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
500 g of ArP = 550 kPaT = 95 °CV = ?

What volume V does 500 g of Ar occupy at 550 kPa and 95 °C? Treat it as an ideal gas.

m = 500 gM = 39.95 g/molP = 550 kPaT = 95 °CR = 8.314 J/(mol·K)
V = L
2.Ideal gas lawHard
Ar, M = 39.95 g/molP = 300 kPaT = 80 °Cρ = ?

Find the density ρ of Ar at 300 kPa and 80 °C, treating it as an ideal gas.

M = 39.95 g/molP = 300 kPaT = 80 °CR = 8.314 J/(mol·K)
ρ = kg/m³
3.Energy balanceMedium
hot sidecold sidelight oil · 150 °C70 °Cwater · 10 °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 kg/scp,h = 2.1 kJ/(kg·K)Th: 150 → 70 °Cṁc = 1 kg/scp,c = 4.18 kJ/(kg·K)tin = 10 °C
tout = °C
4.Energy balanceHard
hot sidecold sideglycol mix · 180 °C110 °Cwater · 25 °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 = 2 kg/scp,h = 3.6 kJ/(kg·K)Th: 180 → 110 °Ct: 25 → 75 °Ccp,c = 4.18 kJ/(kg·K)loss = 15 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 400 °CTL​ = ?EQH​ = 4500 kJQL​ = 1926 kJW

A reversible (Carnot) heat engine takes in 4500 kJ of heat from a reservoir at 400 °C and rejects 1926 kJ per cycle. Find the temperature TL of the cold reservoir in °C.

TH = 400 °CQH = 4500 kJQL = 1926 kJ
TL = °C
6.Heat engines & refrigeratorsHard
TH​ = 350 °CTL​ = 10 °CEQH​ = 2100 kJQL​ = 1176 kJW = 924 kJ

A heat engine takes in 2100 kJ of heat from a reservoir at 350 °C, produces 924 kJ of work and rejects the rest to a reservoir at 10 °C, per cycle. Find the total entropy generated Sgen per cycle.

TH = 350 °CTL = 10 °CQH = 2100 kJW = 924 kJ
Sgen = kJ/K
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 15 and a cutoff ratio rc = v₃/v₂ = 1.5. 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 = 15rc = 1.5T1 = 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 18. Air enters the compressor at 290 K and the turbine at 1400 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 = 18T1 = 290 KT3 = 1400 Kk = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: V = 69.65 L

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

Moles

n = 500/39.95 = 12.52 mol
T = 95 + 273.15 = 368.1 K

Volume

V = nRT/P = 12.52·8.314·368.1/550 = 69.65 L

Answer

V = 69.65 L
2.Ideal gas law

Answer: ρ = 4.082 kg/m³

Ideal gas density: ρ = PM/(RT).

Rearrange the gas law

PV = (m/M)RT → ρ = m/V = PM/(RT)
T = 80 + 273.15 = 353.1 K

Density

ρ = 300·39.95/(8.314·353.1) = 4.082 kg/m³

Answer

ρ = 4.082 kg/m³
3.Energy balance

Answer: tout = 50.19 °C

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

Heat released by the hot stream

Q = 1·2.1·(150 − 70) = 168 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 10 + 168/(1·4.18) = 50.19 °C

Answer

tout = 50.19 °C
4.Energy balance

Answer: ṁc = 2.05 kg/s

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

Heat released

Qh = 2·3.6·(180 − 110) = 504 kW

Heat that reaches the water

Qc = (1 − 0.15)·504 = 428.4 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 428.4/(4.18·50) = 2.05 kg/s

Answer

ṁc = 2.05 kg/s
5.Heat engines & refrigerators

Answer: TL = 14.96 °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 temperature of the source

TH = 400 + 273.15 = 673.1 K

Reversible heat ratio

TL = TH·QL/QH = 673.1·1926/4500 = 288.1 K = 14.96 °C

Answer

TL = 14.96 °C
6.Heat engines & refrigerators

Answer: Sgen = 0.7833 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 = 2100 − 924 = 1176 kJ

Absolute temperatures

TH = 350 + 273.15 = 623.1 K
TL = 10 + 273.15 = 283.1 K

Entropy changes of the reservoirs

ΔSH = −2100/623.1 = −3.37 kJ/K
ΔSL = 1176/283.1 = 4.153 kJ/K
Sgen = 4.153 − 3.37 = 0.7833 kJ/K

Answer

Sgen = 0.7833 kJ/K

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

7.Gas power cycles

Answer: qin = 475 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 = 320·150.4 = 945.3 K
T3 = 1.5·945.3 = 1418 K

Heat added at constant pressure

qin = 1.005·(1418 − 945.3) = 475 kJ/kg

Answer

qin = 475 kJ/kg
8.Gas power cycles

Answer: wnet = 416.8 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 = 290·180.2857 = 662.3 K
T4 = 1400/180.2857 = 613 K

Compressor and turbine work

wc = 1.005·(662.3 − 290) = 374.2 kJ/kg
wt = 1.005·(1400 − 613) = 790.9 kJ/kg

Net work

wnet = 790.9 − 374.2 = 416.8 kJ/kg

Answer

wnet = 416.8 kJ/kg

Back-work ratio: wc/wt = 47.31%.

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