THE SECOND LAW OF THERMODYNAMICS
PROPRIETARY AND CONFIDENTIAL
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Second Law of Thermodynamics and Thermal Energy Reservoirs
7-1C Transferring5 kWh of heat to an electric resistance wire and producing 6 kWh of electricity
7-2C Transferring5 kWh of heat to an electric resistance wire and producing 5 kWh of electricity
7-3C An electric resistance heater which consumes 5 kWh of electricityand supplies 6 kWh of heat to a room.
7-4C No. Heat cannot flow from a low-temperature medium to a higher temperature medium.
7-5C A thermal-energyreservoir is a body that can supply or absorb finite quantities of heat isothermally. Some examples are the oceans, the lakes, and the atmosphere.
7-6C Yes. Because the temperature of the oven remains constant no matter how much heat is transferred to the potatoes.
Heat Engines and Thermal Efficiency
7-7C Heat engines are cyclic devices that receive heat from a source, convert some of it to work, and reject the rest to a sink.
7-8C It is expressed as "No heat engine can exchange heat with a single reservoir, and produce an equivalent amount of work"
7-9C No. Such an engine violates the Kelvin-Planckstatement of the second law of thermodynamics.
7-10C No. Because 100% of the work can be converted to heat.
7-11C (a) No, (b) Yes. According to the second law, no heat engine can have and efficiencyof 100%.
7-12C No. Such an engine violates the Kelvin-Planck statement of the second law of thermodynamics.
7-13C No. The Kelvin-Plank limitation applies only to heat engines; engines that receive heat and convert some of it to work
7-14C Method (b). With the heating element in the water, heat losses to the surrounding air are minimized, and thus the desired heating can be achieved with less electrical energy input.
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7-2
7-15 The rates of heat supply and heat rejection of a power plant are given The power output and the thermal efficiency of this power plant are to be determined
Assumptions 1 The plant operates steadily 2 Heat losses from the working fluid at the pipes and other components are taken into consideration.
Analysis (a) The total heat rejected by this power plant is
Q L = 145+ 8 = 153GJ/h
Then the net power output of the plant becomes
W net,out = Q H Q L = 280 153 = 127 GJ/h = 35.3
(b) The thermal efficiency of the plant is determined from its definition, sink
net,out 127 GJ/h
= = = 0.454 = 45.4% th Q 280 GJ/h
Q H = 280GJ/h
7-16E The power output and thermal efficiencyof a car engine are given The rate of fuel consumptionis to be determined
Assumptions The car operates steadily.
Properties The heating value of the fuel is given to be 19,000 Btu/lbm.
Analysis This car engine is converting 28% of the chemical energy released during the combustion process into work The amount of energy input required to produce a power output of 110 hp is determined from the definition of thermal efficiency to be
To supply energy at this rate, the engine must burn fuel at a rate of
since 19,000 Btu of thermal energy is released for each lbm of fuel burned.
7-17E The rate of heat input and thermal efficiencyof a heat engine are given. The power output of the heat engine is to be determined
Assumptions 1 The plant operates steadily. 2 Heat losses from the working fluid at the pipes and other componentsare negligible.
Analysis Applying the definition of the thermal efficiency to the heat engine,
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7-3
) H H
Furnace
HE
MW
Q L W
W net,out 110 hp 2545 Btu/h Q = = = 999,598 Btu/h Fuel Engine th 0 28 1hp 110 hp
m =
52.6 lbm/h 19,000Btu/lbm
19,000 Btu/lbm HE sink 28%
999,598Btu/h
=
W net = thQ H 3104 Source Btu/h HE th = 40% W net = (0.4)(3104 Btu/h 1hp
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7-18 The power output and thermal efficiencyof a heat engine are given The rate of heat input is to be determined
Assumptions 1 The plant operates steadily. 2 Heat losses from the working fluid at the pipes and other componentsare negligible.
Analysis Applying the definition of the thermal efficiency to the heat engine,
th = 35% W net 60hp 0 7457kJ/s
60 hp QH = th = 0.35 1hp = 128 kJ/s
7-19 The power output and thermal efficiencyof a power plant are given. The rate of heat rejection is to be determined, and the result is to be compared to the actual case in practice.
Assumptions 1 The plant operates steadily 2 Heat losses from the working fluid at the pipes and other components are negligible.
Analysis The rate of heat supply to the power plant is determined from the thermal efficiencyrelation,
Q H W net,out 600 MW = = = 1500MW
th 0.4
The rate of heat transfer to the river water is determined from the first law relation for a heat engine,
Q L = Q H W net,out = 1500 600 = 900 MW
In reality the amount of heat rejected to the river will be lower since part of the heat will be lost to the surroundingair from the working fluid as it passes through the pipes and other components
7-20 The work output and heat input of a heat engine are given The heat rejection is to be determined
Assumptions 1 The plant operates steadily 2 Heat losses from the working fluid at the pipes and other componentsare negligible.
Analysis Applying the first law to the heat engine gives QL = QH Wnet = 700kJ 250kJ = 450 kJ
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7-5
Source Q
HE
Sink
H
Furnace
HE sink
th = 40% 600 MW
Furnace Q
HE QL
sink
H
Wnet
7-21 The heat rejection and thermal efficiencyof a heat engine are given The heat input to the engine is to be determined
Assumptions 1 The plant operates steadily. 2 Heat losses from the working fluid at the pipes and other componentsare negligible.
Analysis According to the definition of the thermal efficiency as applied to the heat engine,
wnet = thqH
qH qL = thqH which when rearranged gives
q = qL = 500kJ/kg = 909 kJ/kg 1 th 1 0.45
7-22 The power output and fuel consumptionrate of a power plant are given The thermal efficiency is to be determined
Assumptions The plant operates steadily.
Properties The heating value of coal is given to be 30,000 kJ/kg.
Analysis The rate of heat supply to this power plant is
Q H = m coal qHV,coal = (60,000kg/h)(30,000kJ/kg) = 1.8109 kJ/h = 500 MW
Then the thermal efficiencyof the plant becomes
W net,out 150 MW
= = = 0 300 = 30.0% th Q 500 MW
7-23 The power output and fuel consumptionrate of a car engine are given The thermal efficiency of the engine is to be determined.
Assumptions The car operates steadily.
Properties The heating value of the fuel is given to be 44,000 kJ/kg
Analysis The mass consumptionrate of the fuel is
m fuel = (V )fuel = (0 8 kg/L)(22 L/h) =176 kg/h
The rate of heat supply to the car is
Q H = m coal
qHV,coal
= (17.6 kg/h)(44,000kJ/kg)
= 774,400kJ/h = 215.1kW
Then the thermal efficiencyof the car becomes
W net,out 55 kW
= = = 0 256 = 25.6% th Q 215.1kW
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H H H
Furnace qH HE qL sink wnet
60 t/h coal Furnace HE sink 150
MW
Fuel 22 L/h Engine HE sink 55 kW
7-24 The United States produces about 51 percent of its electricityfrom coal at a conversion efficiencyof about 34 percent. The amount of heat rejected by the coal-fired power plants per year is to be determined
Analysis Noting that the conversion efficiency is 34%, the amount of heat rejected by the coal plants per year
7-25E The power output and thermal efficiencyof a solar pond power plant are given The rate of solar energy collection is to be determined.
Assumptions The plant operates steadily.
Analysis The rate of solar energy collection or the rate of heat supply to the power plant is determined from the thermal efficiency relation to be
7-26 A coal-burningpower plant produces 300 MW of power. The amount of coal consumed during a one-day period and the rate of air flowing through the furnace are to be determined.
