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
130 g of CH₄V = 5 LT = 100 °CP = ?

A tank of 5 L contains 130 g of CH₄ at 100 °C. Treat it as an ideal gas and find the pressure P.

m = 130 gM = 16.04 g/molV = 5 LT = 100 °CR = 8.314 J/(mol·K)
P = kPa
2.Ideal gas lawHard
CO₂, M = 44.01 g/molP = 250 kPaT = 90 °Cρ = ?

Find the density ρ of CO₂ at 250 kPa and 90 °C, treating it as an ideal gas.

M = 44.01 g/molP = 250 kPaT = 90 °CR = 8.314 J/(mol·K)
ρ = kg/m³
3.Energy balanceMedium
hot sidecold sideglycol mix · 150 °C90 °Cwater · 10 °Ct = ? °C

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

ṁh = 1.5 kg/scp,h = 3.6 kJ/(kg·K)Th: 150 → 90 °Cṁc = 1 kg/scp,c = 4.18 kJ/(kg·K)tin = 10 °C
tout = °C
4.Energy balanceHard
hot sidecold sideethanol · 170 °C110 °Cwater · 25 °C65 °C · ṁ = ?5% lost

Hot ethanol heats water in an exchanger that loses 5% of the heat released by the hot stream to the surroundings. Find the water flow rate ṁc needed.

ṁh = 0.5 kg/scp,h = 2.44 kJ/(kg·K)Th: 170 → 110 °Ct: 25 → 65 °Ccp,c = 4.18 kJ/(kg·K)loss = 5 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 525 °CTL​ = 20 °CEQH​ = 4900 kJQL​W = ?

A heat engine works between a hot reservoir at 525 °C and a cold reservoir at 20 °C. It takes in 4900 kJ of heat. Find the most work Wmax it could possibly produce.

TH = 525 °CTL = 20 °CQH = 4900 kJ
Wmax = kJ
6.Heat engines & refrigeratorsHard
TH​ = 25 °CTL​ = -18 °CRQ̇H​Q̇L​ = 3 kWẆ = ?

A refrigerator keeps its cold space at -18 °C in a kitchen at 25 °C, removing heat from the cold space at 3 kW. Find the minimum power input Ẇmin.

TH = 25 °CTL = -18 °CQ̇L = 3 kW
Ẇmin = kW
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 14 and a cutoff ratio rc = v₃/v₂ = 3. At the start of compression the air is at 295 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 temperature T3 at the end of heat addition, in K.

r = 14rc = 3T1 = 295 Kk = 1.4
T3 = K
8.Gas power cyclesHard
vP1234qin​qout​

A gas-turbine plant runs on a Brayton cycle with a compressor pressure ratio of 15. Air enters the compressor at 295 K and the turbine at 1300 K. Both machines are isentropic. 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 = 15T1 = 295 KT3 = 1300 Kk = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: P = 5029 kPa

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

Moles

n = m/M = 130/16.04 = 8.105 mol
T = 100 + 273.15 = 373.1 K

Pressure

P = nRT/V = 8.105·8.314·373.1/0.005 = 5029 kPa

Answer

P = 5029 kPa
2.Ideal gas law

Answer: ρ = 3.644 kg/m³

Ideal gas density: ρ = PM/(RT).

Rearrange the gas law

PV = (m/M)RT → ρ = m/V = PM/(RT)
T = 90 + 273.15 = 363.1 K

Density

ρ = 250·44.01/(8.314·363.1) = 3.644 kg/m³

Answer

ρ = 3.644 kg/m³
3.Energy balance

Answer: tout = 87.51 °C

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

Heat released by the hot stream

Q = 1.5·3.6·(150 − 90) = 324 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 10 + 324/(1·4.18) = 87.51 °C

Answer

tout = 87.51 °C
4.Energy balance

Answer: ṁc = 0.4159 kg/s

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

Heat released

Qh = 0.5·2.44·(170 − 110) = 73.2 kW

Heat that reaches the water

Qc = (1 − 0.05)·73.2 = 69.54 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 69.54/(4.18·40) = 0.4159 kg/s

Answer

ṁc = 0.4159 kg/s
5.Heat engines & refrigerators

Answer: Wmax = 3100 kJ

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 = 525 + 273.15 = 798.1 K
TL = 20 + 273.15 = 293.1 K

Carnot efficiency

ηmax = 1 − TL/TH = 1 − 293.1/798.1 = 63.27 %

Maximum work

Wmax = ηmax·QH = 0.6327·4900 = 3100 kJ

Answer

Wmax = 3100 kJ
6.Heat engines & refrigerators

Answer: Ẇmin = 0.5056 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 = 25 + 273.15 = 298.1 K
TL = -18 + 273.15 = 255.1 K

Best possible COP

COPR,max = TL/(TH − TL) = 255.1/(298.1 − 255.1) = 5.934

Minimum power

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

Ẇmin = Q̇L/COP = 3/5.934 = 0.5056 kW

Answer

Ẇmin = 0.5056 kW
7.Gas power cycles

Answer: T3 = 2543 K

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)).

End of compression

T2 = 295·140.4 = 847.8 K

Heat addition at constant pressure

T3 = rc·T2 = 3·847.8 = 2543 K

Answer

T3 = 2543 K
8.Gas power cycles

Answer: wnet = 357.6 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

T2 = 295·150.2857 = 639.5 K
T4 = 1300/150.2857 = 599.7 K

Compressor and turbine work

wc = 1.005·(639.5 − 295) = 346.2 kJ/kg
wt = 1.005·(1300 − 599.7) = 703.8 kJ/kg

Net work

wnet = 703.8 − 346.2 = 357.6 kJ/kg

Answer

wnet = 357.6 kJ/kg

Back-work ratio: wc/wt = 49.19%.

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