Performance complaints are usually one of: lower heat transfer, higher pressure drop, or contamination from a leak. Treat them separately.
Duty lower than design
- Confirm the process case: flow, inlet temperatures, and composition vs the datasheet.
- Check instrumentation (orifice plates, RTDs) before blaming the exchanger.
- Fouling: approach temperatures close up; ΔP often rises.
- Bypass: missing or damaged sealing strips, baffle-to-shell leakage, or a failed longitudinal baffle on F-shells.
- Vapour binding or non-condensables in a condenser vent path.
Pressure drop higher than design
Debris at inlets, crushed packing, collapsed tubes, or severe fouling. Do not raise pump speed as a permanent fix without checking vibration and erosion.
Cross-contamination
Tube leaks, gasket blow-by at the tubesheet, or a cracked pass partition. Isolate, depressurise per procedure, and hydro or dye-check as the ITP allows. Mixing of the two fluids is a safety issue when they are incompatible — treat it as such.
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