Assumptions 1 The power plant operates steadily 2 The kinetic and potential energy changes are zero
Properties The heating value of the coal is given to be 28,000 kJ/kg
(a) The rate and the amount of heat inputs to the power plant are
The amount and rate of coal consumed during this period are
= 33 48kg/s
(b) Noting that the air-fuel ratio is 12, the rate of air flowing through the furnace is
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W W th = coal = coal Coal Qin W Qout + Wcoal Furnace Qout = coal Wcoal th 1.8781012 kWh 12 = 1.87810 kWh 0.34 = 3.646 1012 kWh Q out HE sink 1 8781012 kWh ηth = 34%
is
Source 180 kW W net,out 180 kW 1Btu 3600s Solar pond HE QH = = = 2.05 107Btu/h th 0.03 1.055 kJ 1h 3% sink
Analysis
Q in = W net ,out = th 300MW 0.32
Qin = Q in t = (937.5 MJ/s)(24 3600s)
8.1107 MJ
= 937.5MW
=
mcoal = Qin = qHV 8.1107 MJ 28MJ/kg = 2.893
kg m 2.893
m = coal =
coal t 24
106
106 kg
3600s
7-8 PROPRIETARY MATERIAL © 2017 McGraw-Hill Education Limited distribution permitted only to teachers and educators for course preparation If you are a student using this Manual, you are using it without permission m air = (AF)m coal = (12kg air/kgfuel)(33 48kg/s) = 401.8 kg/s
7-27E An OTEC power plant operates between the temperature limits of 86F and 41F. The cooling water experiences a temperature rise of 6F in the condenser The amount of power that can be generated by this OTEC plans is to be determined.
Assumptions 1 Steady operating conditions exist. 2 Water is an incompressiblesubstance with constant properties.
Properties The density and specific heat of water are taken = 64.0 lbm/ft3 and c = 1.0 Btu/lbm.F, respectively.
= V water
= (64.0lbm/ft3)(13,300gal/min) 1ft =113,790lbm/min =1897lbm/s
7 4804gal
The rate of heat rejection to the cooling water is Q out = m waterC(Tout Tin ) = (1897lbm/s)(1 0Btu/lbm F)(6F) =
11,380Btu/s
Noting that the thermal efficiencyof this plant is 2 5%, the power generation is determined to be
= W = W → 0 025= W → W = 292Btu/s = 308 kW Q in W + Q out
since 1 kW = 0.9478 Btu/s.
W + (11,380 Btu/s)
Refrigerators and Heat Pumps
7-28C The difference between the two devices is one of purpose. The purpose of a refrigerator is to remove heat from a cold medium whereas the purpose of a heat pump is to supply heat to a warm medium
7-29C The difference between the two devices is one of purpose. The purpose of a refrigerator is to remove heat from a refrigerated space whereas the purpose of an air-conditioneris remove heat from a living space.
7-30C No. Because the refrigerator consumes work to accomplish this task.
7-31C No. Because the heat pump consumes work to accomplish this task.
7-32C The coefficientof performance of a refrigerator represents the amount of heat removed from the refrigerated space for each unit of work supplied It can be greater than unity
7-33C The coefficientof performance of a heat pump represents the amount of heat supplied to the heated space for each unit of work supplied It can be greater than unity
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7-9
Analysis The mass flow rate of the cooling water is
3 m water
7-34C No. The heat pump captures energy from a cold mediumand carries it to a warm medium. It does not create it.
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7-10
7-35C No The refrigerator captures energy from a cold mediumand carries it to a warm medium It does not create it.
7-36C No device can transfer heat from a cold medium to a warm medium without requiring a heat or work input from the surroundings
7-37C The violation of one statement leads to the violation of the other one, as shown in Sec. 7-4, and thus we conclude that the two statements are equivalent.
7-38 The heat removal rate of a refrigerator per kW of power it consumes is given. The COP and the rate of heat rejection are to be determined.
Assumptions The refrigerator operates steadily.
Analysis The coefficient of performance of the refrigerator is determined from its definition, Kitchen air
The rate of heat rejection to the surrounding air, per kW of power consumed, is determined from the energy balance,
= Q
+ W net,in = (5040kJ/h) + (1 3600 kJ/h) = 8640kJ/h
7-39 The rate of heat supply of a heat pump per kW of power it consumes is given The COP and the rate of heat absorption from the cold environment are to be determined
Assumptions The heat pump operates steadily Analysis The coefficient of performance of the refrigerator is determined from its definition,
= 2.22
The rate of heat absorption from the surrounding air, per kW of power consumed, is determined from the energy balance,
= Q H W net,in = (8,000kJ/h) (1)(3600kJ/h) = 4400 kJ/h
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7-11
Q L 5040kJ/h 1kW R COPR = = =
1 kW W net,in 1kW 3600kJ/h 5040 kJ/h
1.4
Refrigerator
Q H
L
Q H 8000kJ/h
House COPHP
8000 kJ/h W net,in 1kW 3600kJ/h HP
1kW
= =
Outside 1 kW
Q L
7-40E The COP and the power input of a residential heat pump are given The rate of heating effect is to be determined
Assumptions The heat pump operates steadily
Analysis Applying the definition of the heat pump coefficient of performance to this heat pump gives
7-41 The power input and the COP of a refrigerator are given The cooling effect of the refrigerator is to be determined
Assumptions The refrigerator operates steadily.
Analysis Rearrangingthe definition of the refrigerator coefficient of
performance and applying the result to this refrigerator gives
= (18)(12 kW) = 2.16 kW
7-42 The power consumptionand the cooling rate of an air conditioner are given. The COP and the rate of heat rejection are to be determined
Assumptions The air conditioner operates steadily Analysis (a) The coefficient of performance of the air-conditioner (or refrigerator) is determined from its definition,
b) The rate of heat discharge to the outside air is determined from the energy balance,
= (750 kJ/min) + (6 60 kJ/min) = 1110
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7-12
2544
Reservoir Q H HP 5 hp Q H = COPHPW net,in = (2.4)(5hp) 1hp = 30,530 Btu/h COP = 2.4 Reservoir
5Btu/h
Q L = COPR
net,in
Q H R Q L COP=1.8 W net,in Reservoir
Reservoir
W
Outdoors Q L 750 kJ/min 1kW 6 kW COPR = W = 6 kW = 2.08 60 kJ/min A/C net,in Q L = 750kJ/min
H
Q L
House
Q
=
+ W net,in
kJ/min
7-43 A refrigerator is used to keep a food department at a specified temperature. The heat gain to the food department and the heat rejection in the condenser are given The power input and the COP are to be determined
Assumptions The refrigerator operates steadily
Analysis The power input is determined from
The COP is
7-44 The COP and the power consumptionof a refrigerator are given The time it will take to cool 5 watermelons is to be determined
Assumptions 1 The refrigerator operates steadily 2 The heat gain of the refrigerator through its walls, door, etc. is negligible. 3 The watermelons are the only items in the refrigerator to be cooled.
Properties The specific heat of watermelons is given to be c = 4.2 kJ/kg C
Analysis The total amount of heat that needs to be removed from the watermelons is
That is, this refrigerator can remove 0 675 kJ of heat per second Thus the time required to remove 4200 kJ of heat is
= 104 min
This answer is optimistic since the refrigerated space will gain some heat during this process from the surroundingair, which will increase the work load Thus, in reality, it will take longer to cool the watermelons
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7-13
W in = Q H Q L 30C = 4800 3300 = 1500kJ/h Q H 4800 kJ/h = (1500kJ/h) 1kW = 0.417 kW R W in
3600kJ/h Q L 3300 kJ/h COP = Q L = 3300kJ/h = 2 2 12C W in 1500kJ/h
QL = (mcT )watermelons = 5 (10 kg)(4 2 kJ/kg C)(28 8)C = 4200 kJ
rate at which
refrigerator
is Q L = (COPR )(W net,in )= (1 5)(0 45 kW) = 0.675 kW Kitchen air 450 W
The
this
removes heat
t = QL = 4200kJ
6222s
R COP = 1.5 cool space Q L 0.675kJ/s
=
7-45E The rate of heat supply and the COP of a heat pump are given The power consumption and the rate of heat absorption from the outside air are to be determined
Assumptions The heat pump operates steadily
Analysis (a) The power consumed by this heat pump can be determined from the definition of the coefficient of performance of a heat pump to be
(b) The rate of heat transfer from the outdoor air is determined from the conservationof energy principle,
L = Q H W net,in = (60,000 24,000)Btu/h = 36,000Btu/h
7-46 A refrigerator is used to cool bananas to a specified temperature. The power input is given. The rate of cooling and the COP are to be determined
Assumptions The refrigerator operates steadily
Properties The specific heat of banana is 3 35 kJ/kg C.
