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Drawing No. EH–TH–016 // Thermal Engineering & HVAC

Heat Exchanger Fouling & Cleaning Calculator

Reviewed August 2026

Estimate how added thermal resistance reduces the overall heat-transfer coefficient and exchanger duty, then compare the recovered duty value with cleaning and downtime costs.

Scope: Screening model for a fixed heat-transfer area and approximately unchanged effective LMTD. It does not replace a full exchanger rating, pressure-drop analysis, process simulation or vendor cleaning assessment.

What this tool does

Enter a clean overall heat-transfer coefficient and either a current fouling resistance or a measured dirty U-value. The tool estimates present duty loss, expected post-cleaning recovery, annual lost value, cleaning payback and net benefit.

Inputs

Use a clean or recently verified baseline on the same area basis.
Use the area basis corresponding to the U-value.
Combined additional resistance on the same U-value basis; include both sides if applicable.
Use corrected LMTD if the exchanger configuration requires an F-factor.
100% restores the clean U-value; lower values leave residual resistance.

Cleaning economics

Often annual operating hours or hours expected before the next shutdown.
Use avoided fuel/utility cost or justified marginal production value.

Results

Cleaning appears economically attractiveExpected recovered value exceeds cleaning and downtime cost over the evaluation period.
Current dirty U-value
606 W/m²·K
24.2% below clean
Current fouling resistance
0.000400 m²·K/W
Total added thermal resistance
Clean duty
960 kW
At entered area and LMTD
Current duty loss
233 kW
24.2% of clean duty
Post-cleaning duty
930.2 kW
203.0 kW recovered
Current lost value
€83,782
Over evaluation operating hours
Total cleaning cost
€20,000
Direct cost plus downtime
Simple payback
1,642 h
68.4 operating days at 24 h/day
Net benefit
€53,066
Recovered value minus cleaning cost
Break-even duty value
€0.0164/kWh
Minimum value for payback within entered hours
Clean
100%
Current
75.8%
After clean
96.9%
Interpretation: A positive net benefit means cleaning recovers more economic value than it costs over the entered evaluation period. Confirm that the duty can actually be monetized or displace utility use before acting.

Thermal resistance and cleaning effect

Fouling adds thermal resistance between the process fluids. Cleaning removes part of that resistance, increasing U and restoring duty.

Simplified fouled heat exchanger diagramA shell-and-tube heat exchanger with a highlighted fouling layer and arrows showing heat transfer before and after cleaning.FOULED EXCHANGERDeposits add resistance: 1/U increasesAFTER CLEANINGLower resistance, higher U and duty

What to do with the result

01
Verify the baseline first

Compare like-for-like flow rates, inlet temperatures and control-valve positions. A low apparent U-value can be caused by maldistribution, bypassing, air binding or bad instruments rather than fouling.

02
Check pressure drop

Thermal fouling and hydraulic restriction often develop together. A rising pressure drop can increase pumping cost and may justify cleaning earlier than the thermal calculation alone.

03
Choose the cleaning method

Confirm compatibility of chemical cleaning, CIP, hydrojetting or mechanical cleaning with plates, tubes, gaskets, metallurgy and deposits.

04
Measure the result

Record pre- and post-cleaning temperatures, flows, pressure drop and calculated U-value. Use the recovered performance to improve the next cleaning decision.

Limitations and model basis

The model is strongest when comparing the same exchanger at similar operating conditions. If flow, phase change, bypassing, LMTD correction factor or available utility temperature changes materially, use a full rating calculation.