Thermodynamics 1: cram pack

Formula sheets, the key method steps for every topic and 8 practice problems, with full solutions at the back.

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1Formulas and methods

Ideal gas law

Ideal gas law
pV = nRT
Gas constant
R = 8.314 J/(mol·K)
Combined gas law
p1V1/T1 = p2V2/T2
Moles
n = m/M
Temperature
T[K] = T[°C] + 273.15

Energy balance

Sensible heat
Q = ṁ·cp·ΔT
Latent heat
Q = ṁ·hfg
Mixing
ΣṁcpTin = ΣṁcpTout
Water
cp ≈ 4.18 kJ/(kg·K)

Heat engines & refrigerators

Efficiency
η = W/QH = 1 − QC/QH
Carnot efficiency
ηC = 1 − TC/TH (kelvin)
Refrigerator COP
COPR = QC/W
Heat pump COP
COPHP = QH/W = COPR + 1
Energy balance
QH = W + QC

Gas power cycles

Isentropic, volume ratio
T2/T1 = rk−1
Isentropic, pressure ratio
T2/T1 = rp(k−1)/k
Otto efficiency
η = 1 − 1/rk−1
Diesel efficiency
η = 1 − (1/rk−1)·(rck − 1)/(k(rc − 1))
Brayton efficiency
η = 1 − 1/rp(k−1)/k
Heat added
Otto: cv(T3 − T2) Diesel, Brayton: cp(T3 − T2)
Brayton net work
w = cp[(T3 − T4) − (T2 − T1)]
Isentropic efficiencies
wc = wc,s/ηc, wt = ηt·wt,s
Cold air
k = 1.4, cp = 1.005, cv = 0.718 kJ/(kg·K)

2Practice problems

1.Ideal gas lawMedium
470 g of N₂V = 10 LT = 65 °CP = ?

A tank of 10 L contains 470 g of N₂ at 65 °C. Treat it as an ideal gas and find the pressure P.

m = 470 gM = 28.01 g/molV = 10 LT = 65 °CR = 8.314 J/(mol·K)
P = kPa
2.Ideal gas lawHard
State 1State 2

A fixed amount of CO₂ goes from 100 kPa, 10 L, 30 °C to 600 kPa and 250 °C. Find the new volume V2.

P1 = 100 kPaV1 = 10 LT1 = 30 °CP2 = 600 kPaT2 = 250 °C
V2 = L
3.Energy balanceMedium
hot sidecold sideethanol · 160 °C120 °Cwater · 20 °Ct = ? °C

Hot ethanol cools water in a counter-flow heat exchanger with no heat loss. Find the water outlet temperature tout.

ṁh = 3 kg/scp,h = 2.44 kJ/(kg·K)Th: 160 → 120 °Cṁc = 1 kg/scp,c = 4.18 kJ/(kg·K)tin = 20 °C
tout = °C
4.Energy balanceHard
hot sidecold sideglycol mix · 120 °C80 °Cwater · 30 °C45 °C · ṁ = ?10% lost

Hot glycol mix heats water in an exchanger that loses 10% of the heat released by the hot stream to the surroundings. Find the water flow rate ṁc needed.

ṁh = 3 kg/scp,h = 3.6 kJ/(kg·K)Th: 120 → 80 °Ct: 30 → 45 °Ccp,c = 4.18 kJ/(kg·K)loss = 10 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 600 °CTL​ = 30 °CEQH​QL​η = 42%

A heat engine receives heat from a source at 600 °C and rejects heat to the surroundings at 30 °C. Its actual thermal efficiency is 42%. Find its second-law efficiency ηII, the ratio of the actual efficiency to the Carnot efficiency.

TH = 600 °CTL = 30 °Cη = 42%
ηII = %
6.Heat engines & refrigeratorsHard
850 °CTm​ = ?25 °CABWA​WB​

Two Carnot engines work in series. Engine A receives heat from a reservoir at 850 °C and rejects heat to an intermediate reservoir at temperature Tm. Engine B takes all that heat and rejects heat to a reservoir at 25 °C. Both engines have the same thermal efficiency. Find Tm in °C.

TH = 850 °CTL = 25 °C
Tm = °C
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 16 and a cutoff ratio rc = v₃/v₂ = 2.5. At the start of compression the air is at 320 K. Use the cold-air-standard assumptions: air is an ideal gas with constant specific heats, k = 1.4, cp = 1.005 kJ/(kg·K) and cv = 0.718 kJ/(kg·K). Find the heat added qin per kilogram of air, in kJ/kg.

r = 16rc = 2.5T1 = 320 Kk = 1.4cp = 1.005 kJ/(kg·K)
qin = kJ/kg
8.Gas power cyclesHard
vP1234qin​qout​

A gas-turbine plant runs on a Brayton cycle with a compressor pressure ratio of 16. Air enters the compressor at 295 K and the turbine at 1100 K. The compressor has an isentropic efficiency of 88% and the turbine 92%. Use the cold-air-standard assumptions: air is an ideal gas with constant specific heats, k = 1.4, cp = 1.005 kJ/(kg·K) and cv = 0.718 kJ/(kg·K). Find the net work output wnet per kilogram of air, in kJ/kg.

rp = 16T1 = 295 KT3 = 1100 Kηc = 88%ηt = 92%k = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: P = 4717 kPa

Ideal gas law: PV = nRT, with n = m/M.

