGE ET ENTRETIEN DU FEU . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 46-47 PRECAUTIONS A PRENDRE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 48 ENTRETIEN ET MAINTENANCE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 48 NETTOYAGE DU SYSTEME DE FUMEE/DEFLECTEUR . . . . . . . . . . . . . . . . . . . . . 49 ELIMINATION DES CENDRES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 50 DEPANNAGE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 51 DIAGRAMMES DE PIECES DETACHEES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 52-53

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Français canadien

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Introduction Félicitations pour l’achat de votre nouveau poêle à bois RAIS. Un poêle à bois RAIS est plus qu’une simple source de chaleur. C’est le symbole même des efforts que vous réalisez pour décorer votre foyer à l’aide de produits originaux de haute qualité. VEUILLEZ LIRE ENTIEREMENT CE MANUEL AVANT D’INSTALLER ET D’UTILISER VOTRE NOUVEAU POELE RAIS. LE NON RESPECT DES INSTRUCTIONS QU’IL CONTIENT PEUT ENTRAÎNER DES DOMMAGES MATERIELS, DES BLESSURES CORPORELLES ET MEME LA MORT. GARDEZ-LE À PORTEE DE MAIN, AFIN DE POUVOIR LE CONSULTER EN CAS DE BESOIN. Tests de sécurité et de respect de l’environnement Les poêles de la série Topas/Opus de RAIS ont été testés par le laboratoire OMNI-Test Laboratories, Inc. de Beaverton, Oregon et sont conformes aux normes UL 1482 et ULC S627. Ils sont aussi homologués EPA et satisfont aux sévères normes en matière d’environnement de l’Etat de Washington. A titre de référence, écrivez le numéro de production de votre poêle à bois RAIS ici. Ce numéro doit être indiqué lors de toute question ou réclamation concernant ce produit.

Garantie Nous proposons une garantie de cinq ans sur votre poêle RAIS. Cette garantie couvre tous les défauts de matériau ou de main--d’œuvre. Cependant, elle ne couvre pas les dommages dus à une mauvaise utilisation ou à une négligence ni la vitre, les joints et les briques réfractaires.

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U.S. ENVIRONMENTAL PROTECTION AGENCY Certified to comply with 2020 particulate emission standards using crib wood. 0.9 g/hr, Method 28R This wood heater needs periodic inspection and repair for proper operation. It is against federal regulations to operate this wood heater in a manner inconsistent with operating instructions in this manual. This wood heater has a manufacturer-set minimum low burn rate that must not be altered. It is against federal regulations to alter this setting or otherwise operate this wood heater in a manner inconsistent with operating instructions in this manual.

Caractéristiques techniques: RAIS Topas Poids - poêle Bloc de stéatite

275 lbs (125 kg) 324 lbs (147kg)

Poêle extérieur :Largeur/profondeur/hauteur (en pouces)

22.9 / 16.1 / 23.5

Largeur/profondeur/hauteur intériure du foyer (en pouces)

17.5 / 10.9 / 10.4

Capacité de chauffage à -20°C/-4°F

Environ

m² /

pieds carrés

Quantité de bois recommandée: Fonctionnement intermittent: Flux de masse du gaz dans le conduit: Température du gaz dans le conduit:

Entretenez le feu toutes les trois heures grammess par seconde °C /

°F

Tuyau de poêle à connecteur mural unique:

6” (15 cm)

Tuyau de cheminée - Classe A, UL-103 HT:

6” (15 cm)

Régime thermique optimum :

kBTU ( kW)

Régime mini/maxi (kW): Pression théorique de poêle minimum en surrégime: Taux d’émission de particules EPA selon tests:

kBTU (

kW)

12 Pascals (0.048”WC) grammes/heure

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Convection Tous les poêles RAIS sont des poêles à convection, si bien que leurs parois ne chauffent jamais outre-mesure. La convection consiste à insuffler de l’air froid dans le système à la base du poêle et à le faire monter dans le conduit de convection situé le long de la chambre de combustion du poêle. L’air chaud s’échappe par le haut du poêle, d’où la création d’une circulation d’air rapide dans la pièce.

