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
230 g of CH₄V = 20 LT = 100 °CP = ?

A tank of 20 L contains 230 g of CH₄ at 100 °C. Treat it as an ideal gas and find the pressure P.

m = 230 gM = 16.04 g/molV = 20 LT = 100 °CR = 8.314 J/(mol·K)
P = kPa
2.Ideal gas lawHard
State 1State 2

A fixed amount of He goes from 150 kPa, 10 L, 20 °C to 600 kPa and 200 °C. Find the new volume V2.

P1 = 150 kPaV1 = 10 LT1 = 20 °CP2 = 600 kPaT2 = 200 °C
V2 = L
3.Energy balanceMedium
hot sidecold sideglycol mix · 170 °C80 °Cwater · 30 °Ct = ? °C

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

ṁh = 0.5 kg/scp,h = 3.6 kJ/(kg·K)Th: 170 → 80 °Cṁc = 1 kg/scp,c = 4.18 kJ/(kg·K)tin = 30 °C
tout = °C
4.Energy balanceHard
hot sidecold sidelight oil · 160 °C120 °Cwater · 20 °C90 °C · ṁ = ?15% lost

Hot light oil heats water in an exchanger that loses 15% of the heat released by the hot stream to the surroundings. Find the water flow rate ṁc needed.

ṁh = 3 kg/scp,h = 2.1 kJ/(kg·K)Th: 160 → 120 °Ct: 20 → 90 °Ccp,c = 4.18 kJ/(kg·K)loss = 15 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 600 °CTL​ = 25 °CEQH​QL​η = 49%

A heat engine receives heat from a source at 600 °C and rejects heat to the surroundings at 25 °C. Its actual thermal efficiency is 49%. Find its second-law efficiency ηII, the ratio of the actual efficiency to the Carnot efficiency.

TH = 600 °CTL = 25 °Cη = 49%
ηII = %
6.Heat engines & refrigeratorsHard
TH​ = 21 °CTL​ = 2 °CHPQ̇H​ = 13 kWQ̇L​Ẇ = ?

A heat pump keeps a house at 21 °C while it is 2 °C outside, delivering 13 kW of heat to the house. Find the minimum power input Ẇmin.

TH = 21 °CTL = 2 °CQ̇H = 13 kW
Ẇmin = kW
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 20 and a cutoff ratio rc = v₃/v₂ = 2. At the start of compression the air is at 300 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 = 20rc = 2T1 = 300 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 300 K and the turbine at 1300 K. The compressor has an isentropic efficiency of 82% and the turbine 85%. 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 = 300 KT3 = 1300 Kηc = 82%ηt = 85%k = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: P = 2224 kPa

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

Moles

n = m/M = 230/16.04 = 14.34 mol
T = 100 + 273.15 = 373.1 K

Pressure

P = nRT/V = 14.34·8.314·373.1/0.02 = 2224 kPa

Answer

P = 2224 kPa
2.Ideal gas law

Answer: V2 = 4.035 L

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

Absolute temperatures

T1 = 293.1 K, T2 = 473.1 K

Combined gas law

V2 = V1·(P1/P2)·(T2/T1) = 10·(150/600)·(473.1/293.1) = 4.035 L

Answer

V2 = 4.035 L
3.Energy balance

Answer: tout = 68.76 °C

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

Heat released by the hot stream

Q = 0.5·3.6·(170 − 80) = 162 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 30 + 162/(1·4.18) = 68.76 °C

Answer

tout = 68.76 °C
4.Energy balance

Answer: ṁc = 0.7321 kg/s

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

Heat released

Qh = 3·2.1·(160 − 120) = 252 kW

Heat that reaches the water

Qc = (1 − 0.15)·252 = 214.2 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 214.2/(4.18·70) = 0.7321 kg/s

Answer

ṁc = 0.7321 kg/s
5.Heat engines & refrigerators

Answer: ηII = 74.41 %

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 = 25 + 273.15 = 298.1 K

Carnot efficiency

ηCarnot = 1 − 298.1/873.1 = 65.85 %

Second-law efficiency

ηII = η/ηCarnot = 49/65.85 = 74.41 %

Answer

ηII = 74.41 %
6.Heat engines & refrigerators

Answer: Ẇmin = 0.8397 kW

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 = 21 + 273.15 = 294.1 K
TL = 2 + 273.15 = 275.1 K

Best possible COP

COPHP,max = TH/(TH − TL) = 294.1/(294.1 − 275.1) = 15.48

Minimum power

The least work is needed by a reversible machine, which has the highest COP.

Ẇmin = Q̇H/COP = 13/15.48 = 0.8397 kW

Answer

Ẇmin = 0.8397 kW
7.Gas power cycles

Answer: qin = 999.3 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 = 300·200.4 = 994.3 K
T3 = 2·994.3 = 1989 K

Heat added at constant pressure

qin = 1.005·(1989 − 994.3) = 999.3 kJ/kg

Answer

qin = 999.3 kJ/kg
8.Gas power cycles

Answer: wnet = 163.4 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 = 300·160.2857 = 662.5 K
T4s = 1300/160.2857 = 588.7 K

Compressor and turbine work

wc = 1.005·(662.5 − 300)/0.82 = 444.2 kJ/kg
wt = 0.85·1.005·(1300 − 588.7) = 607.6 kJ/kg

Net work

wnet = 607.6 − 444.2 = 163.4 kJ/kg

Answer

wnet = 163.4 kJ/kg

Back-work ratio: wc/wt = 73.11%.

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