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
350 g of HeP = 350 kPaT = 20 °CV = ?

What volume V does 350 g of He occupy at 350 kPa and 20 °C? Treat it as an ideal gas.

m = 350 gM = 4.003 g/molP = 350 kPaT = 20 °CR = 8.314 J/(mol·K)
V = L
2.Ideal gas lawHard
Ar, M = 39.95 g/molP = 350 kPaT = 100 °Cρ = ?

Find the density ρ of Ar at 350 kPa and 100 °C, treating it as an ideal gas.

M = 39.95 g/molP = 350 kPaT = 100 °CR = 8.314 J/(mol·K)
ρ = kg/m³
3.Energy balanceMedium
hot sidecold sidelight oil · 120 °C60 °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 = 2 kg/scp,h = 2.1 kJ/(kg·K)Th: 120 → 60 °Cṁc = 1.5 kg/scp,c = 4.18 kJ/(kg·K)tin = 30 °C
tout = °C
4.Energy balanceHard
hot sidecold sidelight oil · 130 °C90 °Cwater · 30 °C65 °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 = 3 kg/scp,h = 2.1 kJ/(kg·K)Th: 130 → 90 °Ct: 30 → 65 °Ccp,c = 4.18 kJ/(kg·K)loss = 5 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 625 °CTL​ = 20 °CEQH​ = 800 kJQL​W = ?

A heat engine works between a hot reservoir at 625 °C and a cold reservoir at 20 °C. It takes in 800 kJ of heat. Find the most work Wmax it could possibly produce.

TH = 625 °CTL = 20 °CQH = 800 kJ
Wmax = kJ
6.Heat engines & refrigeratorsHard
TH​ = 30 °CTL​ = -10 °CRQ̇H​Q̇L​ = 2 kWẆ

A refrigerator keeps its cold space at -10 °C in a kitchen at 30 °C, removing heat from the cold space at 2 kW. Find the highest possible coefficient of performance COPmax.

TH = 30 °CTL = -10 °CQ̇L = 2 kW
COPmax =
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 20 and a cutoff ratio rc = v₃/v₂ = 1.5. At the start of compression the air is at 320 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 = 20rc = 1.5T1 = 320 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 8. Air enters the compressor at 288 K and the turbine at 1400 K. The compressor has an isentropic efficiency of 88% and the turbine 90%. 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 = 288 KT3 = 1400 Kηc = 88%ηt = 90%k = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: V = 608.9 L

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

Moles

n = 350/4.003 = 87.43 mol
T = 20 + 273.15 = 293.1 K

Volume

V = nRT/P = 87.43·8.314·293.1/350 = 608.9 L

Answer

V = 608.9 L
2.Ideal gas law

Answer: ρ = 4.507 kg/m³

Ideal gas density: ρ = PM/(RT).

Rearrange the gas law

PV = (m/M)RT → ρ = m/V = PM/(RT)
T = 100 + 273.15 = 373.1 K

Density

ρ = 350·39.95/(8.314·373.1) = 4.507 kg/m³

Answer

ρ = 4.507 kg/m³
3.Energy balance

Answer: tout = 70.19 °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·(120 − 60) = 252 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 30 + 252/(1.5·4.18) = 70.19 °C

Answer

tout = 70.19 °C
4.Energy balance

Answer: ṁc = 1.636 kg/s

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

Heat released

Qh = 3·2.1·(130 − 90) = 252 kW

Heat that reaches the water

Qc = (1 − 0.05)·252 = 239.4 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 239.4/(4.18·35) = 1.636 kg/s

Answer

ṁc = 1.636 kg/s
5.Heat engines & refrigerators

Answer: Wmax = 538.9 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 = 625 + 273.15 = 898.1 K
TL = 20 + 273.15 = 293.1 K

Carnot efficiency

ηmax = 1 − TL/TH = 1 − 293.1/898.1 = 67.36 %

Maximum work

Wmax = ηmax·QH = 0.6736·800 = 538.9 kJ

Answer

Wmax = 538.9 kJ
6.Heat engines & refrigerators

Answer: COPmax = 6.579

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 = 30 + 273.15 = 303.1 K
TL = -10 + 273.15 = 263.1 K

Best possible COP

COPR,max = TL/(TH − TL) = 263.1/(303.1 − 263.1) = 6.579

Answer

COPmax = 6.579
7.Gas power cycles

Answer: T3 = 1591 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 = 320·200.4 = 1061 K

Heat addition at constant pressure

T3 = rc·T2 = 1.5·1061 = 1591 K

Answer

T3 = 1591 K
8.Gas power cycles

Answer: wnet = 300.4 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 = 288·80.2857 = 521.7 K
T4s = 1400/80.2857 = 772.9 K

Compressor and turbine work

wc = 1.005·(521.7 − 288)/0.88 = 266.9 kJ/kg
wt = 0.9·1.005·(1400 − 772.9) = 567.2 kJ/kg

Net work

wnet = 567.2 − 266.9 = 300.4 kJ/kg

Answer

wnet = 300.4 kJ/kg

Back-work ratio: wc/wt = 47.05%.

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