Fouling occurs when minerals, rust, biofilm, or process residues deposit on plate surfaces. Even a thin layer reduces heat transfer and forces higher energy consumption to maintain duty. Scaling is a hard-water subtype that forms crystalline layers and becomes difficult to remove if ignored.
Leakage in gasketed PHE is usually caused by gasket aging, chemical attack, thermal cycling, or incorrect tightening. Small leaks reduce efficiency and can become cross-contamination risks.
Corrosion mechanisms include pitting (chlorides), crevice corrosion (stagnant zones), and stress corrosion cracking. Correct material selection is the most effective prevention strategy.
- 316L: general industrial service with moderate chlorides
- Titanium: seawater / high chloride environments
- SMO: harsh cooling water with higher chlorides
- C276 / Ni alloys: aggressive chemical duty
PHE channels are narrow by design. If the exchanger is undersized or fouled, pressure drop rises and pump power increases. Incorrect piping, air lock, or flow imbalance can also cause abnormal ΔP.
Frequent start/stop cycles and large temperature swings create cyclic stress in plates and gaskets. Over time, this can cause deformation, gasket blowout, or micro-cracks.
FAQ (Click to Expand)
What are the first signs of fouling in a plate heat exchanger?
Common early signs include rising approach temperature, gradually increasing pressure drop, and higher pump power. Trend data is the fastest warning.
Why does a gasketed plate heat exchanger start leaking after stable operation?
Typical causes include gasket compression set, chemical incompatibility, thermal cycling, misalignment, or incorrect tightening. Re-torque to spec and confirm gasket compound.
How do I choose gasketed vs brazed plate heat exchangers?
Gasketed PHEs are serviceable and ideal for larger duties and dirty fluids. Brazed PHEs are compact and leak-resistant (no gaskets), often used in refrigeration and closed loops.
Which plate material is best for high-chloride water or seawater?
Titanium is common for seawater. SMO or other corrosion-resistant alloys may fit high-chloride industrial water depending on temperature and oxidizers.
How can I reduce pressure drop without losing heat transfer?
Clean fouling first, then optimize plate pattern and size with ΔP margin. Flow balancing and correct piping often solve “hidden” ΔP problems.