Analysis The rate of cooling is determined from
L = m c p (T1 T2 ) = (215/ 60 kg/min)(3.35kJ/kg C)(24 13) C = 132 kJ/min The COP is
7-47 The rate of heat loss, the rate of internal heat gain, and the COP of a heat pump are given The power input to the heat pump is to be determined
Assumptions The heat pump operates steadily.
Analysis The heating load of this heat pump system is the difference between the heat lost to the outdoors and the heat generated in the house from the people, lights, and appliances,
Q H = 85,000 4000 = 81,000kJ/h
Using the definition of COP, the power input to the heat pump is determined to be
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7-14
House
W
hp Q H COP
60,000 Btu/h
net,i n = Q H = 60,000 Btu/h = 24,000 Btu/h = 9.43
HP 2 5 HP
Q
Outside COP
= 2.5
Q
W
COP = Q L = (132/60)kW = 1.57
in 1.4kW
House Q H HP 85,000
W Q H 81,000kJ/h 1kW COP = 3.2 net,in = COP = 3 2 = 7.03 kW 3600kJ/h Outside HP
kJ/h
7-48E The COP and the refrigerationrate of an ice machine are given The power consumptionis to be determined
Assumptions The ice machine operates steadily.
Analysis The cooling load of this ice machine is
L = m qL = (28lbm/h)(169Btu/lbm) = 4732 Btu/h
Using the definition of the coefficient of performance, the power input to the ice machine system is determined to be
7-49 The COP and the refrigeration rate of a refrigerator are given. The power consumption of the refrigerator is to be determined.
Assumptions The refrigerator operates steadily.
Analysis Since the refrigerator runs one-fourth of the time and removes heat from the food compartment at an average rate of 800 kJ/h, the refrigerator removes heat at a rate of
L = 4 (800 kJ/h) = 3200 kJ/h
when running Thus the power the refrigerator draws when it is running is
= 2.2
7-50 The rate of heat loss from a house and the COP of the heat pump are given The power consumption of the heat pump when it is running is to be determined.
Assumptions The heat pump operates one-third of the time.
Analysis Since the heat pump runs one-third of the time and must supply heat to the house at an average rate of 22,000 kJ/h, the heat pump supplies heat at a rate of
Q H = 3 (22,000 kJ/h) = 66,000 kJ/h
when running Thus the power the heat pump draws when it is running is
COP = 2.8 W
66,000kJ/h 1kW
2.8 = 6.55 kW 3600kJ/h
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7-15
Q
Outdoors COP =
R Q L W Q
net,in
COP
water Ice ice R 55°F Machine
2.4
L 4732 Btu/h 1hp
= =
2.4 = 0.775 hp 2545Btu/h
25°F
Kitchen air R COP
Q
800
Refrigerator W net,i n
Q
COPR
kJ/h
=
L = 3200 kJ/h = 1455 kJ/h = 0.40 kW
2.2
House Q H 22,000
kJ/h
HP
Q
Outside net,in
COP
HP
H
= =
7-51E An office that is being cooled adequatelyby a 12,000 Btu/h window air-conditioneris converted to a computer room
The number of additional air-conditionersthat need to be installed is to be determined
Assumptions 1 The computers are operated by 7 adult men 2 The computers consume 40 percent of their rated power at any given time.
Properties The average rate of heat generation from a person seated in a room/office is 100 W (given)
Analysis The amount of heat dissipated by the computers is equal to the amount of electrical energy they consume. Therefore,
Q computers = (Rated power) (Usagefactor)= (8 4kW)(0 4)= 3 36kW
Q people = (No of people) Q person = 7 (100W) = 700W
Q total = Q computers + Q people = 3360 + 700 = 4060W =13,853Btu/h
since 1 W = 3 412 Btu/h Then noting that each available air conditioner provides 7000 Btu/h cooling, the number of air-conditionersneeded becomes
No of air conditioners = Coolingload = 13,853Btu/h
Coolingcapacityof A/C = 1.98 2 Air conditione rs 7000Btu/h
7000 Btu/h
7-52 A decision is to be made between a cheaper but inefficient air-conditionerand an expensive but efficient airconditioner for a building The better buy is to be determined
Assumptions The two air conditioners are comparable in all aspects other than the initial cost and the efficiency
Analysis The unit that will cost less during its lifetime is a better buy The total cost of a system during its lifetime (the initial, operation, maintenance, etc ) can be determined by performing a life cycle cost analysis A simpler alternative is to determine the simple payback period The energy and cost savings of the more efficient air conditioner in this case is
Energy savings = (Annual energyusage of A) (Annual energyusage of B)
= (Annual coolingload)(1/COPA 1/COPB )
= (40,000kWh/year)(1/2 3 1/3.6)
= 6280kWh/year
Costsavings = (Energy savings)(Unit costof energy) = (6280kWh/year)($0.10/kWh)= $628/year
The installation cost difference between the two air-conditionersis Cost difference = Cost of B – cost of A = 7000 – 5500 = $1500
Therefore, the more efficient air-conditionerB will pay for the $1500 cost differential in this case in about $1500/$628 = 2 39 years
Air Cond. A
COP = 2.3
Air Cond B
COP = 3.6
Discussion A cost conscious consumer will have no difficulty in deciding that the more expensive but more efficient airconditioner B is clearly the better buy in this case since air conditioners last at least 15 years But the decision would not be so easy if the unit cost of electricityat that location was much less than $0 10/kWh, or if the annual air-conditioningload of the house was much less than 40,000 kWh.
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7-16
Outside AC
Computer
room
(
7-53 Refrigerant-134aflows through the condenser of a residential heat pump unit. For a given compressor power consumptionthe COP of the heat pump and the rate of heat absorbed from the outside air are to be determined
Assumptions 1 The heat pump operates steadily. 2 The kinetic and potential energy changes are zero
Properties The enthalpies of R-134a at the condenser inlet and exit are
P1 = 800kPa
T1 = 35C
P2 = 800kPa h2 = 95.48 kJ/kg
x2 = 0
Analysis (a) An energy balance on the condenser gives the heat rejected in the condenser
Q H = m (h1 h2 ) = (0.018kg/s)(271.24 95.48) kJ/kg =
3 164kW
The COP of the heat pump is
COP = Q H = 3 164kW = 2.64
W in 1.2 kW
b) The rate of heat absorbed from the outside air
Q L = Q H W in = 3.164 1.2 = 1.96 kW
Reversible and Irreversible Processes
7-54C No Because it involves heat transfer through a finite temperature difference
7-55C This process is irreversible. As the block slides down the plane, two things happen, (a) the potential energy of the block decreases, and (b) the block and plane warm up because of the friction between them The potential energy that has been released can be stored in some form in the surroundings (e g., perhaps in a spring) When we restore the system to its original condition, we must (a) restore the potential energy by lifting the block back to its original elevation, and (b) cool the block and plane back to their original temperatures.
The potential energy may be restored by returning the energy that was stored during the original process as the block decreased its elevation and released potential energy The portion of the surroundings in which this energy had been stored would then return to its original condition as the elevation of the block is restored to its original condition
In order to cool the block and plane to their original temperatures, we have to remove heat from the block and plane. When this heat is transferred to the surroundings, something in the surroundings has to change its state (e g., perhaps we warm up some water in the surroundings). This change in the surroundings is permanent and cannot be undone. Hence, the original process is irreversible.