Vitre et remplacement de la vitre. Tous les poêles RAIS sont fournis avec une vitre Robax® dans la porte. Le verre Robax® est un type de verre céramique adapté aux poêles. La vitre est installée par RAIS en tant que partie intégrante de la porte. Vérifiez l’absence de fissures dans la vitre avant le premier feu. Les mauvais traitements peuvent provoquer des dégâts au niveau de la vitre et de la porte. Évitez de heurter la porte ou la vitre, et de refermer violemment la porte Évitez de faire démarrer le feu trop près de la vitre ou de l’ouverture. Evitez d’utiliser le poêle si la vitre est cassée ; dans ce cas, prenez contact avec votre revendeur agréé. Si la vitre se fend lors de l’utilisation du poêle, laissez celui-ci brûler doucement le reste des braises sous surveillance. Évitez de fermer le déflecteur de cheminée si le poêle en est équipé. Prenez contact avec le revendeur agréé le plus proche de votre domicile. La vitre est fournie en tant que partie intégrante de la porte. Le verre Robax® ne doit être remplacé qu’à l’aide de pièces détachées d’origine de RAIS. Évitez d’utiliser des matériaux de remplacement. Le remplacement de la vitre doit être impérativement effectué par du personnel agréé.

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Cheminée Les poêles RAIS doivent être installés à l’aide d’un système de cheminée intégrée homologué UL 103 HT de classe A ou d’une cheminée maçonnée homologuée équipée d’une gaine de conduit. Au Canada, l’installation doit être conforme à la norme CAN/ CSA-B365. La cheminée doit dépasser du toit d’au moins 3’ (1 m), et de 2’ (0,6 m) par rapport à toute structure située à moins de 10’ (3 m). Les caractéristiques et la hauteur de la cheminée jouent un rôle très important dans l’utilisation optimale du poêle et nous recommandons une hauteur totale de 10’ (3 m). Remarque : Le tuyau de connexion de la cheminée ne doit pas traverser de grenier, d’espace sous toit, d’armoire, d’espace confiné, de plancher ou de plafond. Evitez de connecter ce poêle à un conduit de cheminée ou à une conduite de distribution d’air ou à tout système branché sur undeautre appareil. Connecteur cheminée

Vers le poêle

Sens d’écoulement du gaz

Tous les connecteurs de cheminée et sections de tuyau de poêle doivent être fixés les uns aux autres avec l’extrémité sertie dirigée vers le poêle. Cela permet d’éviter les débordements éventuels de créosote condensée ou liquide hors du tuyau ou de la partie supérieure du poêle.

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Français canadien

Manuel d’utilisation des modèles Q-Tee II USA Eléments d’installation obligatoires:

A. B. C. D.

B. E.

F.

A. Couvercle de cheminée B. Cheminée isolée C. Collier tempête D. Raccord de toit E. Boîte de support de plafond ou entretoise de bouclier/protection incendie F. Connecteur de cheminée Pour une évacuation verticale dans une cheminée de classe A, un tuyau mural unique (de diamètre minimum 24) peut être utilisé dans la pièce où est installé le poêle. Reportez-vous aux instructions du fabricant pour la connexion à la cheminée considérée. Le diamètre du tuyau de cheminée/poêle ne doit pas être inférieur à 6” (15 cm). Pour une évacuation directement dans une cheminée maçonnée ou par le biais d’une virole, le haut du tuyau mural individuel doit être situé au moins à 18” (46 cm) en dessous de tout plafond combustible et être conforme aux directives et méthodes NFPA 211. Reportez-vous au diagramme de gauche.

Conduit Chimneyde cheminée Flue

Tuyau de connexion Connector Pipe 18”(46 cm) sous plafond 18” (46cm) below ceiling

Min. 2” (5cm)

Cheminée Insulated Chimney isolée Min. 2” (5cm)

Masonry Maçonnerie

Pour l’évacuation arrière ou d’autres configurations non représentées, veuillez vous reporter aux normes de construction locales et respecter les directives NFPA 211. Si le tuyau de poêle est équipé d’un déflecteur, il doit être actionné manuellement, placé de façon visible pour en faciliter l’utilisation et ne doit pas fermer complètement. Consultez votre expert en cheminées pour toute question éventuelle. Remarque importante : Assurez-vous que la porte de nettoyage de la cheminée est facilement accessible.

