Heat conduction
- Fourier’s law
- Q̇ = kAΔT/L
- Conduction resistance
- R = L/(kA)
- Convection resistance
- R = 1/(hA)
- Resistances in series
- Q̇ = ΔTtotal/ΣR
- U-value
- U = 1/(ΣR·A)
Heat Transfer: cram pack
Formula sheets, the key method steps for every topic and 4 practice problems, with full solutions at the back.
1Formulas and methods
Heat exchangers (LMTD)
- Heat duty
- Q = U·A·ΔTlm
- Log mean temperature difference
- ΔTlm = (ΔT1 − ΔT2)/ln(ΔT1/ΔT2)
- Stream balance
- Q = ṁcp(Tin − Tout)
2Practice problems
1.Heat conductionMedium
A wall is made of 200 mm of glass and 50 mm of concrete, with an area of 15 m². The outer faces are at 24 °C and -2 °C. Find the heat flow Q̇ through the wall.
L1 = 200 mm, k1 = 0.96 W/(m·K)L2 = 50 mm, k2 = 1.4 W/(m·K)A = 15 m²T1 = 24 °CT3 = -2 °C
Q̇ = W
2.Heat conductionHard
A wall of 100 mm gypsum board and 25 mm concrete separates a room at 22 °C from outside air at -3 °C. The convection coefficients are 6 W/(m²·K) inside and 25 W/(m²·K) outside, and the wall area is 10 m². Find the overall heat transfer coefficient U of the wall.
L1 = 100 mm, k1 = 0.17 W/(m·K)L2 = 25 mm, k2 = 1.4 W/(m·K)A = 10 m²hi = 6 W/(m²·K)ho = 25 W/(m²·K)Troom = 22 °CTout = -3 °C
U = W/(m²·K)
3.Heat exchangers (LMTD)Medium
A parallel-flow heat exchanger transfers 110 kW. The hot fluid cools from 125 to 95 °C and the cold fluid heats from 30 to 60 °C. The overall heat transfer coefficient is 200 W/(m²·K). Find the heat transfer area A needed.
Q̇ = 110 kWU = 200 W/(m²·K)Th: 125 → 95 °CTc: 30 → 60 °C
A = m²
4.Heat exchangers (LMTD)Hard
In a counter-flow double-pipe heat exchanger, hot oil (0.3 kg/s, cp = 2.3 kJ/(kg·K)) flows in the inner tube and cools from 130 to 80 °C. Water (0.8 kg/s, cp = 4.18 kJ/(kg·K)) in the annulus enters at 15 °C. The inner tube has a diameter of 20 mm, and U = 150 W/(m²·K) is based on this diameter. Find the tube length L needed.
ṁh = 0.3 kg/scp,h = 2.3 kJ/(kg·K)Th: 130 → 80 °Cṁc = 0.8 kg/sTc,in = 15 °CD = 20 mmU = 150 W/(m²·K)
L = m
3Solutions
1.Heat conduction
Answer: Q̇ = 1598 W
Thermal resistance: steady heat flow through layers in series behaves like current through resistors in series: Q̇ = ΔT/ΣR, with R = L/(kA) for a conducting layer and R = 1/(hA) for a convecting surface. The temperature drop across each layer is proportional to its resistance.
Layer resistances
R1 = L1/(k1A) = (200/1000)/(0.96·15) = 0.01389 K/W
R2 = L2/(k2A) = (50/1000)/(1.4·15) = 0.002381 K/W
Heat flow
Q̇ = (T1 − T3)/(R1 + R2) = 26/0.01627 = 1598 W
Answer
Q̇ = 1598 W
2.Heat conduction
Answer: U = 1.23 W/(m²·K)
Thermal resistance: steady heat flow through layers in series behaves like current through resistors in series: Q̇ = ΔT/ΣR, with R = L/(kA) for a conducting layer and R = 1/(hA) for a convecting surface. The temperature drop across each layer is proportional to its resistance.
Resistances in series
Ri = 1/(hiA) = 1/(6·10) = 0.01667 K/W
R1 = L1/(k1A) = (100/1000)/(0.17·10) = 0.05882 K/W
R2 = L2/(k2A) = (25/1000)/(1.4·10) = 0.001786 K/W
Ro = 1/(hoA) = 1/(25·10) = 0.004 K/W
ΣR = 0.08128 K/W
Overall coefficient
U = 1/(A·ΣR) = 1/(10·0.08128) = 1.23 W/(m²·K)
Answer
U = 1.23 W/(m²·K)
3.Heat exchangers (LMTD)
Answer: A = 9.153 m²
LMTD method: the temperature difference between the streams changes along the exchanger, so the rate equation uses its logarithmic mean: Q̇ = U·A·ΔTlm, with ΔTlm = (ΔT₁ − ΔT₂)/ln(ΔT₁/ΔT₂), where ΔT₁ and ΔT₂ are the differences at the two ends. Counter-flow gives a larger ΔTlm than parallel flow for the same inlet and outlet temperatures.
End temperature differences
In parallel flow both inlets are at the same end, and both outlets at the other.
ΔT₁ = Th,in − Tc,in = 125 − 30 = 95 K
ΔT₂ = Th,out − Tc,out = 95 − 60 = 35 K
Log-mean temperature difference
ΔTlm = (ΔT₁ − ΔT₂)/ln(ΔT₁/ΔT₂) = (95 − 35)/ln(95/35) = 60.09 K
Area
A = Q̇/(U·ΔTlm) = 110000/(200·60.09) = 9.153 m²
Answer
A = 9.153 m²
4.Heat exchangers (LMTD)
Answer: L = 43.96 m
LMTD method: the temperature difference between the streams changes along the exchanger, so the rate equation uses its logarithmic mean: Q̇ = U·A·ΔTlm, with ΔTlm = (ΔT₁ − ΔT₂)/ln(ΔT₁/ΔT₂), where ΔT₁ and ΔT₂ are the differences at the two ends. Counter-flow gives a larger ΔTlm than parallel flow for the same inlet and outlet temperatures.
Heat duty and water outlet temperature
Q̇ = 0.3·2.3·(130 − 80) = 34.5 kW
Tc,out = 15 + 34.5/(0.8·4.18) = 25.32 °C
End temperature differences
In counter-flow the hot inlet faces the cold outlet, and the hot outlet faces the cold inlet.
ΔT₁ = Th,in − Tc,out = 130 − 25.32 = 104.7 K
ΔT₂ = Th,out − Tc,in = 80 − 15 = 65 K
Log-mean temperature difference
ΔTlm = (ΔT₁ − ΔT₂)/ln(ΔT₁/ΔT₂) = (104.7 − 65)/ln(104.7/65) = 83.27 K
Area and length
A = 34500/(150·83.27) = 2.762 m²
L = A/(πD) = 2.762/(π·0.02) = 43.96 m
Answer
L = 43.96 m
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