Vacuum Distillation • Jacket-Water Heat • Condenser Duty • Ejector Performance • Salinity Control • Distillate Production • Fouling • Low-Load Capacity

Marine Freshwater Generator Capacity, Vacuum & Distillate Production Tool

Screen a shipboard vacuum freshwater generator as a complete heat-and-mass balance. Simple mode estimates production from jacket-water heat, vacuum boiling temperature, equipment capacity and salinity status. Advanced mode compares multiple operating points, evaporation and condensation limits, brine concentration, fouling, ejector/vacuum condition, distillate demand and measured performance.

Figures represent
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Fast performance screen with 9 inputs.The tool estimates gross distillate production from available jacket-water heat and the measured vacuum condition, caps production at the entered OEM capacity, and separately decides whether that distillate is accepted or diverted based on the entered salinity limit.
VacuumPressure → boiling temperature
HeatJacket-water evaporation duty
QualityAccept or divert distillate

Freshwater Generator Condition

m³/day at the maker's stated reference condition.
m³/h.
°C.
°C.
°C. Used for condenser-temperature context.
kPa absolute. About 12.3 kPa corresponds to ~50°C saturation temperature.
% effective thermal condition after fouling / scaling allowance.
ppm or mg/L as displayed by the vessel instrument.
User-entered vessel / maker setting.

Unit & Operating Limits

m³/day.
kPa absolute.
°C between jacket-water outlet and boiling temperature.
°C between boiling temperature and seawater outlet.
ppm / mg/L, user-entered.
m³/day.
g/kg or ppt for brine concentration estimate.
Feed volume divided by gross distillate volume.
g/kg or ppt, user-entered scale / concentration reference.

Equipment Condition Factors

% of clean/reference performance.
% of clean/reference performance.
% quality / carryover effectiveness applied to gross production.
% condition indicator used diagnostically, not as a hidden capacity multiplier.

Operating Point Register

Enter measured or planned conditions. Evaporator heat is taken from jacket-water flow × ΔT. Condenser duty is taken from seawater flow × ΔT. The lower thermal-side production limit governs before the OEM capacity cap.

UsePointShare %JW flow m³/hJW in °CJW out °CSW flow m³/hSW in °CSW out °CAbs press kPaSalinity ppmMeasured m³/d

Operational Checks

Engineering boundary: this tool screens vacuum-evaporator capacity and operating condition. It does not replace the maker's performance curves, commissioning data, salinometer calibration, potable-water treatment requirements, or vessel-specific operating procedures.
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