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Si ce poele n’est pas installe correctement, il risque de provoquer un incendie domestique. Pour reduire ce risque, veuillez respecter scruoileusement les instructions d’installation.

Installation Précautions et caractéristiques techniques: Consultez l’inspecteur de la construction ou le commissaire des incendies le plus proche de votre domicile avant l’installation, afin de déterminer s’il est nécessaire d’obtenir un permis. Vérifiez également l’existence ou non de restrictions et de conditions d’inspection des installations dans votre zone. Si vous utilisez une cheminée existante, nous vous suggérons de demander à un maçon ou à un installateur de poêles professionnel d’effectuer une inspection complète préalable de votre cheminée, de la gaine et du conduit. Pour que le poêle fonctionne et tire correctement, il faut disposer d’une arrivée d’air suffisante ! Vérifiez en particulier la présence éventuelle de ventilateurs mécaniques (de cuisine ou de salle d’eau notamment), susceptibles d’affecter la qualité du tirage. Vérifiez que le sol et le sous-sol de la pièce dans laquelle le poêle est installé sont conçus pour supporter la surcharge pondérale due au poêle. Le protecteur de sol ou la plaque doivent être fabriqués à l’aide d’un matériau non combustible. La plaque de sol doit couvrir la partie située sous le poêle et dépasser de 16” (41 cm) (18” (45 cm) au Canada) devant la porte du poêle, de 8” (20 cm) des deux côtés de la porte de chargement du combustible, ainsi que sous le tuyau et de 2” (5 cm) des deux côtés de la ventilation arrière. Au Canada, une protection de sol de 8” (20 cm) est obligatoire des deux côtés et à l’arrière du poêle (0” à l’arrière aux EU). Lors de l’installation du poêle, tenez compte de la diffusion de la chaleur au niveau des autres pièces. Placez le poêle à bonne distance des matériaux combustibles ; reportezvous aux références sur l’étiquette du poêle. 197

35


Date of manufacture Date of fabrication

C

Adjacent wall

Month Mois

A: Mur latéral - Appareil B: Mur arriére - Appareil C: Mur de coin - Appareil D: Plafond - Lappareil E: Distance meuble devant

198

Floor protection must be non-combustible material extending beneath the stove, and to the front and sides from door opening and to the rear as indicated. The floor protection needed on the floor when used WITHOUT the base is required to have thermal protection with an R value of 3.19 Btu*in/Hrs*ft2*°F (equal to 0.46 w/mk in SI units). with the base, the floor protection is not required to have thermal protection (R=0)

** Not Tested - NFPA Guidelines in USA, CAN/CSA B365-M91 in Canada

NON COMBUSTIBLE MATERIAL 1" THICK (K-VALUE = 0,84 ((BTU*IN)/(FT2*HR*°F)))

FLOOR PROTECTION:

Tested to: UL 1482 ULC S627-00

Serial no. N° de série

8"

Front

8"

Floor Protector must be under connector pipe and 2" (5 cm) to the side for a thru-the wall configuration.

Floor protection for Canada: 30" (76 cm) from unit to front of floor protector.

8"

FLOOR PROTECTOR

Made in Denmark Fabriqué au Danemark

Report No. #

La protection de sol doit être au moins de 3/8 inch matériel non combustible placé sous le foyer s'étendant vers l'avant, les côtés les ouvertures et l'arriére comme induqué.

** Non testé - NFPA Guidelines au USA, CAN/CSA B365-M91 au Canada

This wood heater needs periodic inspection and repair for proper operation.  Consult the owner's manual for further information. It is against federal  regulations to operate this wood heater in a manner inconsistent with the  operating instructions in the owner's manual.

