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
20 g of O₂V = 10 LT = 0 °CP = ?

A tank of 10 L contains 20 g of O₂ at 0 °C. Treat it as an ideal gas and find the pressure P.

m = 20 gM = 32 g/molV = 10 LT = 0 °CR = 8.314 J/(mol·K)
P = kPa
2.Ideal gas lawHard
State 1State 2

A fixed amount of CH₄ goes from 300 kPa, 10 L, 15 °C to 550 kPa and 90 °C. Find the new volume V2.

P1 = 300 kPaV1 = 10 LT1 = 15 °CP2 = 550 kPaT2 = 90 °C
V2 = L
3.Energy balanceMedium
hot sidecold sidelight oil · 150 °C110 °Cwater · 15 °Ct = ? °C

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

ṁh = 1.5 kg/scp,h = 2.1 kJ/(kg·K)Th: 150 → 110 °Cṁc = 2 kg/scp,c = 4.18 kJ/(kg·K)tin = 15 °C
tout = °C
4.Energy balanceHard
hot sidecold sideethanol · 170 °C90 °Cwater · 20 °C60 °C · ṁ = ?5% lost

Hot ethanol 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 = 1 kg/scp,h = 2.44 kJ/(kg·K)Th: 170 → 90 °Ct: 20 → 60 °Ccp,c = 4.18 kJ/(kg·K)loss = 5 %
ṁc = kg/s
5.Heat engines & refrigeratorsMedium
TH​ = 775 °CTL​ = ?EQH​ = 500 kJQL​ = 149 kJW

A reversible (Carnot) heat engine takes in 500 kJ of heat from a reservoir at 775 °C and rejects 149 kJ per cycle. Find the temperature TL of the cold reservoir in °C.

TH = 775 °CQH = 500 kJQL = 149 kJ
TL = °C
6.Heat engines & refrigeratorsHard
TH​ = 700 °CTL​ = 35 °CEQH​ = 3100 kJQL​ = 1395 kJW = 1705 kJ

A heat engine takes in 3100 kJ of heat from a reservoir at 700 °C, produces 1705 kJ of work and rejects the rest to a reservoir at 35 °C, per cycle. Find the total entropy generated Sgen per cycle.

TH = 700 °CTL = 35 °CQH = 3100 kJW = 1705 kJ
Sgen = kJ/K
7.Gas power cyclesMedium
vP1234qin​qout​

An ideal Diesel cycle has a compression ratio r = 19 and a cutoff ratio rc = v₃/v₂ = 2. At the start of compression the air is at 300 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 = 19rc = 2T1 = 300 Kk = 1.4
T3 = K
8.Gas power cyclesHard
vP1234qin​qout​

An ideal Brayton cycle operates with a compressor pressure ratio of 12. 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 = 12k = 1.4
η = %

3Solutions

1.Ideal gas law

Answer: P = 141.9 kPa

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

Moles

n = m/M = 20/32 = 0.625 mol
T = 0 + 273.15 = 273.1 K

Pressure

P = nRT/V = 0.625·8.314·273.1/0.01 = 141.9 kPa

Answer

P = 141.9 kPa
2.Ideal gas law

Answer: V2 = 6.874 L

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

Absolute temperatures

T1 = 288.1 K, T2 = 363.1 K

Combined gas law

V2 = V1·(P1/P2)·(T2/T1) = 10·(300/550)·(363.1/288.1) = 6.874 L

Answer

V2 = 6.874 L
3.Energy balance

Answer: tout = 30.07 °C

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

Heat released by the hot stream

Q = 1.5·2.1·(150 − 110) = 126 kW

Heat picked up by the water

tout = tin + Q/(ṁccp,c) = 15 + 126/(2·4.18) = 30.07 °C

Answer

tout = 30.07 °C
4.Energy balance

Answer: ṁc = 1.109 kg/s

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

Heat released

Qh = 1·2.44·(170 − 90) = 195.2 kW

Heat that reaches the water

Qc = (1 − 0.05)·195.2 = 185.4 kW

Water flow rate

ṁc = Qc/(cp,c·Δt) = 185.4/(4.18·40) = 1.109 kg/s

Answer

ṁc = 1.109 kg/s
5.Heat engines & refrigerators

Answer: TL = 39.2 °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 = 775 + 273.15 = 1048 K

Reversible heat ratio

TL = TH·QL/QH = 1048·149/500 = 312.3 K = 39.2 °C

Answer

TL = 39.2 °C
6.Heat engines & refrigerators

Answer: Sgen = 1.341 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 − 1705 = 1395 kJ

Absolute temperatures

TH = 700 + 273.15 = 973.1 K
TL = 35 + 273.15 = 308.1 K

Entropy changes of the reservoirs

ΔSH = −3100/973.1 = −3.186 kJ/K
ΔSL = 1395/308.1 = 4.527 kJ/K
Sgen = 4.527 − 3.186 = 1.341 kJ/K

Answer

Sgen = 1.341 kJ/K

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

7.Gas power cycles

Answer: T3 = 1948 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 = 300·190.4 = 974.1 K

Heat addition at constant pressure

T3 = rc·T2 = 2·974.1 = 1948 K

Answer

T3 = 1948 K
8.Gas power cycles

Answer: η = 50.83 %

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 − 1/120.2857 = 1 − 1/2.034 = 50.83%

Answer

η = 50.83%

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