Thermodynamics 1: cram pack

Formula sheets, the key method steps for every topic and 8 practice problems, with full solutions at the back.

New problemsBack to the course

In the print window, choose “Save as PDF” to keep a copy on your device.

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 O₂P = 300 kPaT = 100 °CV = ?

What volume V does 30 g of O₂ occupy at 300 kPa and 100 °C? Treat it as an ideal gas.

m = 30 gM = 32 g/molP = 300 kPaT = 100 °CR = 8.314 J/(mol·K)
V = L
2.Ideal gas lawHard
CO₂, M = 44.01 g/molP = 150 kPaT = 30 °Cρ = ?

Find the density ρ of CO₂ at 150 kPa and 30 °C, treating it as an ideal gas.

M = 44.01 g/molP = 150 kPaT = 30 °CR = 8.314 J/(mol·K)
ρ = kg/m³
3.Energy balanceMedium
hot sidecold sidelight oil · 150 °C90 °Cwater · 30 °Ct = ? °C

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

ṁh = 0.5 kg/scp,h = 2.1 kJ/(kg·K)Th: 150 → 90 °Cṁc = 2 kg/scp,c = 4.18 kJ/(kg·K)tin = 30 °C
tout = °C
4.Energy balanceHard
hot sidecold sideglycol mix · 150 °C100 °Cwater · 25 °C70 °C · ṁ = ?5% lost

Hot glycol mix 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 = 2.5 kg/scp,h = 3.6 kJ/(kg·K)Th: 150 → 100 °Ct: 25 → 70 °Ccp,c = 4.18 kJ/(kg·K)loss = 5 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 850 °CTL​ = 25 °CEQH​QL​η = 48%

A heat engine receives heat from a source at 850 °C and rejects heat to the surroundings at 25 °C. Its actual thermal efficiency is 48%. Find its second-law efficiency ηII, the ratio of the actual efficiency to the Carnot efficiency.

TH = 850 °CTL = 25 °Cη = 48%
ηII = %
6.Heat engines & refrigeratorsHard
TH​ = 300 °CTL​ = 40 °CEQH​ = 4200 kJQL​ = 3066 kJW = 1134 kJ

A heat engine takes in 4200 kJ of heat from a reservoir at 300 °C, produces 1134 kJ of work and rejects the rest to a reservoir at 40 °C, per cycle. Find the total entropy generated Sgen per cycle.

TH = 300 °CTL = 40 °CQH = 4200 kJW = 1134 kJ
Sgen = kJ/K
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 14 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 = 14rc = 1.5T1 = 305 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 8. Air enters the compressor at 295 K and the turbine at 1100 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 = 8T1 = 295 KT3 = 1100 Kk = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: V = 9.695 L

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

Moles

n = 30/32 = 0.9375 mol
T = 100 + 273.15 = 373.1 K

Volume

V = nRT/P = 0.9375·8.314·373.1/300 = 9.695 L

Answer

V = 9.695 L
2.Ideal gas law

Answer: ρ = 2.619 kg/m³

Ideal gas density: ρ = PM/(RT).

Rearrange the gas law

PV = (m/M)RT → ρ = m/V = PM/(RT)
T = 30 + 273.15 = 303.1 K

Density

ρ = 150·44.01/(8.314·303.1) = 2.619 kg/m³

Answer

ρ = 2.619 kg/m³
3.Energy balance

Answer: tout = 37.54 °C

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

Heat released by the hot stream

Q = 0.5·2.1·(150 − 90) = 63 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 30 + 63/(2·4.18) = 37.54 °C

Answer

tout = 37.54 °C
4.Energy balance

Answer: ṁc = 2.273 kg/s

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

Heat released

Qh = 2.5·3.6·(150 − 100) = 450 kW

Heat that reaches the water

Qc = (1 − 0.05)·450 = 427.5 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 427.5/(4.18·45) = 2.273 kg/s

Answer

ṁc = 2.273 kg/s
5.Heat engines & refrigerators

Answer: ηII = 65.35 %

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 = 850 + 273.15 = 1123 K
TL = 25 + 273.15 = 298.1 K

Carnot efficiency

ηCarnot = 1 − 298.1/1123 = 73.45 %

Second-law efficiency

ηII = η/ηCarnot = 48/73.45 = 65.35 %

Answer

ηII = 65.35 %
6.Heat engines & refrigerators

Answer: Sgen = 2.463 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 = 4200 − 1134 = 3066 kJ

Absolute temperatures

TH = 300 + 273.15 = 573.1 K
TL = 40 + 273.15 = 313.1 K

Entropy changes of the reservoirs

ΔSH = −4200/573.1 = −7.328 kJ/K
ΔSL = 3066/313.1 = 9.791 kJ/K
Sgen = 9.791 − 7.328 = 2.463 kJ/K

Answer

Sgen = 2.463 kJ/K

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

7.Gas power cycles

Answer: qin = 440.4 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 = 305·140.4 = 876.5 K
T3 = 1.5·876.5 = 1315 K

Heat added at constant pressure

qin = 1.005·(1315 − 876.5) = 440.4 kJ/kg

Answer

qin = 440.4 kJ/kg
8.Gas power cycles

Answer: wnet = 254.6 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 = 295·80.2857 = 534.4 K
T4 = 1100/80.2857 = 607.2 K

Compressor and turbine work

wc = 1.005·(534.4 − 295) = 240.6 kJ/kg
wt = 1.005·(1100 − 607.2) = 495.2 kJ/kg

Net work

wnet = 495.2 − 240.6 = 254.6 kJ/kg

Answer

wnet = 254.6 kJ/kg

Back-work ratio: wc/wt = 48.58%.

ExamProblems · examproblems.com/courses/thermodynamics-1