U.S. ENVIRONMENTAL PROTECTION AGENCY Certified to comply  with 2020 particulate emission standards using crib wood.  0.9  g/hr, Method 28R

**

**Rear/Top vent option Ceiling

Year Année

For Use With Solid Wood Fuel Only

A: SIDEWALL TO UNIT 15 B: BACKWALL TO UNIT 15 C: CORNERWALL TO UNIT 13 D: CEILING TO APPLIANCE E: FRONT WALL / FURNISHING:

Side wall

Écartement minimum

E

MINIMUM CLEARANCES

A

Back wall

B

Clearances to combustible surfaces

Model Modéle

Adjacent wall

Model: Q-Tee II USA Solid Fuel Room Heater

Industrivej 20, DK-9900 Frederikshavn, Denmark

RAIS A/S

C

Manufactured by:

D

36 16"

Français canadien Manuel d’utilisation des modèles Q-Tee II USA


Français canadien

Manuel d’utilisation des modèles Q-Tee II USA

199

37


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Manuel d’utilisation des modèles Q-Tee II USA

Distance aux parois combustibles Pour savoir si la paroi près de laquelle le poêle doit être placé est combustible ou pas, veuillez consulter votre architecte ou les autorités locales en matière de bâtiment. Si le sol est combustible, le poêle doit être placé sur une plaque non-combustible en métal, en verre ou en pierre.

Manufactured Manufactured by: by: Réf. A B C

Description

Distance minimum

Paroi latérale à unité

A/S ParoiRAIS arrière à unité RAIS A/S

”(

cm)

”(

cm)

ParoiIndustrivej de coin20, à unité ”( cm) 20, DK-9900 Frederikshavn, Denmark Industrivej DK-9900 Frederikshavn, Denmark

D

Paroi latérale à connecteur

E Paroi arrière à connecteur Model: II USA Model: Q-TeeQ-Tee II USA Heater SolidSolid Fuel Fuel RoomRoom Heater

”(

cm)

”(

cm)

For With Use With For Use SolidSol Wo

of manufactureMonthMonth Date Date of manufacture of fabrication Mois Mois Date Date of fabrication

ModelModel Modéle Modéle

Clearances to combustible surfaces Clearances to combustible surfaces

C

C

200

38

C

C

Adjacent wall

B

B E

A

E

Side wall

Side wall

A

Adjacent wall

Adjacent Adjacent wall wall

BackBack wall wall


Français canadien

Manuel d’utilisation des modèles Q-Tee II USA

**Rear/Top vent option Ceiling

**: Veuillez consulter les directives de la NFPA aux EU et de la CAN/CSA B365-M91 au Canada.

FLOOR PR

8

8"

16"

D

**

Fro

Floor prote Canada: 30 from unit to

Floor Prote connector side for a t

U.S. ENVIRONMENTAL PROTECTION AGENCY Certified to with 2020 particulate emission standards using crib wood g/hr, Method 28R

This wood heater needs periodic inspection and repair fo Consult the owner's manual for further information. It is 201 regulations to operate this wood heater in a manner inco 39


Français canadien

Manuel d’utilisation des modèles Q-Tee II USA

Distance à paroi non combustible Nous recommandons une distance minimum à tout matériau non combustible d’au moins 2” (50 mm), afin de faciliter le nettoyage. La porte de nettoyage doit être accessible à tout moment. Les distances ne pourront être réduites que dans les cas approuvés par les autorités de régulation.

Protection de sol La protection de sol doit être en matériau non combustible dépassant derrière le poêle, et sur l’avant et les côtés de l’ouverture de porte, ainsi que sur l’arrière conformément aux indications.

Report No. #

Protection de sol pour le Canada : 18” (45 cm) de l’unité à l’avant du protecteur de sol. Le protecteur de sol doit se trouver sous le tuyau de connecteur et 2” (5 cm) sur le côté pour une configuration à travers le mur.

Made in Denmark Fabriqué au Danemark

Serial no. N° de série

PROTECTION DE SOL

FLOOR PROTECTOR

n

8"

8" 16"

8"

Front

40

Floor protection for 202 Canada: 30" (76 cm) from unit to front of floor protector.


