Vapour-compression multi-stage evaporation, usually tied to a waste-heat source. Catalogued for orientation; EngiMetric models no MED thermal or performance figures.
- Information only
- Not quantitatively modeled
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Desalination driven by low-grade heat already available on site, typically from power generation or process exhaust. Orientation only.
Desalination driven by low-grade heat already available on site, typically from power generation or process exhaust. Orientation only.
Separation mechanism and feed window. As for the underlying thermal cycle.
What the process produces. Very low TDS distillate.
Energy. Low-grade recovered heat. The economics depend almost entirely on the heat being otherwise wasted.
Where this technology normally sits in a treatment train. The steps either side of it are documented in the Library as separate entries.
The parameters an engineer actually sets, and why each one drives the design. EngiMetric does not assume any of them.
| Parameter | Why it matters |
|---|---|
| Available waste-heat flow and temperature | The entire feasibility case. |
| Temperature approach | How much of the available heat is actually recoverable. |
| Duty matches the heat source | The cycle must run at the availability of the source, not its peak. |
Industry maturity and commercial status describe the technology itself. EngiMetric support and quantitative modeling describe what this platform does with it — and those two are read from the engineering registry at build time, so they cannot drift from the code.
Not quantitatively modeled. EngiMetric publishes no energy, recovery, flux, capacity or cost figure for this technology. Every quantitative statement on this page comes from your own inputs or from an external source, never from a calculation on this platform.
Because no EngiMetric engine exists for Waste-Heat Desalination, this page deliberately contains no calculated figures. Any energy, recovery, flux or capacity value you need must come from a supplier, a published plant or your own analysis.