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
30 g of O₂V = 20 LT = 65 °CP = ?

A tank of 20 L contains 30 g of O₂ at 65 °C. Treat it as an ideal gas and find the pressure P.

m = 30 gM = 32 g/molV = 20 LT = 65 °CR = 8.314 J/(mol·K)
P = kPa
2.Ideal gas lawHard
State 1State 2

A fixed amount of CO₂ goes from 100 kPa, 10 L, 20 °C to 250 kPa and 190 °C. Find the new volume V2.

P1 = 100 kPaV1 = 10 LT1 = 20 °CP2 = 250 kPaT2 = 190 °C
V2 = L
3.Energy balanceMedium
hot sidecold sideethanol · 170 °C140 °Cwater · 25 °Ct = ? °C

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

ṁh = 2.5 kg/scp,h = 2.44 kJ/(kg·K)Th: 170 → 140 °Cṁc = 1.5 kg/scp,c = 4.18 kJ/(kg·K)tin = 25 °C
tout = °C
4.Energy balanceHard
hot sidecold sidelight oil · 140 °C70 °Cwater · 15 °C45 °C · ṁ = ?10% lost

Hot light oil 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 = 3 kg/scp,h = 2.1 kJ/(kg·K)Th: 140 → 70 °Ct: 15 → 45 °Ccp,c = 4.18 kJ/(kg·K)loss = 10 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 675 °CTL​ = 30 °CEQH​ = 4700 kJQL​W = ?

A heat engine works between a hot reservoir at 675 °C and a cold reservoir at 30 °C. It takes in 4700 kJ of heat. Find the most work Wmax it could possibly produce.

TH = 675 °CTL = 30 °CQH = 4700 kJ
Wmax = kJ
6.Heat engines & refrigeratorsHard
TH​ = 45 °CTL​ = -10 °CHPQ̇H​ = 16 kWQ̇L​Ẇ = ?

A heat pump delivers 16 kW of heat to a heating system at 45 °C, taking heat from a source at -10 °C. Its actual COP is 55% of the Carnot COP between these temperatures. Find the electrical power Ẇ it uses.

TH = 45 °CTL = -10 °CηII = 55%Q̇H = 16 kW
Ẇ = kW
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 16 and a cutoff ratio rc = v₃/v₂ = 2.2. 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 = 16rc = 2.2T1 = 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 18. Air enters the compressor at 300 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 = 18T1 = 300 KT3 = 1100 Kk = 1.4cp = 1.005 kJ/(kg·K)
wnet = kJ/kg

3Solutions

1.Ideal gas law

Answer: P = 131.8 kPa

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

Moles

n = m/M = 30/32 = 0.9375 mol
T = 65 + 273.15 = 338.1 K

Pressure

P = nRT/V = 0.9375·8.314·338.1/0.02 = 131.8 kPa

Answer

P = 131.8 kPa
2.Ideal gas law

Answer: V2 = 6.32 L

Combined gas law: for a fixed amount of ideal gas, P1V1/T1 = P2V2/T2.

Absolute temperatures

T1 = 293.1 K, T2 = 463.1 K

Combined gas law

V2 = V1·(P1/P2)·(T2/T1) = 10·(100/250)·(463.1/293.1) = 6.32 L

Answer

V2 = 6.32 L
3.Energy balance

Answer: tout = 54.19 °C

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

Heat released by the hot stream

Q = 2.5·2.44·(170 − 140) = 183 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 25 + 183/(1.5·4.18) = 54.19 °C

Answer

tout = 54.19 °C
4.Energy balance

Answer: ṁc = 3.165 kg/s

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

Heat released

Qh = 3·2.1·(140 − 70) = 441 kW

Heat that reaches the water

Qc = (1 − 0.1)·441 = 396.9 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 396.9/(4.18·30) = 3.165 kg/s

Answer

ṁc = 3.165 kg/s
5.Heat engines & refrigerators

Answer: Wmax = 3197 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 = 675 + 273.15 = 948.1 K
TL = 30 + 273.15 = 303.1 K

Carnot efficiency

ηmax = 1 − TL/TH = 1 − 303.1/948.1 = 68.03 %

Maximum work

Wmax = ηmax·QH = 0.6803·4700 = 3197 kJ

Answer

Wmax = 3197 kJ
6.Heat engines & refrigerators

Answer: Ẇ = 5.029 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 = 45 + 273.15 = 318.1 K
TL = -10 + 273.15 = 263.1 K

Carnot and actual COP

COPmax = 318.1/(318.1 − 263.1) = 5.785
COP = 0.55·5.785 = 3.181

Power input

Ẇ = Q̇H/COP = 16/3.181 = 5.029 kW

Answer

Ẇ = 5.029 kW
7.Gas power cycles

Answer: qin = 1115 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 = 305·160.4 = 924.6 K
T3 = 2.2·924.6 = 2034 K

Heat added at constant pressure

qin = 1.005·(2034 − 924.6) = 1115 kJ/kg

Answer

qin = 1115 kJ/kg
8.Gas power cycles

Answer: wnet = 234.4 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

T2 = 300·180.2857 = 685.1 K
T4 = 1100/180.2857 = 481.7 K

Compressor and turbine work

wc = 1.005·(685.1 − 300) = 387.1 kJ/kg
wt = 1.005·(1100 − 481.7) = 621.4 kJ/kg

Net work

wnet = 621.4 − 387.1 = 234.4 kJ/kg

Answer

wnet = 234.4 kJ/kg

Back-work ratio: wc/wt = 62.28%.

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