Technical note
Equipment is a third of the job. Take-off points, pump and piping, power, drainage, access and transition plan must all be settled first.
Retrofitting electrochemical treatment into an existing system is a third equipment and two-thirds site conditions. The six checks below must be confirmed before work starts; miss one and commissioning is likely to stall.
The take-off should sit on the cooling tower return header or near the basin where flow is stable; the return should re-enter upstream of the pump suction to avoid short-circuiting. A take-off in a dead zone, or a return next to the suction, will cut treatment effectiveness sharply. Review the piping drawings before deciding where to cut.
The equipment has rated flow and allowable pressure drop. Size the pump for the worst case (fouled filters, scaled piping), not for a new pipe. Small diameters and too many elbows push actual flow below design. Install a flow meter on the side-stream line and commission against measured flow.
The unit is a DC load and needs stable power and earthing. The control cabinet should be dry, ventilated and easy to observe, and cable runs to the unit should be checked for voltage drop. If only temporary power is available on site, fix it first; nuisance tripping during commissioning will wreck the schedule.
Blowdown from the unit (concentrated calcium, magnesium and deposits) needs a defined destination: sewer, settling tank or recovery system, agreed with the owner in advance. It must not go to a storm drain or back to the tower basin. Slope and diameter of the drain must handle the momentary flow during flushing.
Allow room to pull plates, replace electrodes and clean. Many sites squeeze the unit into a corner, and the first cleaning requires dismantling piping. Reserve the maintenance space specified by the manufacturer, and consider lifting and transport access.
Provide sampling and on-line monitoring positions for at least free chlorine, pH, conductivity and turbidity. Do not stop chemicals immediately: design a transition from chemical plus electrochemical operation, through phased reduction, to confirmation by monitoring data — with acceptance indicators agreed up front (corrosion rate, exchanger temperature difference, colony counts, scale mass).
Equipment selection sets the ceiling; site conditions decide whether it lands. Write these six items into a checklist, sign each one before work starts, and the retrofit costs far less than reworking it later.
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This note covers method and limits only; no unverified case data is quoted.