Français canadien

Manuel d’utilisation des modèles Q-Tee II USA

Bois à brûler Ne brûlez que du bois ayant séché pendant au moins un an (2 si possible !). Si le bois n’a pas été entreposé ou n’a pas séché, une grande part de l’énergie calorifique servira à l’évaporation de l’eau contenue dans le bois. D’autre part, de la condensation ou de la créosote risque d’apparaître dans le poêle et le tuyau si vous brûlez du bois humide. Le bois coupé de fraîche date contient environ 60 à 70 % d’eau et est complètement impropre à la combustion. Les bûches doivent en principe mesurer environ 2” (5 cm) de moins que la largeur du foyer.

EVITEZ DE BRULER DES DECHETS (LES PLASTICS ET AUTRES DECHETS EMETTENT DES GAZ NOCIFS), DU BOIS ECHAPPE, TRAITE OU PAINT, DES BUCHES ARTIFICIELLES OU DU BOIS NON ENTREPOSE. Tous les types de bois ont le même pouvoir calorifique par livre ; cependant, la densité du bois n’est pas la même, comme indiqué dans le tableau ci-dessous, qui reflète la valeur de combustion d’un bois séché pendant deux ans avec un taux d’humidité de 15-20 %. Voir tableau de gauche.

Séchage et entreposage Le bois utilisé dans un poêle doit être séché pendant deux ans pour une combustion optimale. Voici quelques conseils d’entreposage : • Coupez et fendez le bois avant de l’entreposer. • Conservez la pile de bois dans un endroit ensoleillé et sec, protégé de la pluie. Evitez de recouvrir la pile avec un plastique, car cela empêcherait le bois de sécher correctement. • Empilez le bois avec assez d’espace entre les files pour garantir une bonne circulation de l’air. • Rentrez les bûches à l’intérieur deux à trois jours avant leur utilisation. Type de bois

Bois sec kg/m³ Comareé au hêtre

Hêtre et chêne

580

100 %

Frêne

570

98 %

Erable

540

93 %

Bouleau

510

88 %

Pin de montagne

480

83 %

Sapin

390

67 %

Peuplier

380

65 %

EVITEZ DE STOCKER DU COMBUSTIBLE SOLIDE A PROXIXITE D’UNE IN STALLATION DE SHAUFFAGE OU DANS L’ESPACE REQUIS POUR CHARGER ET DECHARGER LES CENDRES. 203

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Réglage de la combustion d’air Tous les poêles RAIS sont équipés d’une poignée facile à utiliser pour le réglage de l’arrivée d’air. En ce qui concerne les différentes positions de la poignée, reportez-vous aux illustrations précédentes. Pour garantir une bonne combustion, il est très important de fournir la quantité d’air appropriée, au bon moment et au bon endroit. Les réglages effectués en usine ne doivent en aucun cas être modifiés pour augmenter le tirage. L’air primaire est défini comme l’air nécessaire à la combustion de la masse de bois et stimule la production de gaz volatiles. L’air secondaire est utilisé pour brûler les gaz à hautes températures (supérieures à 1 000°F (540°C)) et pour éviter l’accumulation de suie sur la vitre. L’air secondaire traverse le contrôle d’air situé sous la chambre de combustion et est réchauffé au travers des canaux latéraux, puis envoyé sur la vitre. L’air chaud balaie la vitre et y empêche la formation de suie. Tout à l’arrière de la chambre de combustion, il y a un troisième canal dans la partie supérieure pour aider à la combustion des gaz restants. Pour fournir suffisamment d’oxygène à la combustion, et tirer le meilleur parti possible de la capacité énergétique du bois, placez le contrôle d’air entre les positions 1 et 2. Des flammes brillantes et jaunes indiquent un bon réglage de l’arrivée d’air. La recherche de la bonne position s’effectue par essais et erreurs, mais est relativement facile à effectuer. Ne fermez jamais complètement l’arrivée d’air lorsque vous utilisez le poêle. Une erreur type consiste à fermer l’arrivée d’air trop tôt parce que la température devient trop élevée. Conséquence : la cheminée dégagera un nuage de fumée noire, indiquant par là une mauvaise utilisation de la capacité énergétique du bois. Pour une bonne maîtrise du feu, il importe de respecter les instructions figurant dans le manuel et de maintenir fermée la porte du poêle. On veillera également à conserver les joints en bon état.

