Back to Water glossary

Water glossary

Electrodialysis Deionization (EDI) for High-Purity Water Production

Explore Electrodialysis Deionization (EDI) technology, its working principles, applications in high-purity water treatment, and key advantages and disadvantages.

Introduction to Electrodialysis Deionization (EDI)

High-purity water production has historically relied on a combination of membrane separation and ion exchange processes. Electrodialysis Deionization (EDI) represents an advanced evolution, integrating semi-permeable membrane technology with ion-exchange media to deliver a highly efficient demineralization solution.

What is EDI?

EDI is a continuous, chemical-free process that utilizes an electrical current and specialized ion-selective membranes to transport and separate charged ionic species from water. Unlike traditional ion exchange, EDI continuously regenerates its resin beds using the applied electrical field, eliminating the need for periodic chemical regeneration with acids and caustics. This approach significantly reduces operational costs, environmental impact, and chemical handling. The EDI process can produce industrial process water of very high purity, reducing chemical consumption by over 95% compared to conventional ion exchange systems.

How EDI Works

An EDI stack fundamentally consists of a series of alternating diluting and concentrating compartments, separated by ion-selective membranes, with ion exchange resin packed into the diluting compartments.

  1. Structure: Each deionization chamber contains mixed-bed ion exchange resins positioned between a cation exchange membrane (CEM) and an anion exchange membrane (AEM). These membranes are selectively permeable, allowing only specific charged ions to pass while restricting water flow.
  2. Ion Removal: As feedwater enters the resin-filled diluting compartment, strong ions are initially captured by the mixed-bed resins. Under the influence of a strong direct current (DC) electric field applied across the stack, these charged ions are drawn off the resin and migrate towards the respective oppositely-charged electrodes.
  3. Concentration: Cations pass through the CEM into the adjacent concentrating compartment, while anions pass through the AEM into a separate adjacent concentrating compartment. They are then blocked from further migration by the subsequent membrane (e.g., cations are blocked by an AEM, and anions by a CEM), thus becoming trapped and concentrated in these compartments, which are continuously flushed with a concentrate stream.
  4. Water Splitting and Regeneration: As strong ions are removed, the conductivity of the water in the diluting compartment becomes very low. The strong electrical potential then causes water molecules to split at the surface of the resin beads, producing hydrogen (H+) and hydroxyl (OH-) ions. These continuously generated H+ and OH- ions serve as in-situ regenerating agents for the ion-exchange resin.
  5. Weak Ion Removal: The regenerated resins, now in H+ and OH- forms, can ionize neutral or weakly-ionized aqueous species like carbon dioxide (CO2) or silica (SiO2). These newly ionized species are then similarly removed through the direct current field and ion exchange membranes.

The ionization reactions occurring in the resin for the removal of weakly ionized compounds are:

  • CO₂ + OH⁻ → HCO₃⁻
  • HCO₃⁻ + OH⁻ → CO₃²⁻
  • SiO₂ + OH⁻ → HSiO₃⁻
  • H₃BO₃ + OH⁻ → B(OH)₄⁻
  • NH₃ + H⁺ → NH₄⁺

Key Applications of EDI Systems

EDI is ideal for any application requiring consistent and economical removal of water impurities without the use of hazardous chemicals. Common applications include:

  • Reuse of residual water in the food and beverages industry
  • Chemical production
  • Biotechnology
  • Electronics manufacturing
  • Cosmetic product formulation
  • Laboratory-grade water production
  • Pharmaceutical industry
  • Boiler feedwater treatment
  • Reduction of ionizable silica (SiO₂) and total organic carbon (TOC)

Advantages of Electrodialysis Deionization

EDI offers significant advancements over traditional ion exchange systems, providing both economic and environmental benefits for high-purity water treatment:

  • Continuous Operation: Provides a constant flow of high-purity water without downtime for regeneration cycles.
  • Chemical-Free Regeneration: Eliminates the need for hazardous acid and caustic chemicals, enhancing safety and reducing environmental impact.
  • Cost-Effective: Low operating and maintenance costs due to reduced chemical consumption, waste neutralization, and labor for regeneration.
  • Low Power Consumption: Efficient use of electrical energy for ion removal and resin regeneration.
  • Environmental Benefits: Reduces chemical discharge and associated pollution.
  • Simplified Automation: Requires fewer automatic valves and complex control sequences compared to batch ion exchange systems.
  • Compact Footprint: Demands less space than traditional ion exchange systems.
  • High Purity Output: Capable of producing exceptionally pure water with near-complete removal of dissolved inorganic particles.
  • Enhanced RO Performance: When combined with reverse osmosis (RO) pretreatment, EDI can remove over 99.9% of ions from the water.

Limitations and Considerations for EDI

While highly effective, EDI systems have specific limitations that necessitate proper feedwater pretreatment:

  • Hardness Sensitivity: EDI units are generally not recommended for feedwater with hardness exceeding 1 ppm (parts per million) as CaCO3. Higher hardness levels can lead to calcium carbonate scaling in the concentrate compartment, impairing performance and potentially damaging the membranes.
  • Pretreatment Requirement: Effective operation of EDI relies on adequate pretreatment to remove suspended solids, colloids, organic matter, and most dissolved solids. Reverse osmosis (RO) is a common and highly effective pretreatment.
  • Carbon Dioxide (CO2) Management: CO2 freely passes through RO membranes and can dissociate in the EDI diluting compartment, forming ionic species (HCO₃⁻, CO₃²⁻) that increase water conductivity and lower the EDI product water resistivity. Managing CO2 can be achieved by:
    • Adjusting the pH of the RO feed water (alkaline pH) to ionize CO2, allowing the RO membrane to reject the ionic species.
    • Employing degasification (e.g., membrane degasifier or forced-draft degasifier) to physically remove CO2 from the RO permeate before EDI.

AquaChain Engineering Tip

For optimal EDI performance and longevity, meticulously monitor and control the feed water's Langelier Saturation Index (LSI) to minimize the risk of scaling in the concentrate compartments. Implementing robust antiscalant dosing or even a second-pass RO system can be critical if the primary RO permeate still presents a scaling potential.

Frequently Asked Questions

Q1: What level of water purity can EDI achieve? A1: EDI systems can typically produce ultrapure water with resistivity ranging from 10 to 18.2 MΩ·cm, suitable for demanding applications such as semiconductor manufacturing, pharmaceutical production, and power plant boiler feed.

Q2: Does EDI replace reverse osmosis (RO)? A2: No, EDI typically complements RO. RO serves as a crucial pretreatment step, removing the majority of dissolved solids, organics, and particulates, thus ensuring optimal performance and extending the lifespan of the downstream EDI unit.

Q3: How does EDI impact chemical usage compared to traditional ion exchange? A3: EDI drastically reduces or entirely eliminates the need for regeneration chemicals (acids and caustics), leading to significant savings in chemical costs, reduced chemical handling risks, and lower wastewater neutralization requirements.

Ultrapure Water