Electric-field separation of ions through ion-exchange membranes. Relevant to salt production from brine; not modeled.
- Information only
- Not quantitatively modeled
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Electrodeionisation by adsorption in an electric field, effective at very low salinity. Research/early-commercial; not modeled.
Electrodeionisation by adsorption in an electric field, effective at very low salinity. Research/early-commercial; not modeled.
Separation mechanism and feed window. Requires very low feed salinity, typically below RO permeate; used as a polisher.
What the process produces. Very low conductivity water.
Energy. Electrical. Energy per unit salt removed rises as feed salinity falls.
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 |
|---|---|
| Feed salinity | The usefulness of CDI falls as feed salinity rises. |
| Energy per unit salt removed | The decisive economic number. |
| Stack gap and spacer | Governs the achievable current density. |
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 Capacitive Deionization, 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.