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
60 g of N₂V = 10 LT = 40 °CP = ?

A tank of 10 L contains 60 g of N₂ at 40 °C. Treat it as an ideal gas and find the pressure P.

m = 60 gM = 28.01 g/molV = 10 LT = 40 °CR = 8.314 J/(mol·K)
P = kPa
2.Ideal gas lawHard
Ar, M = 39.95 g/molP = 250 kPaT = 30 °Cρ = ?

Find the density ρ of Ar at 250 kPa and 30 °C, treating it as an ideal gas.

M = 39.95 g/molP = 250 kPaT = 30 °CR = 8.314 J/(mol·K)
ρ = kg/m³
3.Energy balanceMedium
hot sidecold sideglycol mix · 140 °C100 °Cwater · 20 °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: 140 → 100 °Cṁc = 1.5 kg/scp,c = 4.18 kJ/(kg·K)tin = 20 °C
tout = °C
4.Energy balanceHard
hot sidecold sideethanol · 120 °C90 °Cwater · 30 °C70 °C · ṁ = ?10% lost

Hot ethanol 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 = 1.5 kg/scp,h = 2.44 kJ/(kg·K)Th: 120 → 90 °Ct: 30 → 70 °Ccp,c = 4.18 kJ/(kg·K)loss = 10 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 200 °CTL​ = 5 °CEQH​QL​W

A heat engine works between a hot reservoir at 200 °C and a cold reservoir at 5 °C. Find the highest possible thermal efficiency ηmax.

TH = 200 °CTL = 5 °C
ηmax = %
6.Heat engines & refrigeratorsHard
TH​ = 22 °CTL​ = 7 °CHPQ̇H​ = 18 kWQ̇L​Ẇ = ?

A heat pump delivers 18 kW of heat to a heating system at 22 °C, taking heat from a source at 7 °C. Its actual COP is 30% of the Carnot COP between these temperatures. Find the electrical power Ẇ it uses.

TH = 22 °CTL = 7 °CηII = 30%Q̇H = 18 kW
Ẇ = kW
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 290 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 = 1.5T1 = 290 Kk = 1.4
T3 = K
8.Gas power cyclesHard
vP1234qin​qout​

An ideal Brayton cycle operates with a compressor pressure ratio of 15. 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 = 15k = 1.4
η = %

3Solutions

1.Ideal gas law

Answer: P = 557.7 kPa

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

Moles

n = m/M = 60/28.01 = 2.142 mol
T = 40 + 273.15 = 313.1 K

Pressure

P = nRT/V = 2.142·8.314·313.1/0.01 = 557.7 kPa

Answer

P = 557.7 kPa
2.Ideal gas law

Answer: ρ = 3.963 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 = 250·39.95/(8.314·303.1) = 3.963 kg/m³

Answer

ρ = 3.963 kg/m³
3.Energy balance

Answer: tout = 31.48 °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·(140 − 100) = 72 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 20 + 72/(1.5·4.18) = 31.48 °C

Answer

tout = 31.48 °C
4.Energy balance

Answer: ṁc = 0.591 kg/s

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

Heat released

Qh = 1.5·2.44·(120 − 90) = 109.8 kW

Heat that reaches the water

Qc = (1 − 0.1)·109.8 = 98.82 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 98.82/(4.18·40) = 0.591 kg/s

Answer

ṁc = 0.591 kg/s
5.Heat engines & refrigerators

Answer: ηmax = 41.21 %

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 = 200 + 273.15 = 473.1 K
TL = 5 + 273.15 = 278.1 K

Carnot efficiency

ηmax = 1 − TL/TH = 1 − 278.1/473.1 = 41.21 %

Answer

ηmax = 41.21 %
6.Heat engines & refrigerators

Answer: Ẇ = 3.049 kW

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 = 22 + 273.15 = 295.1 K
TL = 7 + 273.15 = 280.1 K

Carnot and actual COP

COPmax = 295.1/(295.1 − 280.1) = 19.68
COP = 0.3·19.68 = 5.903

Power input

Ẇ = Q̇H/COP = 18/5.903 = 3.049 kW

Answer

Ẇ = 3.049 kW
7.Gas power cycles

Answer: T3 = 1285 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 = 290·150.4 = 856.7 K

Heat addition at constant pressure

T3 = rc·T2 = 1.5·856.7 = 1285 K

Answer

T3 = 1285 K
8.Gas power cycles

Answer: η = 53.87 %

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 − 1/150.2857 = 1 − 1/2.168 = 53.87%

Answer

η = 53.87%

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