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Overall Heat Transfer Coefficient and the Heat Transfer Equation Q=K·A·ΔTm

Aug 13, 2026 60 views ~10 min read Technical Knowledge
The overall heat transfer capacity of a heat exchanger is summarized by Q = K·A·ΔTm: K is the overall heat transfer coefficient, A is the area, and ΔTm is the logarithmic mean temperature difference. K consists of the series combination of the convective thermal resistances on both sides and the wall resistance; raising K or A both increase heat transfer, but at different costs.

I. The "Master Equation" of Heat Exchanger Design

No matter how complex the heat exchanger, steady-state heat transfer can be written as:

Q = K · A · ΔTm

K is the overall heat transfer coefficient (W/m²·K), A is the heat transfer area, and ΔTm is the mean temperature difference (usually the logarithmic mean, covered next). This equation is the "quotation" for selection: to transfer a given amount of heat Q, either make K large, make A sufficient, or raise the temperature difference.

II. K Is the Sum of the Reciprocals of Layer-by-Layer Thermal Resistances

Heat from the hot fluid to the cold fluid passes sequentially through: hot-side convection → wall conduction → cold-side convection. The total thermal resistance is added in series:

1/K = 1/h_hot + δ/λ + 1/h_cold (+ fouling thermal resistance)

Whichever link is largest dominates the whole. Common situations:

  • Air-to-air heat exchange: Both h are small, 1/h dominates; raising flow velocity and adding disturbance is most effective;
  • Air-to-water heat exchange: Air-side h is far smaller than water-side, so optimization is almost entirely on the air side;
  • Long-running equipment: Fouling thermal resistance gradually grows and becomes the main factor later.

III. Raise K or Add A?

MethodAdvantageCost
Raise K (speed up, disturb flow)Compact equipment, small footprintRising pressure drop and fan power
Add A (larger plates)Low temperature difference demand, small pressure dropMore expensive and space-consuming equipment

Actual design is a combination: first use channel design to raise K to a reasonable level, then use A to make up the remaining heat. Blindly piling up area produces big, expensive equipment; blindly increasing speed lets fan electricity bills eat the energy-saving gains.

IV. A Quick Check

For any heat exchange scheme, first ask: What is K? How big is A? What is ΔTm? Does their product equal the Q you need? If not, the scheme is inflated. Break K into three thermal resistances and you immediately know which side is the bottleneck.


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Keywords: overall heat transfer coefficient heat transfer equation series thermal resistance K value heat transfer area heat exchanger design
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