CDU Filter Pressure-Drop Calculation Example
The following is a simplified example to show how a filter pressure-drop budget can be built. The actual values should come from the pump curve, system component data, and filter test data.
At the design point, assume a TCS flow rate of 500 GPM and a pump differential pressure of 12 psi.
Pressure losses elsewhere in the TCS are estimated as follows:
- Heat exchanger: 3.0 psi
- Piping and fittings: 2.0 psi
- Manifold and connections: 1.5 psi
- Other components: 1.0 psi
Total: 7.5 psi
Pump differential pressure at the design point: 12 psi
Pressure available for filter + operating margin: 4.5 psi
At 500 GPM, a filter with a clean pressure drop of 1.2 psi would bring the total system loss to 8.7 psi, leaving 3.3 psi of available margin.
Filter loading changes this balance. With the filter at 2.5 psi ΔP, total system pressure loss is 10 psi, with 2 psi remaining as operating margin.
This is why filter pressure drop should be considered beyond the clean condition. The expected operating condition and available pressure margin also need to be checked as part of the overall TCS design.
The actual allowable pressure drop will vary with the system and should not be treated as a fixed value for every CDU application.
How to Build the Pressure-Drop Budget
A practical review can start with four steps.
1. Determine the Required Flow
Start with the TCS design flow and the expected operating range.
The filter pressure drop should be checked at the actual design flow and, where relevant, at the highest expected operating flow.
2. Determine Available Pump Pressure
Look at the pump curve at the required flow rate. The differential pressure at this point is the value used in the calculation.
The pump’s maximum pressure rating is not used unless the system actually operates at that point.
3. Calculate Other System Losses
Pressure drop from the heat exchanger, piping, valves, fittings, manifolds, and other TCS components forms the remainder of the system-side losses.
4. Evaluate the Filter
Check the filter ΔP at the design flow against the pressure remaining after the other system losses.
The clean ΔP is only the starting point. The expected increase in ΔP during operation also needs to be allowed for.
This approach helps determine whether the selected filter provides sufficient flow capacity without using an excessive portion of the available pressure.
Low-Pressure-Drop CDU Filter Selection
A low-pressure-drop CDU filter should be evaluated as part of the overall filtration and hydraulic design.
The goal is not simply to choose the filter with the lowest ΔP. The filter still has to meet the particle-control and flow requirements of the TCS, while working with the selected coolant and the space available for installation and maintenance.
A filter curve showing low clean ΔP does not tell the whole story. The pressure drop at the design flow, the change in ΔP as the filter collects contaminants, and the pressure available in the TCS all matter when comparing filter options.
The final selection should balance filtration performance, pressure drop, filtration area, filter life, installation space, and maintenance requirements.