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Ammonia Liquid Overfeed & Recirculation Calculator engineering
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Ammonia Liquid Overfeed & Recirculation Calculator

Model pumped ammonia liquid overfeed circulation ratios, pump flow rates, evaporated mass flow, and low-pressure receiver (LPR) surge vessel sizing.

Evaporator System & Temperatures

Coil Holdup & Vessel Retention

Pump Flow & Circulation Rates

Total Pump Flow Rate
-- GPM
-- lbs/min pumped
Evaporated Ammonia Rate
-- lbs/hr
-- GPM equivalent
Un-evaporated Liquid Return
-- GPM
wet return to LPR
Circulation Mass Ratio
-- : 1
pumped to evaporated

Low Pressure Receiver (LPR) Sizing

Evaporator Liquid Operating Holdup: -- Gallons
Liquid Operating Volume in Drum: -- Gallons
Recommended Gross LPR Vessel: -- Gallons
LPR Gross Volume (cu ft): -- cu ft

Hydraulic & Cavitation Advisory

Ammonia liquid in the low-pressure receiver is at saturated boiling temperature. To prevent destructive pump cavitation, the LPR must be elevated to provide at least 4.0 to 6.0 feet of net static liquid head above the centerline of the canned motor pumps (NPSHA > NPSHR).

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Frequently Asked Questions

What is a liquid overfeed (recirculation) ammonia refrigeration system?

In a liquid overfeed system, mechanical pumps circulate liquid ammonia through the evaporator coils at a rate significantly higher than the evaporation rate (typically 3 to 4 times the evaporation rate). The excess liquid ensures that every square foot of internal coil surface remains completely wetted, maximizing heat transfer coefficients.

Why are expansion valves not required on individual evaporator coils in overfeed systems?

Instead of delicate thermostatic or electronic expansion valves prone to superheat hunting and freezing, overfeed evaporators use simple fixed hand expansion valves or orifice plates to distribute liquid. The flow rate is determined by the central liquid pump pressure.

What is the role of the Low-Pressure Receiver (LPR) surge drum?

The LPR acts as both a liquid pump reservoir and a gravity vapor-liquid separator. Wet return vapor and un-evaporated liquid from the coils enter the vessel; the liquid drops down into the pump suction sump, while clean dry vapor rises into the compressor suction header without danger of liquid slugs.

Why must liquid ammonia pumps have substantial static suction head?

Because the liquid in the LPR is at its boiling saturation point, any minor pressure drop in the pump suction line causes the liquid to flash into vapor, resulting in cavitation, seal damage, and lost flow. Elevating the drum 4 to 6 feet above the pump provides the necessary Net Positive Suction Head Available (NPSHA).