7-56C The chemical reactions of combustion processes of a natural gas and air mixture will generate carbon dioxide, water, and other compounds and will release heat energy to a lower temperature surroundings. It is unlikely that the surroundings will return this energy to the reacting system and the products of combustion react spontaneously to reproduce the natural gas and air mixture
7-17
preparation If
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800 kPa x=0 QH Condenser 800 kPa 35C
Expansion
Win
valve
Compressor
Evaporator QL
7-57C Adiabatic stirring processes are irreversible because the energy stored within the system can not be spontaneously released in a manor to cause the mass of the system to turn the paddle wheel in the opposite direction to do work on the surroundings.
7-58C When the compression process is non-quasi equilibrium, the molecules before the piston face cannot escape fast enough, forming a high pressure region in front of the piston It takes more work to move the piston against this high pressure region.
7-59C When an expansion process is non-quasiequilibrium,the molecules before the piston face cannot follow the piston fast enough, forming a low pressure region behind the piston The lower pressure that pushes the piston produces less work
7-60C The irreversibilitiesthat occur within the system boundaries are internal irreversibilities;those which occur outside the system boundaries are external irreversibilities
7-61C A reversible expansion or compressionprocess cannot involve unrestrained expansion or sudden compression, and thus it is quasi-equilibrium A quasi-equilibriumexpansion or compressionprocess, on the other hand, may involve external irreversibilities(such as heat transfer through a finite temperature difference), and thus is not necessarilyreversible.
7-62C Because reversible processes can be approached in reality, and they form the limiting cases. Work producing devices that operate on reversible processes deliver the most work, and work consuming devices that operate on reversible processes consume the least work.
The Carnot Cycle and Carnot's Principle
7-63C The four processes that make up the Carnot cycle are isothermal expansion, reversible adiabatic expansion, isothermal compression, and reversible adiabatic compression
7-64C They are (1) the thermal efficiency of an irreversible heat engine is lower than the efficiency of a reversible heat engine operating between the same two reservoirs, and (2) the thermal efficiency of all the reversible heat engines operating between the same two reservoirs are equal.
7-65C (a) No, (b) No They would violate the Carnot principle.
7-66C False. The second Carnot principle states that no heat engine cycle can have a higher thermal efficiency than the Carnot cycle operating between the same temperature limits.
7-67C Yes. The second Carnot principle states that all reversible heat engine cycles operating between the same temperature limits have the same thermal efficiency.
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7-18
Carnot Heat Engines
7-68C No.
7-69C The one that has a source temperature of 600°C. This is true because the higher the temperature at which heat is supplied to the working fluid of a heat engine, the higher the thermal efficiency
7-70 Two pairs of thermal energy reservoirs are to be compared from a work-productionperspective.
Assumptions The heat engine operates steadily.
Analysis For the maximum production of work, a heat engine operating between the energy reservoirs would have to be completelyreversible. Then, for the first pair of reservoirs
= 1 = 1 = 0.519
For the second pair of reservoirs,
275K
= 1 = 1 = 0 560
The second pair is then capable of producing more work for each unit of heat extracted from the hot reservoir.
7-71E The sink temperature of a Carnot heat engine, the rate of heat rejection, and the thermal efficiency are given The power output of the engine and the source temperature are to be determined.
Assumptions The Carnot heat engine operates steadily.
Analysis (a) The rate of heat input to this heat engine is determined from the definition of thermal efficiency,
Then the power output of this heat engine can be determined from
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7-19
L L QH T T
TH
th,max
HE
T 325K
H 675K
QL Wnet T
T th,max
L
H
625K
th = 1 Q L → 0 55 = 1 800 Btu/min → Q H = 1777 8 Btu/min Q H Q H
TH W net,out = thQ H = (0.55)(1777.8Btu/min) = 977.8 Btu/min = 23.1 hp Q T H = H HE (b) For reversible cyclic devices we have Q L rev Thus the temperature of
TL 60°F 800 Btu/min Q T = H T = 1777.8 Btu/min (520 R) = 1155.6 R H Q L L rev 800 Btu/min
the source TH must be
(
7-72 The sink temperature of a Carnot heat engine and the rates of heat supply and heat rejection are given The source temperature and the thermal efficiencyof the engine are to be determined
Assumptions The Carnot heat engine operates steadily
Analysis (a) For reversible cyclic devices we have
Thus the temperature of the source TH must be
b) The thermal efficiency of a Carnot heat engine depends on the source and the sink temperatures only, and is determined from
7-73 The source and sink temperatures of a Carnot heat engine and the rate of heat supply are given. The thermal efficiency and the power output are to be determined
Assumptions The Carnot heat engine operates steadily.
Analysis (a) The thermal efficiency of a Carnot heat engine depends on the source and the sink temperatures only, and is determined from
(b) The power output of this heat engine is determined from the definition of thermal efficiency,
7-74 The source and sink temperatures of a heat engine and the rate of heat supply are given. The maximumpossible power output of this engine is to be determined
Assumptions The heat engine operates steadily.
Analysis The highest thermal efficiency a heat engine operating between two specified temperature limits can have is the Carnot efficiency, which is determined from
1
K = 0.600 or 60.0%
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7-20
T T T
Q T source H = H 650 kJ
QL rev TL HE 250 kJ Q 650
H TH = Q TL = (297 K) = 772.2 K 250 kJ 24°C L rev
kJ
= 1 TL = 1 297 K = 0.615
th,C H 772.2 K
or 61.5%
1000 K = 1 TL = 1 300 K = 0 70 or 70% 800 kJ/min th,C H 1000K HE
W net,out = thQ H = (0 70)(800 kJ/min)
560 kJ/min
kW 300 K
=
= 9.33
477°C 65,000 kJ/min = = 1 TL
th,max th,C H (477
K HE
=
298
+ 273)
Then the maximum power output of this heat engine is determined from the definition of thermal efficiency to be
W net,out =thQ H = (0 600)(65,000kJ/min) = 39,000 kJ/min = 653 kW
25°C
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7-21
7-75 Problem 7-74 is reconsidered The effects of the temperatures of the heat source and the heat sink on the power produced and the cycle thermal efficiency as the source temperature varies from 300°C to 1000°C and the sink temperature varies from 0°C to 50°C are to be studied. The power produced and the cycle efficiency against the source temperature for sink temperatures of 0°C, 25°C, and 50°C are to be plotted
Analysis The problem is solved using EES, and the results are tabulated and plotted below
T_H = 477 [C]
T_L =25 [C]
Q dot H = 65000 [kJ/min]
"First Law applied to the heat engine"
Q dot H - Q dot_L- W dot net = 0
W dot_net KW=W dot net*convert(kJ/min,kW)
"Cycle Thermal Efficiency - Temperatures must be absolute"
eta th = 1 - (T_L + 273)/(T_H + 273)
"Definition of cycle efficiency"
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7-22
TH [C] WnetkW [kW] th 300 567 2 0.5236 400 643.9 0.5944 500 700 7 0.6468 600 744.6 0.6873 700 779 4 0.7194 800 807.7 0.7456 900 831 2 0.7673 1000 851 0.7855 TL=0°C TL=25°C TL=50°C t h W n e t [ k W ]
eta th=W dot net / Q_dot_H 850 800 750 700 650 600 Values for TL = 0C 550 500 0 8 450 300 400 500 600 700 800 900 1000 TH [C] 0 75 0 7 0 65 0 6 TL=0°C TL=50°C TL=25°C 0 55 0 5 0 45 0.4 300 400 500 600 700 800 900 1000 TH [C]
7-76E The claim of an inventor about the operation of a heat engine is to be evaluated
Assumptions The heat engine operates steadily.
Analysis If this engine were completelyreversible, the thermal efficiency would be
When the first law is applied to the engine above,
The actual thermal efficiency of the proposed heat engine is then
Since the thermal efficiency of the proposed heat engine is smaller than that of a completely reversible heat engine which uses the same isothermal energy reservoirs, the inventor's claim is valid (but not probable with these values)
7-77 The work output and thermal efficiency of a Carnot heat engine are given. The heat supplied to the heat engine, the heat rejected and the temperature of heat sink are to be determined
Assumptions 1 The heat engine operates steadily 2 Heat losses from the working fluid at the pipes and other components are negligible.
