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
190 g of N₂P = 650 kPaT = 10 °CV = ?

What volume V does 190 g of N₂ occupy at 650 kPa and 10 °C? Treat it as an ideal gas.

m = 190 gM = 28.01 g/molP = 650 kPaT = 10 °CR = 8.314 J/(mol·K)
V = L
2.Ideal gas lawHard
N₂, M = 28.01 g/molP = 100 kPaT = 190 °Cρ = ?

Find the density ρ of N₂ at 100 kPa and 190 °C, treating it as an ideal gas.

M = 28.01 g/molP = 100 kPaT = 190 °CR = 8.314 J/(mol·K)
ρ = kg/m³
3.Energy balanceMedium
hot sidecold sidelight oil · 130 °C90 °Cwater · 20 °Ct = ? °C

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

ṁh = 1.5 kg/scp,h = 2.1 kJ/(kg·K)Th: 130 → 90 °Cṁc = 1.5 kg/scp,c = 4.18 kJ/(kg·K)tin = 20 °C
tout = °C
4.Energy balanceHard
hot sidecold sideethanol · 140 °C80 °Cwater · 30 °C80 °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 = 2 kg/scp,h = 2.44 kJ/(kg·K)Th: 140 → 80 °Ct: 30 → 80 °Ccp,c = 4.18 kJ/(kg·K)loss = 5 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 300 °CTL​ = 10 °CEQH​QL​η = 20%

A heat engine receives heat from a source at 300 °C and rejects heat to the surroundings at 10 °C. Its actual thermal efficiency is 20%. Find its second-law efficiency ηII, the ratio of the actual efficiency to the Carnot efficiency.

TH = 300 °CTL = 10 °Cη = 20%
ηII = %
6.Heat engines & refrigeratorsHard
TH​ = 550 °CTL​ = 30 °CEQH​ = 700 kJQL​ = 392 kJW = 308 kJ

A heat engine takes in 700 kJ of heat from a reservoir at 550 °C, produces 308 kJ of work and rejects the rest to a reservoir at 30 °C, per cycle. Find the total entropy generated Sgen per cycle.

TH = 550 °CTL = 30 °CQH = 700 kJW = 308 kJ
Sgen = kJ/K
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 19 and a cutoff ratio rc = v₃/v₂ = 1.5. At the start of compression the air is at 305 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 = 19rc = 1.5T1 = 305 Kk = 1.4cp = 1.005 kJ/(kg·K)
qin = kJ/kg
8.Gas power cyclesHard
vP1234qin​qout​

An ideal Brayton cycle operates with a compressor pressure ratio of 16. 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.

rp = 16k = 1.4
η = %

3Solutions

1.Ideal gas law

Answer: V = 24.57 L

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

Moles

n = 190/28.01 = 6.783 mol
T = 10 + 273.15 = 283.1 K

Volume

V = nRT/P = 6.783·8.314·283.1/650 = 24.57 L

Answer

V = 24.57 L
2.Ideal gas law

Answer: ρ = 0.7274 kg/m³

Ideal gas density: ρ = PM/(RT).

Rearrange the gas law

PV = (m/M)RT → ρ = m/V = PM/(RT)
T = 190 + 273.15 = 463.1 K

Density

ρ = 100·28.01/(8.314·463.1) = 0.7274 kg/m³

Answer

ρ = 0.7274 kg/m³
3.Energy balance

Answer: tout = 40.1 °C

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

Heat released by the hot stream

Q = 1.5·2.1·(130 − 90) = 126 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 20 + 126/(1.5·4.18) = 40.1 °C

Answer

tout = 40.1 °C
4.Energy balance

Answer: ṁc = 1.331 kg/s

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

Heat released

Qh = 2·2.44·(140 − 80) = 292.8 kW

Heat that reaches the water

Qc = (1 − 0.05)·292.8 = 278.2 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 278.2/(4.18·50) = 1.331 kg/s

Answer

ṁc = 1.331 kg/s
5.Heat engines & refrigerators

Answer: ηII = 39.53 %

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 = 300 + 273.15 = 573.1 K
TL = 10 + 273.15 = 283.1 K

Carnot efficiency

ηCarnot = 1 − 283.1/573.1 = 50.6 %

Second-law efficiency

ηII = η/ηCarnot = 20/50.6 = 39.53 %

Answer

ηII = 39.53 %
6.Heat engines & refrigerators

Answer: Sgen = 0.4427 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 = 700 − 308 = 392 kJ

Absolute temperatures

TH = 550 + 273.15 = 823.1 K
TL = 30 + 273.15 = 303.1 K

Entropy changes of the reservoirs

ΔSH = −700/823.1 = −0.8504 kJ/K
ΔSL = 392/303.1 = 1.293 kJ/K
Sgen = 1.293 − 0.8504 = 0.4427 kJ/K

Answer

Sgen = 0.4427 kJ/K

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

7.Gas power cycles

Answer: qin = 497.7 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 = 305·190.4 = 990.4 K
T3 = 1.5·990.4 = 1486 K

Heat added at constant pressure

qin = 1.005·(1486 − 990.4) = 497.7 kJ/kg

Answer

qin = 497.7 kJ/kg
8.Gas power cycles

Answer: η = 54.71 %

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.

Thermal efficiency

η = 1 − 1/160.2857 = 1 − 1/2.208 = 54.71%

Answer

η = 54.71%

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