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 ArP = 150 kPaT = 25 °CV = ?

What volume V does 60 g of Ar occupy at 150 kPa and 25 °C? Treat it as an ideal gas.

m = 60 gM = 39.95 g/molP = 150 kPaT = 25 °CR = 8.314 J/(mol·K)
V = L
2.Ideal gas lawHard
O₂, M = 32 g/molP = 300 kPaT = 170 °Cρ = ?

Find the density ρ of O₂ at 300 kPa and 170 °C, treating it as an ideal gas.

M = 32 g/molP = 300 kPaT = 170 °CR = 8.314 J/(mol·K)
ρ = kg/m³
3.Energy balanceMedium
hot sidecold sideethanol · 180 °C140 °Cwater · 20 °Ct = ? °C

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

ṁh = 1.5 kg/scp,h = 2.44 kJ/(kg·K)Th: 180 → 140 °Cṁc = 2 kg/scp,c = 4.18 kJ/(kg·K)tin = 20 °C
tout = °C
4.Energy balanceHard
hot sidecold sideglycol mix · 140 °C90 °Cwater · 25 °C45 °C · ṁ = ?15% lost

Hot glycol mix 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 = 3.6 kJ/(kg·K)Th: 140 → 90 °Ct: 25 → 45 °Ccp,c = 4.18 kJ/(kg·K)loss = 15 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 225 °CTL​ = ?EQH​ = 3600 kJQL​ = 2082 kJW

A reversible (Carnot) heat engine takes in 3600 kJ of heat from a reservoir at 225 °C and rejects 2082 kJ per cycle. Find the temperature TL of the cold reservoir in °C.

TH = 225 °CQH = 3600 kJQL = 2082 kJ
TL = °C
6.Heat engines & refrigeratorsHard
TH​ = 28 °CTL​ = -18 °CRQ̇H​Q̇L​ = 2.5 kWẆ

A refrigerator keeps its cold space at -18 °C in a kitchen at 28 °C, removing heat from the cold space at 2.5 kW. Find the highest possible coefficient of performance COPmax.

TH = 28 °CTL = -18 °CQ̇L = 2.5 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 = 2.5. 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 = 20rc = 2.5T1 = 305 Kk = 1.4cp = 1.005 kJ/(kg·K)
qin = kJ/kg
8.Gas power cyclesHard
vP1234qin​qout​

An ideal Brayton cycle operates with a compressor pressure ratio of 14. 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 = 14k = 1.4
η = %

3Solutions

1.Ideal gas law

Answer: V = 24.82 L

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

Moles

n = 60/39.95 = 1.502 mol
T = 25 + 273.15 = 298.1 K

Volume

V = nRT/P = 1.502·8.314·298.1/150 = 24.82 L

Answer

V = 24.82 L
2.Ideal gas law

Answer: ρ = 2.606 kg/m³

Ideal gas density: ρ = PM/(RT).

Rearrange the gas law

PV = (m/M)RT → ρ = m/V = PM/(RT)
T = 170 + 273.15 = 443.1 K

Density

ρ = 300·32/(8.314·443.1) = 2.606 kg/m³

Answer

ρ = 2.606 kg/m³
3.Energy balance

Answer: tout = 37.51 °C

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

Heat released by the hot stream

Q = 1.5·2.44·(180 − 140) = 146.4 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 20 + 146.4/(2·4.18) = 37.51 °C

Answer

tout = 37.51 °C
4.Energy balance

Answer: ṁc = 5.49 kg/s

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

Heat released

Qh = 3·3.6·(140 − 90) = 540 kW

Heat that reaches the water

Qc = (1 − 0.15)·540 = 459 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 459/(4.18·20) = 5.49 kg/s

Answer

ṁc = 5.49 kg/s
5.Heat engines & refrigerators

Answer: TL = 14.95 °C

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 temperature of the source

TH = 225 + 273.15 = 498.1 K

Reversible heat ratio

TL = TH·QL/QH = 498.1·2082/3600 = 288.1 K = 14.95 °C

Answer

TL = 14.95 °C
6.Heat engines & refrigerators

Answer: COPmax = 5.547

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 = 28 + 273.15 = 301.1 K
TL = -18 + 273.15 = 255.1 K

Best possible COP

COPR,max = TL/(TH − TL) = 255.1/(301.1 − 255.1) = 5.547

Answer

COPmax = 5.547
7.Gas power cycles

Answer: qin = 1524 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 = 305·200.4 = 1011 K
T3 = 2.5·1011 = 2527 K

Heat added at constant pressure

qin = 1.005·(2527 − 1011) = 1524 kJ/kg

Answer

qin = 1524 kJ/kg
8.Gas power cycles

Answer: η = 52.95 %

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 − 1/140.2857 = 1 − 1/2.126 = 52.95%

Answer

η = 52.95%

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