Moles

n = m/M = 470/28.01 = 16.78 mol
T = 65 + 273.15 = 338.1 K

Pressure

P = nRT/V = 16.78·8.314·338.1/0.01 = 4717 kPa

Answer

P = 4717 kPa
2.Ideal gas law

Answer: V2 = 2.876 L

Combined gas law: for a fixed amount of ideal gas, P1V1/T1 = P2V2/T2.

Absolute temperatures

T1 = 303.1 K, T2 = 523.1 K

Combined gas law

V2 = V1·(P1/P2)·(T2/T1) = 10·(100/600)·(523.1/303.1) = 2.876 L

Answer

V2 = 2.876 L
3.Energy balance

Answer: tout = 90.05 °C

Exchanger energy balance: with no losses, ṁhcp,h(Th,in − Th,out) = ṁccp,c(tout − tin).

Heat released by the hot stream

Q = 3·2.44·(160 − 120) = 292.8 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 20 + 292.8/(1·4.18) = 90.05 °C

Answer

tout = 90.05 °C
4.Energy balance

Answer: ṁc = 6.201 kg/s

Energy balance with losses: heat released = heat absorbed + heat lost.

Heat released

Qh = 3·3.6·(120 − 80) = 432 kW

Heat that reaches the water

Qc = (1 − 0.1)·432 = 388.8 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 388.8/(4.18·15) = 6.201 kg/s

Answer

ṁc = 6.201 kg/s
5.Heat engines & refrigerators

Answer: ηII = 64.34 %

Second-law limits: no cycle working between reservoirs at absolute temperatures TH and TL can beat the reversible (Carnot) cycle: ηmax = 1 − TL/TH, COPR,max = TL/(TH − TL) and COPHP,max = TH/(TH − TL). Energy is always conserved: QH = W + QL.

Absolute temperatures

TH = 600 + 273.15 = 873.1 K
TL = 30 + 273.15 = 303.1 K

Carnot efficiency

ηCarnot = 1 − 303.1/873.1 = 65.28 %

Second-law efficiency

ηII = η/ηCarnot = 42/65.28 = 64.34 %

Answer

ηII = 64.34 %
6.Heat engines & refrigerators

Answer: Tm = 305.5 °C

Second-law limits: no cycle working between reservoirs at absolute temperatures TH and TL can beat the reversible (Carnot) cycle: ηmax = 1 − TL/TH, COPR,max = TL/(TH − TL) and COPHP,max = TH/(TH − TL). Energy is always conserved: QH = W + QL.

Absolute temperatures

TH = 850 + 273.15 = 1123 K
TL = 25 + 273.15 = 298.1 K

Equal efficiencies

1 − Tm/TH = 1 − TL/Tm gives Tm² = TH·TL.

Tm = √(1123·298.1) = 578.7 K = 305.5 °C

Answer

Tm = 305.5 °C
7.Gas power cycles

Answer: qin = 1462 kJ/kg

Diesel cycle (compression-ignition engine): 1→2 isentropic compression, 2→3 heat addition at constant pressure, 3→4 isentropic expansion, 4→1 heat rejection at constant volume. With compression ratio r = v₁/v₂ and cutoff ratio rc = v₃/v₂: T₂ = T₁·rk−1, T₃ = rc·T₂, qin = cp·(T₃ − T₂) and η = 1 − (1/rk−1)·(rck − 1)/(k·(rc − 1)).

Temperatures

T2 = 320·160.4 = 970.1 K
T3 = 2.5·970.1 = 2425 K

Heat added at constant pressure

qin = 1.005·(2425 − 970.1) = 1462 kJ/kg

Answer

qin = 1462 kJ/kg
8.Gas power cycles

Answer: wnet = 149.4 kJ/kg

Brayton cycle (gas turbine): 1→2 isentropic compression, 2→3 heat addition at constant pressure, 3→4 isentropic expansion in the turbine, 4→1 heat rejection at constant pressure. With pressure ratio rp = P₂/P₁: T₂ = T₁·rp(k−1)/k, T₄ = T₃/rp(k−1)/k and η = 1 − 1/rp(k−1)/k. Net work w = cp·[(T₃ − T₄) − (T₂ − T₁)]. With isentropic efficiencies, the compressor needs ws/ηc and the turbine gives ηt·ws.

Isentropic temperatures

T2s = 295·160.2857 = 651.4 K
T4s = 1100/160.2857 = 498.1 K

Compressor and turbine work

wc = 1.005·(651.4 − 295)/0.88 = 407 kJ/kg
wt = 0.92·1.005·(1100 − 498.1) = 556.5 kJ/kg

Net work

wnet = 556.5 − 407 = 149.4 kJ/kg

Answer

wnet = 149.4 kJ/kg

Back-work ratio: wc/wt = 73.15%.

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