Hong Kong PHE: Treated Clear, Untreated Blocked 3 ft

Home 9 Case Studies and Results 9 Hong Kong PHE: Treated Clear, Untreated Blocked 3 ft
Key results
Treated PHE largely unblocked
Untreated blocked to 3 ft
14-18% higher seawater flow

Case Study from Hydropath Asia

Plate heat exchanger macrofouling on Hong Kong seawater cooling

Plate heat exchanger macrofouling was blocking the seawater channels of a Hong Kong building‘s PHEs despite screening and chlorination. Mussels and barnacles restricted flow, biofilm impaired heat rejection, higher differential pressure drove up pumping demand, and discharge limits capped residual chlorine. A HydroFLOW® unit was first fitted at the PHE02 inlet. Once upstream fouling was identified, a custom 24 inch unit was repositioned to the header-pipe outlet to PHE02, with untreated PHE01 as the comparator from 22 February to 30 August 2023. After six months PHE02 remained largely open while PHE01 was blocked to a depth of 3 ft, and PHE02 maintained 14 to 18% higher seawater flow.

The Challenge

  • Plate heat exchanger macrofouling blocked seawater channels despite screening and chlorination
  • Mussels and barnacles restricted the seawater channels
  • Biofilm impaired heat rejection across the PHE plates
  • Higher differential pressure increased pumping demand
  • Discharge limits restricted how much residual chlorine could be used

Untreated comparison plate heat exchanger PHE01, fouled in November 2022 and later blocked with shells and silt, Hong Kong
The Solution

  • Unit installed: HydroFLOW® custom 24 inch
  • Installation point: header-pipe outlet to PHE02, moved from the PHE02 inlet
  • Trial: untreated PHE01 as comparator, 22 February to 30 August 2023

The trial set treated PHE02 against untreated PHE01 so plate heat exchanger macrofouling could be compared side by side. The unit was first fitted at the PHE02 inlet. When fouling was found upstream, the custom 24 inch unit was moved to the header-pipe outlet to PHE02 to extend treatment across the affected pipework. Both exchangers were then compared at the final inspection.

Key Outcomes

R

Final inspection found far less water-channel blockage in treated PHE02

R

PHE02 remained largely open while PHE01 was blocked to a depth of 3 ft

R

After six months, biofilm on treated PHE02 was visibly thinner than on untreated PHE01

R

Treated PHE02 maintained 14–18% higher seawater flow and lower differential pressure

Independent Verification

All results in this study were measured and verified by third-party facilities managers and technical staff.

Summary

After six months the untreated exchanger was blocked to a depth of 3 ft while the treated one remained largely open, with visibly thinner biofilm and lower differential pressure. For seawater-cooled buildings limited on residual chlorine, this side-by-side comparison is the reference: the treated and untreated exchangers ran over the same period, so the difference shows at the inspection. The Hong Kong seawater chillers post is the companion piece.

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