When sizing a shell and tube heat exchanger or a plate heat exchanger, it is critical to account for the buildup of material on the tube surface. This thermal resistance is called the Fouling Factor (\(R_f\)).
The overall heat transfer coefficient (\(U\)) including fouling is calculated as:
\[ U_{dirty} = \frac{1}{\frac{1}{U_{clean}} + R_f} \]Where:
Please find below the reference values used in the calculator. Note: Data is for preliminary estimation only.
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1. Compressor Power
2. Pump Power
3. Pipe Pressure Drop
4. Fluid Velocity
5. Churchill Correlation
| Water Type | Heating ≤115.5°C Water ≤51.6°C Vel ≤0.9m/s |
Heating ≤115.5°C Water ≤51.6°C Vel >0.9m/s |
Heating >115.5°C Water >51.6°C Vel ≤0.9m/s |
Heating ≤115.5°C Water >51.6°C Vel >0.9m/s |
|---|---|---|---|---|
| Units | (m².K/W) | |||
| Boiler Blowdown | 0.0003526 | 0.0003526 | 0.0003526 | 0.0003526 |
| Brackish Water | 0.0003526 | 0.0001763 | 0.0005289 | 0.0003526 |
| Condensate | 8.815E-05 | 8.815E-05 | 8.815E-05 | 8.815E-05 |
| Cooling Tower (Treated) | 0.0001763 | 0.0001763 | 0.0003526 | 0.0003526 |
| River Water (Avg) | 0.0005289 | 0.0003526 | 0.0007052 | 0.0005289 |
| Sea Water | 8.815E-05 | 8.815E-05 | 0.0001763 | 0.0001763 |