Thermohydraulic performance of Curved Delta Winglet Vortex Generator using Ramped Expansion Channel

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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056

Volume: 11 Issue: 03 | Mar 2024 www.irjet.net p-ISSN: 2395-0072

Thermohydraulic performance of Curved Delta Winglet Vortex Generator using Ramped Expansion Channel

1Student, Department of Mechanical Engineering, Kumaraguru College of Technology, Tamil Nadu, India. 2Assistant Professor II, Department of Mechanical Engineering, Kumaraguru College of Technology, Tamil Nadu, India.

Abstract – Thesearchforimprovingheattransferandfluid mixing efficiency in diverse engineering applications has prompted the investigation of novel vortex generator geometries and combinations. This study examines the thermohydraulic performance of a new ramping expansion channelincorporatedcurveddeltawinglet vortexgenerator. The goal of the curved delta winglet vortex generator is to minimize pressure loss while increasing convective heat transferandcreatingvortices.Theuseofarampedexpansion channelisintendedtoregulatetheflowfieldandenhancethe capacity for heat transmission. The study methodically investigates the effects of ramp angle, winglet height, and geometrical factors on the system's thermohydraulic performance.

Key Words: Heat transfer, vortex generator, ramped expansionchannel,rampangle.

1.INTRODUCTION

Theutilizationofvortexgeneratorsinreal-timehasbeen madepossiblebyrecentsuccessfulinventions,research,and testing aimed at improving the effect of heat transmission.By creating vortices in the boundary layer, delta winglet vortex generators have traditionally shown themselves to be effective in enhancing convective heat transfer.Butmorerecently,developmentshaveaccelerated the shift to curved versions, leveraging the advantages of curved geometries to maximize vorticity production and flow management. Meanwhile, the addition of a ramped expansionchannelgivestheflowrouteanewdimensionand improves mixing and heat transmission properties. Comprehendingthecomplexitiesofheattransmissionand fluid movement in this unique arrangement is crucial for improvingthermalengineeringtechniques.Theknowledge gained from this study may be applied to the design and improvementofair-coolingsystems,heatexchangers,and other thermal management equipment, leading to the creation of more sustainable and energy-efficient engineeringsolutions.

1.1 Ramped expansion channel

Separated flows are difficult to understand because of their unpredictable nature. To better understand these

instabilitiesand,tosomeextent,reducetheunpredictability, researchers have been experimenting with a variety of shapes,includingrib,fence,bluffbodywithasplitterplate, abruptly expanding pipes, ramping duct, and cavities. Becauseofitsonesetseparationpoint,therampedexpansion channelprovedtobethemostpopularofall.Therearethree mainareasthatmakeuptheflowwake:theshearlayerarea, the separation bubble or recirculation zone, and the reattachment zone. These divisions are based on the importantflowcharacteristicsinaplanarrampinggeometry thathavebeenstudiedbypreviousresearchers.Duetothe unfavorable pressure gradient that forms into a thin boundary layer, the basic features of a ramped expansion flow start with an angular momentum in the flow. The turbulentstructuresinsidetheboundarylayermergeasthe flow moves downstream, expanding the boundary layer's area.Theterm"layerregion" referstothisarea wherethe boundarylayerformsandexpands.Inthespacebetweenthe shear layer and the nearby wall, this flow results in lowvelocityrecirculation.Therecirculationzoneoftheramping geometry produces a primary vortex in the center and a secondary vortex adjacent to the corner. When the shear layer eventually swings down towards the wall, the reattachment point is where the fluid's advantageous pressuregradienthitsthewallataspecificlocation.

1.2 Vortex Generator

To provide a safety buffer between the airspeed and stall speed,vortexgeneratorsaretoolsthathelplowerthestall speed. By increasing the flow's turbulent nature and decreasing the creation of boundary layers, vortex generatorsaidinimprovingheattransferperformance.Ina channel,thestrongturbulentflowofthemediumdecreases the development of boundary layers and increases heat transmission. Based on their features and usage patterns, vortex generators may be categorized. Both passive and active vortex generators are those. Using a certain aerodynamicsurfaceshape,passivevortexgeneratorsmay producerollingorlongitudinalverticeswithouttheneedfor outsidepowersources.Deltawinglet(DW)andDeltawinglet pair(DWP)arethemostutilizedconfigurations.Awingletis createdwhenthevortexgeneratorshavedistinctanglesof attack from one another, whereas a wing is defined as geometrypositionedperpendiculartothedirectionofflow.

International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056

Volume: 11 Issue: 03 | Mar 2024 www.irjet.net p-ISSN: 2395-0072

2. Methodology

Scientificallysounddiscoveriesareproducedbystudyusingasoundapproach.Theprocedureismadeeasy,efficient,and manageablebythecomprehensivestrategyitoffers,whichalsoaidsinkeepingresearchersoncourse.Findingtrustworthyand accuratedata,comingtoinsightfulconclusions,andaddingtothebodyofknowledgeareallhamperedbyapoorlydefined researchtechnique.