Analysis Applying the definition of the thermal efficiency and an energy balance to the heat engine, the unknown values are determined as follows:
7-78 The source and sink temperatures of an OTEC (Ocean Thermal Energy Conversion) power plant are given. The maximum thermal efficiencyis to be determined
Assumptions The power plant operates steadily
Analysis The highest thermal efficiency a heat engine operating between two specified temperature limits can have is the Carnot efficiency, which is determined from
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7-23
T H L T
920 R Q H
th,max H 920R HE 4.5 hp
= 1 TL = 1 490R = 0.467
15,000 Btu/h 490 R Q
W
H net
=
+ Q = (4.5hp) 2544 5Btu/h + 15,000Btu/h = 26,450Btu/h
L 1hp
W net 4 5hp
th
Q H
=
2544 5Btu/h
0.433
=
=
26,450Btu/h
1hp
1200°C QH HE th = 40% 500 kJ Q = Wnet = 500kJ = 1250 kJ Q th 0 4 sink QL = QH Wnet = 1250 500 = 750 kJ T T th,max = 1 L → 0 40 = 1 L →TL = 8838 K = 611C TH (1200 + 273) K
24C HE W = = 1 TL = 1 276 K = 0.071 or 7.1% th,max th,C H 297 K 3C
7-79 The source and sink temperatures of a geothermal power plant are given The maximum thermal efficiency is to be determined
Assumptions The power plant operates steadily
Analysis The highest thermal efficiency a heat engine operating between two specified temperature limits can have is the Carnot efficiency, which is determined from
= = 1 TL = 1 20 +273 K = 0 291 or 29.1%
th,max th,C H 140 + 273 K
Carnot Refrigerators and Heat Pumps
7-80C The difference between the temperature limits is typically much higher for a refrigerator than it is for an air conditioner The smaller the difference between the temperature limits a refrigerator operates on, the higher is the COP Therefore, an air-conditionershould have a higher COP
7-81C The deep freezer should have a lower COP since it operates at a much lower temperature, and in a given environment, the COP decreases with decreasing refrigerationtemperature.
7-82C By increasing TL or by decreasing TH.
7-83C No. At best (when everythingis reversible), the increase in the work produced will be equal to the work consumed by the refrigerator In reality, the work consumed by the refrigerator will always be greater than the additional work produced, resulting in a decrease in the thermal efficiency of the power plant.
7-84C No At best (when everythingis reversible), the increase in the work produced will be equal to the work consumed by the refrigerator In reality, the work consumed by the refrigerator will always be greater than the additional work produced, resulting in a decrease in the thermal efficiency of the power plant.
7-85C Bad idea At best (when everything is reversible), the increase in the work produced will be equal to the work consumed by the heat pump. In reality, the work consumed by the heat pump will always be greater than the additional work produced, resulting in a decrease in the thermal efficiency of the power plant.
7-24 PROPRIETARY MATERIAL
McGraw-Hill Education Limited distribution permitted only to teachers and educators for course preparation If
are a student using this Manual,
are using it without permission T
© 2017
you
you
140C HE W
20C
7-86 An experimentalist claims to have developed a refrigerator The experimentalist reports temperature, heat transfer, and work input measurements The claim is to be evaluated
Analysis The highest coefficient of performance a refrigerator can have when removing heat from a cool medium at -30°C to a warmer medium at 25°C is
The work consumed by the actual refrigerator during this experiment is
Then the coefficient of performance of this refrigerator becomes
which is above the maximum value. Therefore, these measurementsare not reasonable
7-87 The refrigerated space and the environment temperatures of a Carnot refrigerator and the power consumption are given The rate of heat removal from the refrigerated space is to be determined
Assumptions The Carnot refrigerator operates steadily. Analysis The coefficient of performance of a Carnot refrigerator depends on the temperature limits in the cycle only, and is determined from
The rate of heat removal from the refrigerated space is determined from the definition of the coefficient of performance of a refrigerator,
7-88 The cooled space and the outdoors temperatures for a Carnot air-conditioner and the rate of heat removal from the airconditioned room are given. The power input required is to be determined.
Assumptions The air-conditioneroperates steadily.
Analysis The COP of a Carnot air conditioner (or Carnot refrigerator) depends on the temperature limits in the cycle only, and is determined from
The power input to this refrigerator is determined from the definition of the coefficient of performance of a refrigerator,
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7-25
COP = COP = 1
1 = R,max R,rev (TH /TL ) 1 (25 + 273 K)/( 30 + 273 K) 1 4 42 25C
=
Wnet,in
W net,int
2 kJ/s
s)
2400 kJ
=
= (
)(20
60
=
R 2 kW 30,000 kJ COPR = QL = 30,000kJ = 12.5 -30C Wnet,in 2400kJ
22C COP = 1 = 1 = R,C (TH /TL ) 1 (22 + 273K)/(3 + 273K) 1 14 5 R
Q L = COPRW net,in = (14 5)(2 kW) = 29 0 kW = 1740 kJ/min 3C 2 kW
COP = 1 = 1 = 35C R,C (TH /TL ) 1 (35 + 273 K)/(24 + 273 K) 1 27 0
House
7-26 PROPRIETARY MATERIAL © 2017 McGraw-Hill Education Limited distribution permitted only to teachers and educators for course preparation If you are a student using this Manual, you are using it without permission A/C W net,i n = Q L = 750 kJ/min = 278 kJ/min = 0.463 kW 24C COPR,max 27 0
7-89 The validity of a claim by an inventor related to the operation of a heat pump is to be evaluated
Assumptions The heat pump operates steadily.
Applying the definition of the heat pump coefficient of performance,
The maximum COP of a heat pump operating between the same temperature limits is
Since the actual COP is less than the maximum COP, the claim is valid.
7-90 The power input and the COP of a Carnot heat pump are given The temperature of the low-temperaturereservoir and the heating load are to be determined. Assumptions
7-91 The refrigerated space and the environmenttemperatures for a refrigerator and the rate of heat removal from the refrigerated space are given. The minimumpower input required is to be determined.
Assumptions The refrigerator operates steadily Analysis The power input to a refrigerator will be a minimum when the refrigerator operates in a reversible manner The coefficient of performance of a reversible refrigerator depends on the temperature limits in the cycle only, and is determined from
The power input to this refrigerator is determined from the definition of the coefficient of performance of a refrigerator,
7-27
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Analysis
COPHP Q 200kW = H =
2 67 293 K W net,in 75kW QH
=
HP Q L 75 kW COP = 1
1 = 14.7 HP,max 1 TL / TH 1 (273K)/(293K) 273 K
=
heat pump
Analysis The temperature of
low-temperature
24C COPHP,max = The heating load is TH TH TL →8.7 = 297K (297 TL ) K →TL = 263 K Q H HP Q L 2 15 kW COPHP,max = Q H W i n →8.7 = Q H 2.15kW → Q H = 18 7 kW TL
The
operates steadily
the
reservoir is
COP =
25C R,rev (TH / TL ) 1 (25 + 273K)/( 8 + 273K) 1 8
1 = 1 =
03
W net,in,mi n
R
300 kJ/min
= Q L = 300
kJ/min = 37 36
kJ/min = 0.623kW
COPR,max 8 03 -8C
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7-28
7-92 An inventor claims to have developed a refrigerator The inventor reports temperature and COP measurements The claim is to be evaluated
Analysis The highest coefficient of performance a refrigerator can have when removing heat from a cool mediumat -12°C to a warmer mediumat 25°C is
The COP claimed by the inventor is 6 5, which is below this maximumvalue, thus the claim is reasonable. However, it is not probable.
