Recovering salts such as sodium chloride from a concentrate. Orientation only; EngiMetric models no crystallization or product-yield calculation.
- Information only
- Not quantitatively modeled
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Electric-field separation of ions through ion-exchange membranes. Relevant to salt production from brine; not modeled.
Electric-field separation of ions through ion-exchange membranes. Relevant to salt production from brine; not modeled.
Separation mechanism and feed window. Needs conductive feed; performance degrades sharply at very low salinity.
What the process produces. A concentrate enriched in the target salt and a depleted diluate.
Energy. Electrical, proportional to the salt transferred.
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 |
|---|---|
| Current density | Governs ion transfer rate. |
| Membrane area | Sets total transfer capacity. |
| Energy per tonne of salt | The commercial decision metric. |
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 Electrodialysis, 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.