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
410 g of O₂V = 5 LT = 0 °CP = ?

A tank of 5 L contains 410 g of O₂ at 0 °C. Treat it as an ideal gas and find the pressure P.

m = 410 gM = 32 g/molV = 5 LT = 0 °CR = 8.314 J/(mol·K)
P = kPa
2.Ideal gas lawHard
State 1State 2

A fixed amount of Ar goes from 350 kPa, 5 L, 10 °C to 450 kPa and 180 °C. Find the new volume V2.

P1 = 350 kPaV1 = 5 LT1 = 10 °CP2 = 450 kPaT2 = 180 °C
V2 = L
3.Energy balanceMedium
hot sidecold sideglycol mix · 170 °C140 °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 = 0.5 kg/scp,h = 3.6 kJ/(kg·K)Th: 170 → 140 °Cṁc = 3 kg/scp,c = 4.18 kJ/(kg·K)tin = 15 °C
tout = °C
4.Energy balanceHard
hot sidecold sidelight oil · 130 °C60 °Cwater · 25 °C55 °C · ṁ = ?5% lost

Hot light oil 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 = 1.5 kg/scp,h = 2.1 kJ/(kg·K)Th: 130 → 60 °Ct: 25 → 55 °Ccp,c = 4.18 kJ/(kg·K)loss = 5 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 250 °CTL​ = 35 °CEQH​QL​W

A heat engine works between a hot reservoir at 250 °C and a cold reservoir at 35 °C. Find the highest possible thermal efficiency ηmax.

TH = 250 °CTL = 35 °C
ηmax = %
6.Heat engines & refrigeratorsHard
TH​ = 650 °CTL​ = 20 °CEQH​ = 3900 kJQL​ = 2028 kJW = 1872 kJ

A heat engine takes in 3900 kJ of heat from a reservoir at 650 °C, produces 1872 kJ of work and rejects the rest to a reservoir at 20 °C, per cycle. Find the total entropy generated Sgen per cycle.

TH = 650 °CTL = 20 °CQH = 3900 kJW = 1872 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 = 1.5. At the start of compression the air is at 310 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 = 22rc = 1.5T1 = 310 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 20. Air enters the compressor at 295 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 = 20T1 = 295 KT3 = 1500 Kk = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: P = 5819 kPa

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

Moles

n = m/M = 410/32 = 12.81 mol
T = 0 + 273.15 = 273.1 K

Pressure

P = nRT/V = 12.81·8.314·273.1/0.005 = 5819 kPa

Answer

P = 5819 kPa
2.Ideal gas law

Answer: V2 = 6.224 L

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

Absolute temperatures

T1 = 283.1 K, T2 = 453.1 K

Combined gas law

V2 = V1·(P1/P2)·(T2/T1) = 5·(350/450)·(453.1/283.1) = 6.224 L

Answer

V2 = 6.224 L
3.Energy balance

Answer: tout = 19.31 °C

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

Heat released by the hot stream

Q = 0.5·3.6·(170 − 140) = 54 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 15 + 54/(3·4.18) = 19.31 °C

Answer

tout = 19.31 °C
4.Energy balance

Answer: ṁc = 1.67 kg/s

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

Heat released

Qh = 1.5·2.1·(130 − 60) = 220.5 kW

Heat that reaches the water

Qc = (1 − 0.05)·220.5 = 209.5 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 209.5/(4.18·30) = 1.67 kg/s

Answer

ṁc = 1.67 kg/s
5.Heat engines & refrigerators

Answer: ηmax = 41.1 %

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 = 250 + 273.15 = 523.1 K
TL = 35 + 273.15 = 308.1 K

Carnot efficiency

ηmax = 1 − TL/TH = 1 − 308.1/523.1 = 41.1 %

Answer

ηmax = 41.1 %
6.Heat engines & refrigerators

Answer: Sgen = 2.693 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 = 3900 − 1872 = 2028 kJ

Absolute temperatures

TH = 650 + 273.15 = 923.1 K
TL = 20 + 273.15 = 293.1 K

Entropy changes of the reservoirs

ΔSH = −3900/923.1 = −4.225 kJ/K
ΔSL = 2028/293.1 = 6.918 kJ/K
Sgen = 6.918 − 4.225 = 2.693 kJ/K

Answer

Sgen = 2.693 kJ/K

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

7.Gas power cycles

Answer: qin = 536.4 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 = 310·220.4 = 1067 K
T3 = 1.5·1067 = 1601 K

Heat added at constant pressure

qin = 1.005·(1601 − 1067) = 536.4 kJ/kg

Answer

qin = 536.4 kJ/kg
8.Gas power cycles

Answer: wnet = 465.7 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 = 295·200.2857 = 694.3 K
T4 = 1500/200.2857 = 637.3 K

Compressor and turbine work

wc = 1.005·(694.3 − 295) = 401.3 kJ/kg
wt = 1.005·(1500 − 637.3) = 867 kJ/kg

Net work

wnet = 867 − 401.3 = 465.7 kJ/kg

Answer

wnet = 465.7 kJ/kg

Back-work ratio: wc/wt = 46.29%.

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