| Feed-water quality | EDI receives low-ion water, most commonly permeate produced by reverse osmosis (RO). | RO permeate; actual limits for conductivity, hardness, silica, carbon dioxide, and other constituents depend on the EDI module. | Provides the controlled feed needed for effective continuous deionization. | Check the module’s feed-water specification and the complete pretreatment design. EDI is generally not intended to treat untreated source water directly. |
| Ion-exchange resin | Resin beads temporarily capture dissolved cations and anions, helping transport ions through the dilute compartment. | Dissolved ionic contaminants in the RO permeate. | Supports ion removal between the membrane barriers. | Feed quality and flow distribution affect performance. Resin does not make EDI a general-purpose filter for suspended solids or organic contaminants. |
| Ion-exchange membranes | Alternating cation- and anion-selective membranes guide positively and negatively charged ions toward concentrate compartments. | Ions migrate out of the product-water stream into a separate concentrate stream. | Separates ionic contaminants from the water being purified. | Membranes are selective for charged species; they do not replace particle filtration or organic-contaminant treatment. |
| Direct-current field | An applied DC electric field drives ion migration through the resin and across the selective membranes. | Electrical power and properly conditioned feed water. | Enables continuous ion removal and helps regenerate the resin during operation. | Voltage, current, temperature, and flow must remain within the equipment manufacturer’s operating limits. |
| Continuous resin regeneration | The electric field splits a small amount of water into hydrogen and hydroxide ions, which help restore the resin’s ion-exchange capacity. | Hydrogen and hydroxide ions are formed within the EDI stack. | Allows the unit to operate continuously without routine chemical regeneration of the EDI resin. | “Chemical-free regeneration” applies to the EDI process itself; the wider water-treatment plant may still use chemicals for pretreatment or cleaning. |
| Dilute and concentrate streams | The dilute stream becomes the purified product, while the concentrate stream carries removed ions away from the stack. | Separate product-water and concentrate-water outlets. | Provides a continuous route for removing contaminants rather than storing them in the product stream. | Concentrate flow, recovery, and disposal or reuse arrangements are system-specific and should be confirmed during design. |
| Product-water quality | EDI reduces dissolved ionic species after RO; performance is monitored using suitable water-quality instruments. | High-purity water; some well-designed systems can produce water approaching 18.2 MΩ·cm resistivity at 25°C under appropriate conditions. | Provides a polishing step for applications requiring low ionic contamination. | Resistivity alone does not establish overall water purity. Silica, boron, dissolved gases, organics, particles, and microbiological quality may require separate monitoring or treatment. |
| Typical process sequence | Common arrangement: pretreatment → RO → EDI → storage and distribution, with additional polishing where the application requires it. | Each stage is selected for the source water and the final quality requirement. | Places EDI after RO as a polishing technology rather than as a standalone treatment train. | Final design depends on source-water analysis, required product-water quality, demand, sanitization needs, and applicable regulations. |
| Monitoring and maintenance | Operators track feed and product quality, flow, pressure, temperature, and electrical readings; pretreatment and instrumentation are maintained. | Routine operating data and water-quality measurements. | Helps identify feed-water changes, scaling or fouling risks, and declining performance. | Use the supplier’s operating and maintenance guidance, and verify product quality with calibrated instruments and appropriate sampling practices. |