ATTENTION LE VERRE CHAUD PROVOQUE DES BRULURES. EVITEZ DE TOUCHER LA VITRE TANT QU’ELLE N’A PAS REFROIDI. NE LAISSEZ EN AUCUN CAS LES ENFANTS TOUCHER LA VITRE. 204

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SOUVENEZ-VOUS QUE LE POELE EST CHAUD EN COURS DE FONCTIONNEMENT ET ELOIGNEZ PAR CONSEQUENT LES ENFANTS, LES VETEMENTS ET LES MEUBLES. LE CONTACT AVEC UN POELE BRULANT PEUT ENTRAINER DES BRULURES DE LA PEAU.

Utilisation du poêle N’utilisez que le bois combustible décrit dans la section BOIS A BRULER de ce manuel.

Réglage de l’arrivée d’air L’arrivée d’air comporte trois positions différentes :

Position 1: Le coupe-tirage est presque fermé, si bien que l’arrivée d’air est minimale.

Position 2: Poussez la poignée vers la droite jusqu’à ce qu’elle se bloque. Cette position permet une arrivée d’air secondaire complète. Pour une combustion ordinaire, la poignée doit être placée à mi-chemin entre les positions 1 et 2. Lorsque les flammes deviennent claires et jaunes, le coupe-tirage est bien réglé et la combustion s’effectue de façon lente et optimale. Position 3: Tirez sur la poignée, et poussez-la vers la droite. Le coupe-tirage est ouvert en grand et permet une arrivée d’aire primaire et secondaire complète. Cette position correspond à la phase d’allumage et ne doit pas servir au fonctionnement normal.

Contrôle Si les cendres sont blanches et les parois de la chambre de combustion ne sont pas couverts de suie, c’est que l’arrivée d’air est bien réglée et que le bois est suffisamment sec. 205

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206

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Premier feu Votre nouveau poêle RAIS doit être mis en route de façon progressive pour des performances optimales et pour éviter d’en abîmer la peinture, les fissures des briques réfractaires et une usure prématurée. Commencez par un feu restreint (ne surchargez jamais le foyer) pour permettre aux matériaux de s’habituer aux températures élevées, puis augmentez graduellement l’intensité. Utilisez 2 bûches maximum. Lors des premiers feux, vous risquez de détecter une odeur étrange liée au « chauffage » de la peinture et des matériaux. Cela est normal et cessera rapidement. Veillez simplement à ce que la pièce soit bien aérée ! Par ailleurs, lors des premiers cycles de température, vous risquez d’entendre des « cliquetis » dus aux différences de température importantes auxquelles sont soumises les parties métalliques. Rien que de très normal là encore. Pour que le bois brûle correctement, il faut fournir une quantité suffisante d’air au bon moment et au bon endroit.

207

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Allumage et entretien Pour allumer le poêle, utilisez des briquettes d’allumage ou quelque chose d’équivalent, ainsi qu’environ 2 kg de petit bois d’allumage fendu en fines bûchettes. Ouvrez l’arrivée d’air en grand. Évitez de placer le bois de chauffage trop près de l’ouverture et de la vitre.

CONSEILS avant l’allumage : Ouvrez une porte ou une fenêtre à proximité du poêle à bois. Si l’air de la cheminée, et donc du poêle, est agité, il est conseillé de placer un morceau de journal froissé entre le déflecteur supérieur et la cheminée, d’y mettre le feu, et d’attendre jusqu’à entendre un “grondement” dans la cheminée. Cela signifie que la cheminée tire bien et permet d’éviter d’enfumer la pièce.

Allumez le feu et repoussez la porte, tout en la laissant entrouverte avec un espace libre d’environ 10-15 mm.

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Français canadien

Manuel d’utilisation des modèles Q-Tee II USA Une fois les flammes claires et vigoureuses, soit au bout d’environ 5 à 10 mn, refermez la porte.