7-93 A heat pump maintains a house at a specified temperature. The rate of heat loss of the house and the power consumptionof the heat pump are given It is to be determined if this heat pump can do the job
Assumptions The heat pump operates steadily
Analysis The power input to a heat pump will be a minimum when the heat pump operates in a reversible manner The coefficient of performance of a reversible heat pump depends on the temperature limits in the cycle only, and is determined from
The required power input to this reversible heat pump is determined from the definition of the coefficient of performance to be
This heat pump is powerful enough since
7-94E The power required by a reversible refrigerator with specified reservoir temperatures is to be determined
Assumptions The refrigerator operates steadily.
Analysis The COP of this reversible refrigerator is
Using this result in the coefficient of performance expression yields
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7-29
L
25C COP = COP = 1 = 1 = R,max R,rev (TH /TL ) 1 (25 + 273 K)/( 12 + 273 K) 1 7 1 R
-12C COP= 6.5
COP = 1 = 1 = HP,rev 1 (TL / TH ) 1 (4 + 273K)/(25 + 273K) 14 19 110,000 kJ/h
House 25C W Q H 110,000kJ/h 1h net,in,min = COP = 14.19 = 2 15 kW 3600s HP 4 75 kW HP
4.75 kW > 2.15 kW.
540 R COP T
=
R,max TH TL 540R 450 R
450R
= = 5
R 15,000 Btu/h W . net,in Q 15,000Btu/h 1kW Wnet,in = L = = 0.879 kW COPR,max 5 3412.14Btu/h 450 R
7-95E The cooled space and the outdoors temperatures for an air-conditioner and the power consumption are given The maximum rate of heat removal from the air-conditioned space is to be determined
Assumptions The air-conditioneroperates steadily
Analysis The rate of heat removal from a house will be a maximum when the air-conditioning system operates in a reversible manner The coefficient of performance of a reversible air-conditioner (or refrigerator) depends on the temperature limits in the cycle only, and is determined from
The rate of heat removal from the house is determined from the definition of the coefficient of performance of a refrigerator,
7-96 The power input and heat rejection of a reversed Carnot cycle are given. The cooling load and the source temperature are to be determined
Assumptions The refrigerator operates steadily
Analysis Applying the definition of the refrigerator coefficient of performance,
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7-30
T T
COP = 1 = 1 = 90F R,rev (TH / TL ) 1 (90 + 460R)/(72 + 460R) 1 29 6
42 41Btu/min House 72F A/C 5 hp Q L = COPRW net,in = (29.6)(5 hp) 1hp = 6277 Btu/min
Q L = Q H W net,in
2000 200
1800 kW 300 K Applying the
of the
Q H 2000 kW R COPR = Q L = 1800kW = 9 200 kW W net,in 200kW Q L The temperature of the heat source is determined from TL COPR,max = L TH TL → 9 = L 300 TL → TL = 270K = 3C
=
=
definition
heat pump coefficient of performance,
(
7-97 A commercial refrigerator with R-134a as the working fluid is considered The condenser inlet and exit states are specified The mass flow rate of the refrigerant, the refrigeration load, the COP, and the minimum power input to the compressor are to be determined.
Assumptions 1 The refrigerator operates steadily 2 The kinetic and potential energy changes are zero
Properties The properties of R-134a and water are (Steam and R-134a tables)
P1 = 1.2MPa
h1 = 27828 kJ/kg
,1 = 75.54 kJ/kg
Analysis (a) The rate of heat transferred to the water is the
energy change of the water from inlet to exit
,1 ) = (025 kg/s)(10901 7554) kJ/kg = 8 367 kW
The energy decrease of the refrigerant is equal to the energy increase of the water in the condenser. That is,
(b) The refrigerationload is
3.30 = 5.07 kW
c) The COP of the refrigerator is determined from its definition,
= = 1.54
(d) The COP of a reversible refrigerator operating between the same temperature limits is
= 1 = 1 = 4.49
1 (18 + 273)/( 35 + 273) 1
Then, the minimum power input to the compressor for the same refrigerationload would be
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7-31
26C Water 18C
C 1.2 MPa QH 1.2 MPa
5 = 41 3C
2
MPa h
5C subcool Condenser 50C
C xw
h
Expansion valve Compressor Win
w
C xw,2
hw
Evaporator
T1 = 50
T2 = Tsat@1.2MPa +
Tsubcool = 46.3
P
= 1.2
2 = 11019 kJ/kg
Tw,1 = 18
,1 = 0
w
T
,2 = 26
= 0
,2 = 10901kJ/kg
QL
Q H = m w (hw,2 hw
Q H = m R (h1 h2 ) → m R = Q H = 8.367kW = 0.0498 kg/s
h1 h2 (278
kJ/kg Q L
Q H W in =
28 11019)
=
8.37
Q
kW COP
L
W
5.07
=
in 3.3kW
COP
max TH
TL
/
W in,mi n Q 5.07
= L =
COPmax
kW
= 1.13 kW
4.49
7-98 A heat pump maintains a house at a specified temperature in winter The maximum COPs of the heat pump for different outdoor temperatures are to be determined
Analysis The coefficient of performance of a heat pump will be a maximum when the heat pump operates in a reversible manner. The coefficient of performance of a reversible heat pump depends on the temperature limits in the cycle only, and is determined for all three cases above to be
7-99E A heat pump maintains a house at a specified temperature. The rate of heat loss of the house is given. The minimum power inputs required for different source temperatures are to be determined
Assumptions The heat pump operates steadily.
Analysis (a) The power input to a heat pump will be a minimum when the heat pump operates in a reversible manner. If the outdoor air at 25°F is used as the heat source, the COP of the heat pump and the required power input are determined to be
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7-32
L L L
COP 1 1 20C HP,rev = 1 (T / TH ) = 1 (10 + 273K)/(20 + 273K) = 29.3 COP 1 1 HP HP,rev = 1 (T / TH ) = 1 ( 5 + 273K)/(20 + 273K) = 11.7 COP 1 1 HP,rev = 1 (T / TH ) = 1 ( 30 + 273K)/(20 + 273K) = 5.86 TL
COP = COP = 1 HP,max HP,rev 1 (TL / TH ) 70,000 Btu/h and = 1 = 10.15 1 (25 + 460 R)/(78 + 460 R) House 78F W Q H 70,000 Btu/h 1 hp net,in,min = COP = 10.15 = 2.71 hp 2545 Btu/h HP HP,max (b) If the well-water at 50°F is used as the heat source, the COP of the heat pump and the required power input are determined to be 25F or COP = COP = 1 = 1 = 50F and HP,max HP,rev 1 (TL /TH ) 1 (50 + 460 R)/(78 + 460 R) 19 2 W Q H 70,000 Btu/h 1 hp net,in,min = COP = 19 2 = 1.43 hp 2545 Btu/h HP,max
7-100 A Carnot heat pump consumes 4.8-kW of power when operating, and maintains a house at a specified temperature. The average rate of heat loss of the house in a particular day is given The actual running time of the heat pump that day, the heating cost, and the cost if resistance heating is used instead are to be determined.