Design Calculations

Fabrication

Modelling

Observation and Calculation

3. Design Calculation

Settingupanexperimentisacrucialstepincarryingouta study. The experiment involves designing the vortex generatorsandthesuddenexpansionrampingflowductby consultingreferencesfromdifferentjournalsandmodifying theirspecificationsaccordingtotheneeds.Thefinaloutput variesdependingonthestability,capacity,performance,and durabilityofthematerialsutilizedintheprocess.

3.1. Ramped Expansion channel dimensions

Comic Section

dimensionsareinmm.

Fig. 2. ComicSection

Material Outsourcing

Resultsand Report Generation

Testing Section

dimensionsareinmm.

3. TestingSection

Ramped duct angle = 450

Fig. 1. MethodologyFlowchart
Fig.
Fig. 4.Rampedexpansionchannel

International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056

Volume: 11 Issue: 03 | Mar 2024 www.irjet.net p-ISSN: 2395-0072

3.2. Delta Vortex Generator Dimensions

 Height=27mm

 Length=45mm

 Radius=23mm

 Thickness=1mm

 Material=CurableAlumina

4. Component Specification

S.No. MATERIALS

DIMENSION

1 CopperPlate 1000x167x2.5mm

4 Plexiglass(acrylic)Sheet 1800×167×3mm

5 Thermocouple(T-type) ø=0.2mm(Accuracy =0.02°C)

6 Nylon 1kg

7 RockWool 2sq.m.

8 Blower 200CubicFeetPer Minute

9 Heater (stainlesssteel) 1000mm×200mm

10 VariacController 0-240V(singlephase)

11 DataAcquisitionSystem 18channels

12 Thermometer Accuracy=±0.02°C

Table.1. ComponentSpecification

5. Experimental Setup

Therock-woolinsulationbedispositionedatthebottom ofthetestsection,withtheheateremployedinbetweenthe copperplates.Weutilizeanairblowerontheothersideof theentrancetochangethedirectionoftheairflow.Variac controllers are used to regulate both the heater and the blower'svoltageinput.Plexisheetisusedtoconstructthe testandcomicsections,whicharejoinedtoformachannel thatisenclosedonallsidesexcepttheinputandoutflow.We employ18"T-type"thermocouples,whichareaffixedtothe copperplate'sbottominadirectionparalleltothestreamto

measure the temperature of the plate.A data acquisition system (DAQ) is then used to measure the readings from thesethermocouplesanddisplaythecorrespondingoutputs. The mass flow rate of air at the comic section's input is measured with a vane anemometer. Pressure transducers areusedatthechannel'sentranceandoutflowtomeasure thepressuredecrease.

Fig.6. ExperimentalSetup

6. Experimentation and Observation

In this experimentation, we position the Curved Delta VortexGeneratorwithhigherleadingedgeinbothcommon flowupandcommonflowdownconfigurationandobserve theirheattransmissioncapabilitiesbyvaryingthevelocityof thefluidfordifferentattackangleofthevortexgenerator.

 CommonFlowUp(CFU)configurationofCurved DeltaVortexGenerator – [Allanglecomparison]

FrictionFactor,f=(2*ΔP*Dh)/(ρ*V2*L)

ReynoldsNumber,Re=(ρ*V*Dh)/µ

The relation shows that the friction factor decreasesasthevelocityofthefluidincreasesand theReynolds numberincreasesasthevelocity of thefluidincreases.

Fig.5. CurvedDeltaVortexGenerator

International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056

Volume: 11 Issue: 03 | Mar 2024 www.irjet.net p-ISSN: 2395-0072

Fig.7. FrictionfactorvsReynoldsnumber

Nusseltnumber,Nu=(h*Dh)/k

ReynoldsNumber,Re=(ρ*V*Dh)/µ

The Nusselt number is the function of Reynolds numberraisedtothecertainpoweralongwiththe Prandtlnumber.

Laminar External flow, Nu ≈ 0.664 * (Re^0.5) * (Pr^0.33)

Turbulent External flow, Nu ≈ 0.037 * (Re^0.8) * (Pr^0.3)

Fig.8. NusseltnumbervsReynoldsnumber

The above graph(Fig.8.)indicates the relation betweenNusseltnumberandReynoldsnumberforvarious attackangles.

Boththeabovegraphs, (Fig.7.)and (Fig.8.) implies thattheattackangle750 showsthe betterthermohydraulic performancefactorwithgreaterheattransmissionrateand lower pressure loss compared to all other attack angles beingpositionedinthecommonflowupconfiguration

Attack Angle = 750

Table.2. DataobtainedforAttackangle750 inCFU

 Common Flow Down (CFD) configuration of Curved Delta Vortex Generator – [All angle comparison]

Analyzingthecommonflowdownperformanceof theCurvedDeltaVortexGeneratorintheramped expansion channel resulted in the following outcomes.

