Thermal engineering · Heat transfer · conduction

Overall heat-transfer coefficient through a wall

Calculate hot-fluid → wall → cold-fluid heat transfer by combining both convection resistances with conduction through one plane wall.

Created v1.0

By Thibaut Grzelak, Mechanical Analysis Engineer

Heat transfer · conduction
01Calculation inputs
T∞,hT∞,chₕh𝒸keQ̇, q″
1/U = 1/hₕ + e/k + 1/h𝒸Calculate hot-fluid → wall → cold-fluid heat transfer by combining both convection resistances with conduction through one plane wall.
W/(m²·K)
W/(m²·K)
W/(m·K)
02

Results

U
Heat flux q″
—W/m²

Heat-transfer rate per unit area.

Overall conductance U
—W/(m²·K)

Overall area conductance including both convection films and the wall.

Total area resistance R″tot
—m²·K/W

Sum 1/hₕ + e/k + 1/h𝒸.

Total thermal resistance Rtot
—K/W

Overall thermal resistance for the entered area.

R″h = — · R″wall = — · R″c = —

Steady-state, one-dimensional heat transfer through a plane wall. The convection coefficients hₕ and h𝒸 are prescribed and uniform over the area.

01Formulas and symbols

Formulas used

R″h1 / hₕHot-side convective resistance
R″walle / kWall conductive resistance
R″c1 / h𝒸Cold-side convective resistance
U1 / (1/hₕ + e/k + 1/h𝒸)Overall heat-transfer coefficient
Q̇U · A · ΔT∞Total heat-transfer rate
R″hR″wallR″cΔTₕΔTwallΔT𝒸
02Assumptions and limits

Scope of validity

  • Steady-state, one-dimensional heat transfer through a plane wall.
  • The convection coefficients hₕ and h𝒸 are prescribed and uniform over the area.
  • The wall is homogeneous with constant thermal conductivity k and no internal heat generation.
  • T∞,h and T∞,c are bulk-fluid temperatures, not wall-surface temperatures.
  • Radiation, contact resistance, thermal bridges, fouling and lateral conduction are excluded.
  • The calculated U applies only to the entered model and is not a regulatory building or heat-exchanger rating.
03Validation example

Reference numerical case

  1. Reference case: hₕ = 10, h𝒸 = 25 W/(m²·K), k = 0.5 W/(m·K), e = 0.10 m, A = 10 m² and ΔT∞ = 20 K.
  2. R″h = 0.10; R″wall = 0.20; R″c = 0.04 m²·K/W, so R″tot = 0.34 m²·K/W.
  3. U = 2.941176 W/(m²·K) and q″ = 58.823529 W/m².
  4. Q̇ = 588.235294 W and Rtot = 0.034 K/W.
04References

Technical references

  1. Incropera et al. — Fundamentals of Heat and Mass Transfer: convection and plane-wall thermal-resistance circuits.
  2. NIST Special Publication 811 — SI units and temperature intervals.