Analysis (a) The coefficient of performance of this Carnot heat pump depends on the temperature limits in the cycle only, and is determined from
(
The amount of heat the house lost that day is
Then the required work input to this Carnot heat pump is determined from the definition of the coefficient of performance to be
Thus the length of time the heat pump ran that day is
(
b) The total heating cost that day is
c) If resistance heating were used, the entire heating load for that day would have to be met by electrical energy. Therefore, the heating system would consume 1,320,000 kJ of electricitythat would cost
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7-33
H
COP = 1 = 1 = HP,rev 1 (TL / TH ) 1 (2 + 273K)/(25 + 273K) 12 96 55,000 kJ/h
H = Q H (1day
Q
) = (55,000kJ/h)(24h) =1,320,000kJ
House 25C HP 4.8 kW Q Wnet,in = COPHP = 1,320,000kJ 12 96 = 101,880 kJ
Wnet,in 101,880kJ t = = = 21,225s = 5.90 h 2C W net,in 4 8 kJ/s
Cost = W price = (W net,in t)(price) = (4 8 kW)(5 90 h)(0 11$/kWh) = $3.11
1kWh New Cost = QH price = (1,320,000kJ) (0 11$/kWh) = $40.3 3600kJ
7-101 A Carnot heat engine is used to drive a Carnot refrigerator The maximumrate of heat removal from the refrigerated space and the total rate of heat rejection to the ambient air are to be determined
Assumptions The heat engine and the refrigerator operate steadily
Analysis (a) The highest thermal efficiency a heat engine operating between two specified temperature limits can have is the Carnot efficiency, which is determined from = = 1 TL = 1 300 K = 0 744
Then the maximum power output of this heat engine is determined from the definition of thermal efficiencyto be
W net,out = thQ H = (0 744)(800 kJ/min) = 595 2
which is also the power input to the refrigerator, W net,in
The rate of heat removal from the refrigerated space will be a maximum if a Carnot refrigerator is used. The COP of the Carnot refrigerator is COP = 1 = 1 = R,rev (TH /TL ) 1 (27 + 273K)/( 5 + 273K) 1 8.37
Then the rate of heat removal from the refrigerated space becomes
(b) The total rate of heat rejection to the ambient air is the sum of the heat rejected by the heat engine ( Q L,HE ) and the heat discarded by the refrigerator ( Q H ,R ),
L,HE = Q H ,HE W net,out = 800 595.2 = 204.8 kJ/min Q
,R = Q L,R + W net,in = 4982+ 595.2 = 5577.2kJ/min
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7-34
T
900
th,max
800
C -5C
th,C H 1173K
kJ/min
kJ/min
HE
27
C
R
Q L
COP
,R = (
R,rev )(W net,in ) = (8 37)(595 2 kJ/min) = 4982 kJ/min
Q ambient = Q L,HE + Q H
Q
H
and
,R = 2048 + 5577.2 = 5782 kJ/min
7-102E A Carnot heat engine is used to drive a Carnot refrigerator The maximum rate of heat removal from the refrigerated space and the total rate of heat rejection to the ambient air are to be determined
Assumptions The heat engine and the refrigerator operate steadily
Analysis (a) The highest thermal efficiency a heat engine operating between two specified temperature limits can have is the Carnot efficiency, which is determined from = = 1 TL = 1 540 R = 0 75
Then the maximum power output of this heat engine is determined from the definition of thermal efficiencyto be
W net,out = thQ H = (0 75)(700 Btu/min) = 525
which is also the power input to the refrigerator, W net,in
The rate of heat removal from the refrigerated space will be a maximum if a Carnot refrigerator is used. The COP of the Carnot refrigerator is 1 1 COPR,rev = (T /T ) 1 = (80 + 460 R)/(20 + 460 R) 1 = 8.0
Then the rate of heat removal from the refrigerated space becomes
(
b) The total rate of heat rejection to the ambient air is the sum of the heat rejected by the heat engine ( Q L,HE ) and the heat discarded by the refrigerator ( Q H ,R ),
7-103 A heat pump that consumes 4-kW of power when operating maintains a house at a specified temperature. The house is losing heat in proportion to the temperature difference between the indoors and the outdoors. The lowest outdoor temperature for which this heat pump can do the job is to be determined
Assumptions The heat pump operates steadily
Analysis Denoting the outdoor temperature by TL, the heating load of this house can be expressed as
= (3800kJ/h K)(297 TL ) = (1 056kW/K)(297 TL )K
The coefficient of performance of a Carnot heat pump depends on the temperature limits in the cycle only, and can be expressed as
24C
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7-29
H L T L
1700F 20
F th,max
700
th,C H 2160R
Btu/min HE R 80F
Btu/min
,R = (COPR,rev )(W net,in ) = (8.0)(525 Btu/min) = 4200 Btu/min
Q L
Q L,HE = Q H ,HE W net,out = 700 525 = 175 Btu/min Q H ,R = Q L,R + W net,in = 4200+ 525 = 4725 Btu/min and Q ambient = Q L,HE + Q H ,R
175
4725
4900 Btu/min
=
+
=
Q H
House
3800
HP 1 (T or / TH ) 1 TL /(297K) HP 4 kW Q (1.056kW/K)(297 T )K COPHP = H = L
kJ/h.K COP = 1 = 1
W net,in 4 kW TL
7-102E A Carnot heat engine is used to drive a Carnot refrigerator The maximum rate of heat removal from the refrigerated space and the total rate of heat rejection to the ambient air are to be determined
Assumptions The heat engine and the refrigerator operate steadily
Equating the two relations above and solving for TL, we obtain
TL = 263 5 K = 9.5°C
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7-30
7-104 An air-conditioner with R-134a as the working fluid is considered The compressor inlet and exit states are specified The actual and maximum COPs and the minimum volume flow rate of the refrigerant at the compressor inlet are to be
determined.
Assumptions 1 The air-conditioneroperates steadily 2 The kinetic and potential energy changes are zero
Properties The properties of R-134a at the compressor inlet and exit states are (Tables A-11 through A-13)
P1 = 400kPa h1 = 25561kJ/kg
x1 = 1 = 0.05127m3/kg
= 1.2
h2 = 30063kJ/kg
Analysis (a) The mass flow rate of the refrigerant and the power consumptionof the compressor are
= 0.02601kg/s
W
1 0 05127m3/kg
= m R (h2 h1) = (0 02601kg/s)(30063 25561) kJ/kg =1 171kW
The heat gains to the room must be rejected by the air-conditioner.That is,
+
Then, the actual COP becomes
= (250kJ/min) 1min
+ 0.9kW = 5.067kW
(b) The COP of a reversible refrigerator operating between the same temperature limits is
/ TL 1 (34 + 273)/(23 + 273) 1
(
c) The minimum power input to the compressor for the same refrigerationload would be
= Q L = 5 067kW = 0.1883kW
The minimummass flow rate is 26.91
= 0.1883kW
255.61) kJ/kg = 0.004182kg/s
Finally, the minimum volume flow rate at the compressor inlet is
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7-30
v 1 L T
QH
Condenser
1.2 MPa
2 Expansion valve 70C
P2
MPa T = 70C
Compressor 400 kPa 3 80L/min
V
Evaporator sat. vap. m
v
Q
1m
1min
1000L
60s
R = 1 =
in
Q
Q
L
60s
=
Q
heat equipment
COP = Q L
W in
= 5 067kW = 4.33
1.171kW
COP
max H
1 = 1 = 26.91
W
n
in,mi
COPmax
m
= W
min h2 h
(300.63
R,min
in,
1
V
min,1
7-104 An air-conditioner with R-134a as the working fluid is considered The compressor inlet and exit states are specified The actual and maximum COPs and the minimum volume flow rate of the refrigerant at the compressor inlet are to be
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7-30
= m R,mi nv1 = (0 004 182kg /s)(0 0 5127 m 3/kg ) = 0 000 2144 m 3/s = 12.9 L/min
7-105 An expression for the COP of a completely reversible refrigerator in terms of the thermal-energyreservoir
temperatures, TL and TH is to be derived
Assumptions The refrigerator operates steadily.
Analysis Application of the first law to the completely reversible refrigerator yields
QL This result may be used to reduce the coefficientof performance,
Since this refrigerator is completelyreversible, the thermodynamic definition of temperature tells us that,
When this is substituted into the COP expression, the result is
Review Problems
7-106 An air-conditioning system maintains a house at a specified temperature. The rate of heat gain of the house, the rate of internal heat generation, and the COP are given. The required power input is to be determined.
Assumptions Steady operating conditions exist.