Fig.9. FrictionfactorvsReynoldsnumber

Fig.10. NusseltnumbervsReynoldsnumber

International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056

Volume: 11 Issue: 03 | Mar 2024 www.irjet.net p-ISSN: 2395-0072

Both the above graphs, (Fig.9.) and (Fig.10.) implies that the attack angle 300 shows the better thermohydraulic performance factor with greater heat transmissionrateandlowerpressurelosscomparedtoall other attack angles being positioned in the common flow downconfiguration.

2.0

Table.3. DataobtainedforAttackangle300 inCFD

7. CONCLUSIONS

Hydro-thermalcharacteristicsoftherampedexpansion channelinunderprocess.Furtherthechannelwithacurved delta winglet vortex generator is made using Curable Aluminafilamentandplacedinthechannel.BothCommon flowupandCommonflowdownconfigurationswithvarying angles of attacks are experimented with. The overall performance of the vortex generator is evaluated with Nu numberandFrictionfactor.Thebelowlistedconfiguration showsthegreaterperformancecharacteristicsintheramped expansionchannelusingCurvedDeltaVortexGenerator.

guidance,andalsoforprovidingusallthenecessaryfacilities required for carrying out this project work. We are very grateful to our respected Head of the Department, MechanicalEngineering, Dr.C.Velmurugan forhisconstant and continuous motivation, review, and cooperation throughout this project work. We wish to record our profound happiness and gratitude to our Project Coordinator Dr. K. M. Senthilkumar, DR. K. Krishnamoorthi, DR. S. Sivakumar andProjectGuide Mr. S. Sivakumar for their constant and continuous effort, guidance,andvaluabletime.Oursincereandheartythanksto allthefacultymembersandstaffofMechanicalEngineering Departmentfortheirwellwishes,timelyhelpandsupport rendered to us for doing this final year design and fabricationprojectwork.Weareverygreatlyindebtedtoour family,relativesandourallfriendswithoutwhomourlife wouldnothavebeenshapedtothislevel.

REFERENCES

[1] Esmaeilzadeh,N.Amanifard,andH.M.Deylami,“In ordertomaximizeflowcharacteristicsandenhance heattransferinaheatexchanger,acomparisonof straightandcurvedtrapezoidallongitudinalvortex generatorswasconducted,” Appl. Therm. Eng.,vol. 125,pp.1414–1425,2017.

[2] Armaly, B., Durst, F., Pereira, J., & Schönung, B. Experimental and theoretical investigation of backward-facing step flow. Journal of Fluid Mechanics,127, 473-496. doi:10.1017/S0022112083002839

[3] W.Hu,L.Wang,Y.Guan,andW.Hu,“Theimpactof wingletvortexgeneratorshapeona circulartube bank fin heat exchanger's thermal-hydrodynamic performance,” Heat Mass Transf. und Stoffuebertragung, vol. 53, no. 9, pp. 2961–2973, 2017.

[4] M.F.MdSalleh,H.A.Mohammed,andM.A.Wahid, “Thermal and hydraulic characteristics of trapezoidal winglet across fin-and-tube heat exchanger(FTHE),” Appl. Therm. Eng.,vol.149,no. November2018,pp.1379–1393,2019.

Table.4 Endresultoftheaboveexperimentalstudy

ACKNOWLEDGEMENT

We wholeheartedly thank our Chairman Dr. B. K Krishnaraj Vanavarayar, our Correspondent Thiru. M.Balasubramanium, our Joint Correspondent Thiru. Shankar Vanavarayar, our advisor Dr. V. Manivel muralidaran for providing us with the required infrastructure at Kumaraguru College of Technology. We express our gratitude to our beloved Principal Dr. D. Saravanan, for his invaluable support, motivation, and

[5] S. K. Sarangi, D. P. Mishra, H. Ramachandran, N. Anand, V. Masih, and L. S. Brar, “Examining and refining the small heat exchanger's curved trapezoidal winglet geometry,” Appl. Therm. Eng., vol.182,no.September2020,p.116088,2021.

[6] J. Carpio and A. Valencia, “Enhancement of heat transferusinglongitudinalvortexgeneratorsinflattubecompactheatexchangers,” Int. Commun. Heat MassTransf.,vol.120,no.xxxx,p.105035,2021.

International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056

Volume: 11 Issue: 03 | Mar 2024 www.irjet.net p-ISSN: 2395-0072

[7] Tsay,YL.,Chang,T.&Cheng,J.Enhancementofheat transferforbackward-facingstepflowinachannel with the placement of baffles on the channel wall. Acta Mechanica 174, 63–76 (2005). https://doi.org/10.1007/s00707-004-0147-5

[8] Abbott,D.E.,andKline,S.J.(September1,1962)." ExaminingSubsonicTurbulentFlowThroughSingle andDoubleBackwardFacingStepsExperimentally." ASME. J. Basic Eng. September 1962; 84(3): 317–325.https://doi.org/10.1115/1.3657313

[9] Kanna,P.R.,andDas,M.K.(January25,2006)."A two-dimensional LaminarInflexible Wall JetFlow Under Backward-Facing Step: A Numerical Simulation."ASME. J. Fluids Eng.September2006; 128(5): 1023–1035.https://doi.org/10.1115/1.2243298

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