น้ำเย็นและระบบทำความเย็นสายเครื่องดื่ม

Calculate load by time for product pull-down, continuous processing, carbonator duty, cold rooms and simultaneous CIP recovery.

State supply, return and product temperatures plus exchanger approach. A low chiller setpoint cannot correct undersized heat-transfer area.

Use credible maximum ambient and condenser conditions for the destination. Separate nominal catalog rating from site-derated capacity.

Review pump curve, pressure drop, bypass, minimum chiller flow and the response as users open or close.

Define corrosion, scaling, biocide, glycol where needed, filtration and compatibility with heat exchangers and seals.

Size storage from load swings and chiller control behavior, then verify recovery after the largest credible production event.