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
30 g of N₂P = 250 kPaT = 85 °CV = ?

What volume V does 30 g of N₂ occupy at 250 kPa and 85 °C? Treat it as an ideal gas.

m = 30 gM = 28.01 g/molP = 250 kPaT = 85 °CR = 8.314 J/(mol·K)
V = L
2.Ideal gas lawHard
State 1State 2

A fixed amount of Ar goes from 350 kPa, 20 L, 15 °C to 450 kPa and 220 °C. Find the new volume V2.

P1 = 350 kPaV1 = 20 LT1 = 15 °CP2 = 450 kPaT2 = 220 °C
V2 = L
3.Energy balanceMedium
hot sidecold sideglycol mix · 120 °C70 °Cwater · 15 °Ct = ? °C

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

ṁh = 2 kg/scp,h = 3.6 kJ/(kg·K)Th: 120 → 70 °Cṁc = 1.5 kg/scp,c = 4.18 kJ/(kg·K)tin = 15 °C
tout = °C
4.Energy balanceHard
hot sidecold sideglycol mix · 130 °C90 °Cwater · 10 °C75 °C · ṁ = ?15% lost

Hot glycol mix 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 = 1.5 kg/scp,h = 3.6 kJ/(kg·K)Th: 130 → 90 °Ct: 10 → 75 °Ccp,c = 4.18 kJ/(kg·K)loss = 15 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 375 °CTL​ = 20 °CEQH​QL​W

A heat engine works between a hot reservoir at 375 °C and a cold reservoir at 20 °C. Find the highest possible thermal efficiency ηmax.

TH = 375 °CTL = 20 °C
ηmax = %
6.Heat engines & refrigeratorsHard
TH​ = 550 °CTL​ = 15 °CEQH​ = 3000 kJQL​ = 1830 kJW = 1170 kJ

A heat engine takes in 3000 kJ of heat from a reservoir at 550 °C, produces 1170 kJ of work and rejects the rest to a reservoir at 15 °C, per cycle. Find the total entropy generated Sgen per cycle.

TH = 550 °CTL = 15 °CQH = 3000 kJW = 1170 kJ
Sgen = kJ/K
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 22 and a cutoff ratio rc = v₃/v₂ = 3. 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 its thermal efficiency η in percent.

r = 22rc = 3k = 1.4
η = %
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 310 K and the turbine at 1500 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 = 310 KT3 = 1500 Kk = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: V = 12.76 L

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

Moles

n = 30/28.01 = 1.071 mol
T = 85 + 273.15 = 358.1 K

Volume

V = nRT/P = 1.071·8.314·358.1/250 = 12.76 L

Answer

V = 12.76 L
2.Ideal gas law

Answer: V2 = 26.62 L

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

Absolute temperatures

T1 = 288.1 K, T2 = 493.1 K

Combined gas law

V2 = V1·(P1/P2)·(T2/T1) = 20·(350/450)·(493.1/288.1) = 26.62 L

Answer

V2 = 26.62 L
3.Energy balance

Answer: tout = 72.42 °C

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

Heat released by the hot stream

Q = 2·3.6·(120 − 70) = 360 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 15 + 360/(1.5·4.18) = 72.42 °C

Answer

tout = 72.42 °C
4.Energy balance

Answer: ṁc = 0.6757 kg/s

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

Heat released

Qh = 1.5·3.6·(130 − 90) = 216 kW

Heat that reaches the water

Qc = (1 − 0.15)·216 = 183.6 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 183.6/(4.18·65) = 0.6757 kg/s

Answer

ṁc = 0.6757 kg/s
5.Heat engines & refrigerators

Answer: ηmax = 54.77 %

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 = 375 + 273.15 = 648.1 K
TL = 20 + 273.15 = 293.1 K

Carnot efficiency

ηmax = 1 − TL/TH = 1 − 293.1/648.1 = 54.77 %

Answer

ηmax = 54.77 %
6.Heat engines & refrigerators

Answer: Sgen = 2.706 kJ/K

Entropy generation: over a full cycle the working fluid has no net entropy change. The hot reservoir loses QH/TH and the cold reservoir gains QL/TL. Their sum is the entropy generated, which is zero for a reversible cycle and positive for every real one.

Heat rejected

QL = QH − W = 3000 − 1170 = 1830 kJ

Absolute temperatures

TH = 550 + 273.15 = 823.1 K
TL = 15 + 273.15 = 288.1 K

Entropy changes of the reservoirs

ΔSH = −3000/823.1 = −3.645 kJ/K
ΔSL = 1830/288.1 = 6.351 kJ/K
Sgen = 6.351 − 3.645 = 2.706 kJ/K

Answer

Sgen = 2.706 kJ/K

Sgen > 0, so the engine is possible but irreversible.

7.Gas power cycles

Answer: η = 62.08 %

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)).

Cutoff term

(31.4 − 1)/(1.4·(3 − 1)) = 1.306

Thermal efficiency

η = 1 − 0.2904·1.306 = 62.08%

Answer

η = 62.08%
8.Gas power cycles

Answer: wnet = 448.3 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 = 310·150.2857 = 672 K
T4 = 1500/150.2857 = 691.9 K

Compressor and turbine work

wc = 1.005·(672 − 310) = 363.8 kJ/kg
wt = 1.005·(1500 − 691.9) = 812.1 kJ/kg

Net work

wnet = 812.1 − 363.8 = 448.3 kJ/kg

Answer

wnet = 448.3 kJ/kg

Back-work ratio: wc/wt = 44.8%.

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