Analysis The cooling load of this air-conditioning system is the sum of the heat gain from the outdoors and the heat generated in the house from the people, lights, and appliances:
Q L = 20,000 + 8,000 = 28,000 kJ/h
Using the definition of the coefficient of performance, the power input to the air-conditioningsystem is determined to be
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7-31
L L
Wnet,in
H
TH COP Q Q 1 = = = R,rev Wnet,in QH QL QH / QL 1 QH
= Q
QH = TH R Wnet,in QL QL TL TL
COPR,rev = 1 = TL TH / TL 1 TH TL
House Outdoors A/C QL COP = 2.5 W = Q L = 28,000kJ/h 1kW 3.11kW net,in = COPR 2 5 3600 kJ/h
7-107E A Carnot heat pump maintains a house at a specified temperature. The rate of heat loss from the house and the outdoor temperature are given The COP and the power input are to be determined
Analysis (a) The coefficient of performance of this Carnot heat pump depends on the temperature limits in the cycle only, and is determined from
(b) The heating load of the house is
Then the required power input to this Carnot heat pump is determined from the definition of the coefficient of performance to be
7-108 The work output and the source and sink temperatures of a Carnot heat engine are given. The heat supplied to and rejected from the heat engine are to be determined
Assumptions 1 The heat engine operates steadily 2 Heat losses from the working fluid at the pipes and other components are negligible.
Applying the definition of the thermal efficiency and an energy balance to the heat engine, the unknown parameters are determined as follows:
7-109E The operating conditions of a heat pump are given The minimum temperature of the source that satisfies the second law of thermodynamicsis to be determined
Assumptions The heat pump operates steadily
Applying the first law to this heat pump gives
7-32 L T H
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COP = 1 HP,rev 1 (T /TH 1 ) = 1 (35 + 460 R)/(75 + 460 R) = 13.4 House 2500 Btu/h F
)
Q H = (2500Btu/h
F)(75 35
F = 100,000 Btu/h
75F HP W = Q H = 100,000Btu/h 1hp 2.93 hp net,in = 35F COPHP 13 4 2545Btu/h
1200°C QH HE 500 kJ = 1 TL = 1 (50 +273) K 0 781 QL th,max H (1200 + 273) K 50°C Q = Wnet = 500kJ = 640 kJ th 0.781 QL = QH Wnet = 640 500 = 140 kJ
Analysis
530
Q = Q W = 32,000 Btu/h (1.8 kW) 341214 Btu/h = 25,860Btu/h Q H L H net,in
Analysis
R
In the reversible case we have
Then the minimum temperature may be determined to be T
= TH Q
= (530R) 25,860Btu/h = 428 R
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7-33 T
HP
1kW
L
L
TL = Q L Q
1.8 kW TH Q H
Q
L
L
H 32,000Btu/h
7-110E A refrigerator with a water-cooled condenser is considered The cooling load and the COP of a refrigerator are given The power input, the exit temperature of water, and the maximum possible COP of the refrigerator are to be determined.
Assumptions The refrigerator operates steadily
The power input is
(b) The rate of heat rejected in the condenser is
(c) Taking the temperature of high-temperaturemedium to be the average temperature of water in the condenser,
25 +460 = 11 2
+ 72.02) 25
7-111 A heat pump with a specified COP and power consumptionis used to heat a house. The time it takes for this heat pump to raise the temperature of a cold house to the desired level is to be determined
Assumptions 1 Air is an ideal gas with constant specific heats at room temperature. 2 The heat loss of the house during the warp-up period is negligible. 3 The house is well-sealed so that no air leaks in or out.
Properties The constant volume specific heat of air at room temperature is cv = 0 718 kJ/kg C.
Analysis Since the house is well-sealed (constant volume), the total amount of heat that needs to be supplied to the house is
QH = (mcv T )house = (1500kg)(0 718kJ/kg C)(22 7)C = 16,155kJ
The rate at which this heat pump supplies heat is
Q H = COPHPW net,in = (2 8)(5 kW) = 14 kW
That is, this heat pump can supply 14 kJ of heat per second. Thus the time required to supply 16,155 kJ of heat is
t = QH = 16,155kJ = 1154s = 19.2 min
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7-34
Analysis (a)
Water Q L 24,000Btu/h 1 055kJ 1h 65F Condenser W = = = 3.702 kW in COP 1.9 1Btu 3600s
Q H = Q L + W in = 24,000Btu/h + 3.702kW 1Btu 3600s Q H R QL W in 24,000 Btu/h = 36,632Btu/h The exit temperature of the
is Q H = m c p (T2 T1) Q T2 = T1 + H m c p 1 055kJ 1h 25F = 65F + 36,632Btu/h = 72.02 F 3600s (1.45lbm/s) 1h (1.0 Btu/lbm F)
water
COP = TL
rev TH TL 0.5(65
=
House HP 5 kW
PROPRIETARY MATERIAL © 2017 McGraw-Hill Education Limited distribution permitted only to teachers and educators for course preparation If you are a student using this Manual, you are using it without permission 7-35 Q H 14 kJ/s
7-112 A Carnot refrigerationcycle is executed in a closed system with a fixed mass of R-134a. The net work input and the ratio of maximum-to-minimumtemperatures are given The minimum pressure in the cycle is to be determined
Assumptions The refrigerator is said to operate on the reversed Carnot cycle, which is totally reversible.
Analysis The
of performance of the cycle is
since the enthalpy of vaporization hfg at a given T or P represents the amount of heat transfer per unit mass as a substance is converted from saturated liquid to saturated vapor at that T or P. Therefore, TH is the temperature that corresponds to the hfg value of 137.5 kJ/kg, and is determined from the R-134a tables to be
MATERIAL
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PROPRIETARY
© 2017
COP = 1 = 1 = 5 T TH = 1 2TL Also, TH / TL 1 1.2 1 4 TH 3 and COPR = L → QL = COPR Win = (5)(22 kJ) = 110 kJ Win QH = QL +W = 110+ 22 = 132kJ 1 2 TL v Q 132kJ q = = = 137.5kJ/kg = H m 0 96kg h fg@T
coefficient
TH
C =
K Then, T 334.3K T = = = 278 6K 5.6C L Therefore, 1.2 1.2 Pmin = Psat@5 6C = 356 kPa
61.3
3343
7-113 Problem 7-112 is reconsidered The effect of the net work input on the minimum pressure as the work input varies from 10 kJ to 30 kJ is to be investigated The minimum pressure in the refrigerationcycle is to be plotted as a function of net work input.
Analysis The problem is solved using EES, and the results are tabulated and plotted below.
Analysis: The coefficient of performance of the cycle is given by"
m_R134a = 0.96 [kg]
THtoTLRatio = 1.2 "T_H = 1.2T L"
"W in = 22 [kJ]" "Depending on the value of W in, adjust the guess value of T_H."
COP_R = 1/( THtoTLRatio- 1)
Q_L = W in*COP_R
"First law applied to the refrigeration cycle yields:"
Q_L + W in = Q_H
"Steady-flow analysis of the condenser yields
m_R134a*h 3 = m_R134a*h 4 +Q_H
Q_H = m_R134a*(h_3-h 4) and h fg = h 3 - h_4 also T_H=T 3=T 4"
Q_H=m_R134a*h fg
h fg=enthalpy(R134a,T=T_H,x=1) - enthalpy(R134a,T=T_H,x=0)
T_H=THtoTLRatio*T_L
"The minimum pressure is the saturation pressure corresponding to T L."
P min = pressure(R134a,T=T L,x=0)*convert(kPa,MPa)
T L_C = T_L – 273
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7-37 P m i n [ M P a ] T L , C [ C ]
Win [kJ] Pmin [MPa] TH [K] TL [K] TL,C [C] 10 0.8673 368 8 307 3 34 32 15 0.6837 358.9 299 26.05 20 0.45 342 7 285 6 12 61 25 0.2251 319.3 266.1 -6.907 30 0.06978 287 1 239 2 -33.78 0 9 0 8 0.7 0 6 0 5 0 4 0 3 0.2 0 1 0 10 14 18 22 26 30 Win [kJ] 40 30 20 10 0 -10 -20 -30 -40 10 14 18 22 26 30 Win [kJ]