Au bout d’environ 10 à 20 mn, une fois la quantité de braises suffisante, ajoutez deux ou trois bûches supplémentaires. Laissez la porte entrouverte jusqu’à ce que les bûches prennent, puis refermez-la. Évitez de placer le bois de chauffage trop près de l’ouverture et de la vitre.

Au bout d’environ 5 mn, ou une fois que les flammes sont claires et vigoureuses, refermez petit à petit l’arrivée d’air. Il est recommandé de laisser une couche de cendres de 20 mm d’épaisseur dans la chambre de combustion, car elle servira d’isolation.

Remarque! En cours de fonctionnement, la porte doit toujours rester fermée. 209

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Précautions en matière de combustibles Evitez de brûler des déchets (les plastiques et autres déchets émettent des gaz nocifs), du bois échappé ou traité, des bûches artificielles, ou du bois non entreposé.

N’utilisez jamais d’essence, de carburant à lanterne de type essence, de kérosène, de fluide de briquet au charbon, d’huile à moteur, ou de liquides similaires pour démarrer ou relancer un feu dans ce réchaud. Conservez tous ces genres de liquides bien à l’écart du poêle pendant son utilisation.

Entretien et maintenance Faites vérifier votre cheminée et votre poêle tous les deux mois pendant la saison de chauffage, ou au moins une fois par an par un ramoneur professionnel et faites-les nettoyer si besoin est. Lors du nettoyage du poêle, vérifiez l’état des joints. Les joints doivent être en bon état et ne pas être endommagés. Lors de tout nettoyage, examen ou réparation, le poêle doit être froid. Si la vitre est couverte de suie, observez le conseil simple suivant : • Humidifiez un bout de papier ou de journal, trempez-le dans les cendres froides et frottez la vitre pleine de suie. • Utilisez un autre bout de papier pour polir la vitre. • On peut aussi utiliser un bon produit nettoyant pour les vitres. • Évitez d’utiliser des nettoyants abrasifs. Les surfaces extérieures peuvent être frottées à l’aide d’un chiffon doux et sec et, le cas échéant, un petit peu de détergent dilué. Ne grattez JAMAIS les surfaces. Nettoyage de la stéatite : Le nettoyage au jour le jour peut être effectué à l’aide d’un chiffon humide. Au besoin, la stéatite peut être soigneusement nettoyée à l’aide d’un diluant à peinture quelconque du commerce. Les tâches résistantes impossibles à dissoudre à l’aide du diluant peuvent être nettoyées au papier de verre doux. Nettoyage de la chambre de combustion : Récupérez les cendres et stockez-les dans un conteneur métallique hermétiquement fermé jusqu’à leur complet refroidissement avant de les transférer dans la benne à ordures. Évitez de placer d’autres détritus dans ce récipient. Rappel : ne JAMAIS enlever toutes les cendres de la chambre de combustion. Laissez une couche d’environ 3/4” pour une meilleure combustion. 210

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Nettoyage du système de chicane à fumée

Retirez le convertisseur de fumée en le penchant d’un côté et en le tournant légèrement sur la tranche. Retirez la plaque avec précaution.

Puis, retirez l’écran à fumée en le soulevant et en le tirant vers l’avant. Retirez l’écran à fumée avec précaution.

Vous avez désormais accès à l’extracteur de fumée. Éliminez saletés et poussières, puis remontez les pièces en sens inverse.

211

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Créosote

Formation et nécessité de s’en dèbarrasser

Lorsque le bois brûle à petit feu, il produit du goudron et d’autres vapeurs organiques, qui s’aaocient au surplus d’humiditè pour former la crèosote.

Les vapeurs de créosote

se condensent dans le conduit de sheminée relativement froid d’un feu qui couve.

Résul-

tat, les résidus de créosote s’accumulent sur le revêtement du conduit.

Une fois embrasée,

cette créosote génère des flammes extrêmement chaudes.

Le connecteur de sheminée et

ka cheminée doivent être inspectés tous les deux mois pedant la saison de shauffage pour détecter la présence éventuelle d’aune accumulation de crésote.

