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
380 g of CH₄V = 20 LT = 10 °CP = ?

A tank of 20 L contains 380 g of CH₄ at 10 °C. Treat it as an ideal gas and find the pressure P.

m = 380 gM = 16.04 g/molV = 20 LT = 10 °CR = 8.314 J/(mol·K)
P = kPa
2.Ideal gas lawHard
State 1State 2

A fixed amount of N₂ goes from 100 kPa, 10 L, 20 °C to 800 kPa and 240 °C. Find the new volume V2.

P1 = 100 kPaV1 = 10 LT1 = 20 °CP2 = 800 kPaT2 = 240 °C
V2 = L
3.Energy balanceMedium
hot sidecold sideethanol · 160 °C60 °Cwater · 10 °Ct = ? °C

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

ṁh = 0.5 kg/scp,h = 2.44 kJ/(kg·K)Th: 160 → 60 °Cṁc = 2 kg/scp,c = 4.18 kJ/(kg·K)tin = 10 °C
tout = °C
4.Energy balanceHard
hot sidecold sidelight oil · 120 °C90 °Cwater · 15 °C75 °C · ṁ = ?10% lost

Hot light oil heats water in an exchanger that loses 10% 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: 120 → 90 °Ct: 15 → 75 °Ccp,c = 4.18 kJ/(kg·K)loss = 10 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 450 °CTL​ = 40 °CEQH​ = 1900 kJQL​W = ?

A heat engine works between a hot reservoir at 450 °C and a cold reservoir at 40 °C. It takes in 1900 kJ of heat. Find the most work Wmax it could possibly produce.

TH = 450 °CTL = 40 °CQH = 1900 kJ
Wmax = kJ
6.Heat engines & refrigeratorsHard
TH​ = 600 °CTL​ = 35 °CEQH​ = 1000 kJQL​ = 550 kJW = 450 kJ

A heat engine takes in 1000 kJ of heat from a reservoir at 600 °C, produces 450 kJ of work and rejects the rest to a reservoir at 35 °C, per cycle. Find the total entropy generated Sgen per cycle.

TH = 600 °CTL = 35 °CQH = 1000 kJW = 450 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 = 2. 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 = 15rc = 2T1 = 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 16. Air enters the compressor at 288 K and the turbine at 1400 K. The compressor has an isentropic efficiency of 88% and the turbine 88%. 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 = 288 KT3 = 1400 Kηc = 88%ηt = 88%k = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: P = 2789 kPa

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

Moles

n = m/M = 380/16.04 = 23.69 mol
T = 10 + 273.15 = 283.1 K

Pressure

P = nRT/V = 23.69·8.314·283.1/0.02 = 2789 kPa

Answer

P = 2789 kPa
2.Ideal gas law

Answer: V2 = 2.188 L

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

Absolute temperatures

T1 = 293.1 K, T2 = 513.1 K

Combined gas law

V2 = V1·(P1/P2)·(T2/T1) = 10·(100/800)·(513.1/293.1) = 2.188 L

Answer

V2 = 2.188 L
3.Energy balance

Answer: tout = 24.59 °C

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

Heat released by the hot stream

Q = 0.5·2.44·(160 − 60) = 122 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 10 + 122/(2·4.18) = 24.59 °C

Answer

tout = 24.59 °C
4.Energy balance

Answer: ṁc = 0.6782 kg/s

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

Heat released

Qh = 3·2.1·(120 − 90) = 189 kW

Heat that reaches the water

Qc = (1 − 0.1)·189 = 170.1 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 170.1/(4.18·60) = 0.6782 kg/s

Answer

ṁc = 0.6782 kg/s
5.Heat engines & refrigerators

Answer: Wmax = 1077 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 = 450 + 273.15 = 723.1 K
TL = 40 + 273.15 = 313.1 K

Carnot efficiency

ηmax = 1 − TL/TH = 1 − 313.1/723.1 = 56.7 %

Maximum work

Wmax = ηmax·QH = 0.567·1900 = 1077 kJ

Answer

Wmax = 1077 kJ
6.Heat engines & refrigerators

Answer: Sgen = 0.6396 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 = 1000 − 450 = 550 kJ

Absolute temperatures

TH = 600 + 273.15 = 873.1 K
TL = 35 + 273.15 = 308.1 K

Entropy changes of the reservoirs

ΔSH = −1000/873.1 = −1.145 kJ/K
ΔSL = 550/308.1 = 1.785 kJ/K
Sgen = 1.785 − 1.145 = 0.6396 kJ/K

Answer

Sgen = 0.6396 kJ/K

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

7.Gas power cycles

Answer: T3 = 1743 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 = 295·150.4 = 871.5 K

Heat addition at constant pressure

T3 = rc·T2 = 2·871.5 = 1743 K

Answer

T3 = 1743 K
8.Gas power cycles

Answer: wnet = 280.1 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 = 288·160.2857 = 636 K
T4s = 1400/160.2857 = 634 K

Compressor and turbine work

wc = 1.005·(636 − 288)/0.88 = 397.4 kJ/kg
wt = 0.88·1.005·(1400 − 634) = 677.4 kJ/kg

Net work

wnet = 677.4 − 397.4 = 280.1 kJ/kg

Answer

wnet = 280.1 kJ/kg

Back-work ratio: wc/wt = 58.66%.

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