Fouling Factor on an Overall Coefficient

1Uf=1Uc+Rf\frac{1}{U_f} = \frac{1}{U_c} + R_f

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A fouling factor is an R-value. Same quantity, same unit, same arithmetic as the insulation on a wall — TEMA simply quotes it as R_f in h·ft²·°F/BTU or m²·K/W and adds it to 1/U. Typical TEMA design values: treated cooling tower water 0.0002 m²·K/W (0.001 in imperial), river water 0.0004, seawater 0.0002, fuel oil 0.0005, and steam 0.00009. The insight the number hides is that fouling hurts a good exchanger far more than a bad one. Take a clean U of 2500 W/(m²·K), which is a plate unit on clean duty: 1/2500 = 0.0004, so a fouling factor of 0.0004 doubles the total resistance and halves the coefficient to 1250. Apply that same 0.0004 to an air-cooled unit at U = 50 and it costs you 2%.

That is why plate exchangers are specified with small fouling allowances and cleaned in place instead, while shell-and-tube units carry generous ones — and it is where the specification trap lives. Fouling allowance is bought as extra surface, and extra surface on a water-cooled unit means lower velocity in the tubes, which fouls faster. Over-specifying R_f is self-fulfilling; 20–30% excess surface is common and defensible, 100% is a fouling machine. The field version of this equation runs backwards: measure the duty and the LMTD, back out the service U, and R_f = 1/U_f − 1/U_c is the deposit you have accumulated since commissioning. When that number reaches the design allowance, the exchanger is due for cleaning — that is what the design fouling factor was always for, and it is a maintenance trigger, not a safety factor.

Fouling Factor on an Overall Coefficient
1Uf=1Uc+Rf\frac{1}{U_f} = \frac{1}{U_c} + R_f
Where
  • UfU_f= Fouled (service) coefficient
  • UcU_c= Clean coefficient
  • RfR_f= Fouling factor
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