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
430 g of ArP = 250 kPaT = 20 °CV = ?

What volume V does 430 g of Ar occupy at 250 kPa and 20 °C? Treat it as an ideal gas.

m = 430 gM = 39.95 g/molP = 250 kPaT = 20 °CR = 8.314 J/(mol·K)
V = L
2.Ideal gas lawHard
CH₄, M = 16.04 g/molP = 250 kPaT = 180 °Cρ = ?

Find the density ρ of CH₄ at 250 kPa and 180 °C, treating it as an ideal gas.

M = 16.04 g/molP = 250 kPaT = 180 °CR = 8.314 J/(mol·K)
ρ = kg/m³
3.Energy balanceMedium
hot sidecold sidelight oil · 140 °C90 °Cwater · 20 °Ct = ? °C

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

ṁh = 2 kg/scp,h = 2.1 kJ/(kg·K)Th: 140 → 90 °Cṁc = 1.5 kg/scp,c = 4.18 kJ/(kg·K)tin = 20 °C
tout = °C
4.Energy balanceHard
hot sidecold sidelight oil · 150 °C110 °Cwater · 25 °C70 °C · ṁ = ?15% lost

Hot light oil 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 = 3 kg/scp,h = 2.1 kJ/(kg·K)Th: 150 → 110 °Ct: 25 → 70 °Ccp,c = 4.18 kJ/(kg·K)loss = 15 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 350 °CTL​ = 20 °CEQH​QL​η = 32%

A heat engine receives heat from a source at 350 °C and rejects heat to the surroundings at 20 °C. Its actual thermal efficiency is 32%. Find its second-law efficiency ηII, the ratio of the actual efficiency to the Carnot efficiency.

TH = 350 °CTL = 20 °Cη = 32%
ηII = %
6.Heat engines & refrigeratorsHard
TH​ = 700 °CTL​ = 20 °CEQH​ = 3100 kJQL​ = 1798 kJW = 1302 kJ

A heat engine takes in 3100 kJ of heat from a reservoir at 700 °C, produces 1302 kJ of work and rejects the rest to a reservoir at 20 °C, per cycle. Find the total entropy generated Sgen per cycle.

TH = 700 °CTL = 20 °CQH = 3100 kJW = 1302 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. 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.

r = 15rc = 1.5k = 1.4
η = %
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 290 K and the turbine at 1300 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 = 290 KT3 = 1300 Kk = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: V = 104.9 L

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

Moles

n = 430/39.95 = 10.76 mol
T = 20 + 273.15 = 293.1 K

Volume

V = nRT/P = 10.76·8.314·293.1/250 = 104.9 L

Answer

V = 104.9 L
2.Ideal gas law

Answer: ρ = 1.064 kg/m³

Ideal gas density: ρ = PM/(RT).

Rearrange the gas law

PV = (m/M)RT → ρ = m/V = PM/(RT)
T = 180 + 273.15 = 453.1 K

Density

ρ = 250·16.04/(8.314·453.1) = 1.064 kg/m³

Answer

ρ = 1.064 kg/m³
3.Energy balance

Answer: tout = 53.49 °C

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

Heat released by the hot stream

Q = 2·2.1·(140 − 90) = 210 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 20 + 210/(1.5·4.18) = 53.49 °C

Answer

tout = 53.49 °C
4.Energy balance

Answer: ṁc = 1.139 kg/s

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

Heat released

Qh = 3·2.1·(150 − 110) = 252 kW

Heat that reaches the water

Qc = (1 − 0.15)·252 = 214.2 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 214.2/(4.18·45) = 1.139 kg/s

Answer

ṁc = 1.139 kg/s
5.Heat engines & refrigerators

Answer: ηII = 60.43 %

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 = 350 + 273.15 = 623.1 K
TL = 20 + 273.15 = 293.1 K

Carnot efficiency

ηCarnot = 1 − 293.1/623.1 = 52.96 %

Second-law efficiency

ηII = η/ηCarnot = 32/52.96 = 60.43 %

Answer

ηII = 60.43 %
6.Heat engines & refrigerators

Answer: Sgen = 2.948 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 = 3100 − 1302 = 1798 kJ

Absolute temperatures

TH = 700 + 273.15 = 973.1 K
TL = 20 + 273.15 = 293.1 K

Entropy changes of the reservoirs

ΔSH = −3100/973.1 = −3.186 kJ/K
ΔSL = 1798/293.1 = 6.133 kJ/K
Sgen = 6.133 − 3.186 = 2.948 kJ/K

Answer

Sgen = 2.948 kJ/K

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

7.Gas power cycles

Answer: η = 63.05 %

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)).

Cutoff term

(1.51.4 − 1)/(1.4·(1.5 − 1)) = 1.092

Thermal efficiency

η = 1 − 0.3385·1.092 = 63.05%

Answer

η = 63.05%
8.Gas power cycles

Answer: wnet = 348.8 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 = 290·80.2857 = 525.3 K
T4 = 1300/80.2857 = 717.7 K

Compressor and turbine work

wc = 1.005·(525.3 − 290) = 236.5 kJ/kg
wt = 1.005·(1300 − 717.7) = 585.3 kJ/kg

Net work

wnet = 585.3 − 236.5 = 348.8 kJ/kg

Answer

wnet = 348.8 kJ/kg

Back-work ratio: wc/wt = 40.41%.

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