Si c’est le cas, il faut

l’éliminer pour réduire le risque d’incendie dans la cheminée.

Elimination des cendres PLACEZ LES CENDRES DANS UN CONTENEUR MÉTALLIQUE MUNI D’UN COUVERCLE HERMÉTIQUE. PLACEZ LE CONTENEUR AVEC LES CENDRES SUR UN PLANCHER ININFLAMMABLE OU SUR LE SOL, À BONNE DISTANCE DE TOUT MATÉRIAU COMBUSTIBLE, EN ATTENDANT DE LES ÉLIMINER DÉFINITIVEMENT. SI LES CENDRES SONT ÉLIMINÉES PAR ENFOUISSAGE DANS LE SOL OU DISPERSÉES LOCALEMENT, ELLES DEVRONT DEMEURER DANS LE CONTENEUR FERMÉ JUSQU’À LEUR REFROIDISSEMENT TOTAL. AUCUN AUTRE DÉCHET NE DOIT ÊTRE DÉPOSÉ DANS CE CONTENEUR. La gaine inférieure du foyer est constituée de brique réfractaire et la gaine latérale de plaques d’isolation en vermiculite (skamol), qui protègent les plaques d’acier extérieures contre la surchauffe. Avec le temps, des petites fissures peuvent apparaître, et cela est normal. Mais en cas de rupture, il faut les remplacer. La vermiculite est un matériau poreux à fort pouvoir isolant, qui doit par conséquent être manipulé avec précautions.

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Dépannage La porte laisse échapper de la fumée : • Pas assez de tirage dans la cheminée (<12 Pa) • Vérifiez la présence éventuelle d’obstacles dans la cheminée ou le tuyau d’aération • Vérifiez si le ventilateur d’extraction de la cuisine est en marche et, si c’est le cas, éteignez-le et ouvrez la fenêtre pendant quelque temps Suie sur la vitre : • Le bois est trop humide • Vérifiez que le poêle est suffisamment réchauffé avant de refermer la porte • L’arrivée d’air est mal réglée (trop faible) Le poêle brûle trop fort : • Le joint n’est peut-être pas étanche. Vérifiez-le et remplacez-le si besoin est • Le tirage de la cheminée est trop élevé (>22 Pa). Si c’est le cas, installez un coupetirage Le poêle brûle trop lentement : • Quantité de bois à brûler insuffisante • Le poêle ne reçoit pas assez d’air • Cheminée bloquée • Cheminée qui fuit • Fuite entre la cheminée et le tuyau Si les problèmes persistent, nous recommandons de consulter votre ramoneur ou votre distributeur RAIS local. Feu de cheminée, feu de suie ou feu de créosote : En cas de feu dans la cheminée, fermez rapidement toutes les portes, les coupe-tirages et les aérations, et appelez les pompiers de votre domicile. Ne JAMAIS utiliser de l’eau pour éteindre le feu.

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Pièces de rechange Q-Tee II USA Si vous utilisez d’autres pièces de rechange que celles recommandées par RAIS, la garantie devient caduque. Toutes les pièces interchangeables peuvent être achetées séparément chez votre distributeur RAIS. Consulter le schéma de pièces détachées spécifiques à chaque produit. Ref.

Nombre

No. produit

Description

1

1

8382090

Porte en acier

2

1

8381090

Porte en verre

3

1

838052490

Couverture Q-Tee II

4

1

8392200

Lot de briques réfractaires

5

1

8383800

Grille de décendrage

6

1

8384001

Bac à cendres

7

1

838121090

Plaque d’air

8

1

838121190

Turbo plaque (Porte en acier)

9

1

838121490

Turbo plaque (Porte en verre)

10

1

8381301

Chicane à fumée

11

1

61-110

Conduit de fumée USA - England 6”

12

1

8380990

Volet

13

1

838040590

Socle élevé complet

14

1

8385500

Garniture d’étanchéité

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10

11

4

5

1 2

7

8

9

14 13

12 6 3

215

53


RAIS A/S Industrivej 20 DK-9900 Frederikshavn www.rais.com

216

0138ws016e non cbi report  
0138ws016e non cbi report