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Datasheet summary

EDI E-Cell Stack MK-3

Engineering summary from PDF text extraction for EDI E-Cell Stack MK-3. Verify every value with the OEM datasheet.

Summary

Product identification

The E-Cell EDI MK-3 Stack is an industrial electrodeionization (EDI) stack designed to produce ultrapure water for applications such as semiconductor fabrication, power generation, and solar panel production.

Key features:

  • Uses electrical current to provide ultrapure water.
  • Delivers high levels of product water quality and low energy consumption.
  • Minimizes cleaning requirements at higher feed water hardness levels using counter-current operation.
  • Guaranteed leak-free with a standard 3-year prorated warranty.
  • Operates continuously, requiring no caustic or acid for regeneration of ion exchange resin.
  • Requires no brine injection or concentrate recirculation.

Typical applications include:

  • Ultrapure water for rinsing of semiconductor chips, solar panels, and other microelectronics.
  • Demineralized boiler feed water for high-pressure boilers.

Quality Assurance

  • CE, RoHS, CSA, and EAC marked.
  • Manufactured in an ISO 9001 and ISO 14001 Facility.
  • Certified with UKCA.
  • Halal certified by the Islamic Food and Nutrition Council of America (IFANCA®).

Mechanical / hydraulic

  • Nominal Flow: 3.4 m³/h (15 gpm)
  • Flow Rate Range: 1.6 – 4.5 m³/h (7.0 – 20 gpm)
  • Shipping Weight: 100 kg (220 lbs)
  • Dimensions (width x height x depth): 30 cm x 61 cm x 54 cm (12'' x 24” x 22”)

Product water

Guarantees available:

  • Resistivity: ≥ 16 MOhm-cm
  • Sodium: ≤ 3 ppb
  • Silica (SiO₂): As low as 5 ppb
  • Boron: As low as 0.08 ppb (contact Veolia for guarantees)
  • Note: Actual performance may vary depending on site conditions. Consult Winflows projection software or contact Veolia for specific guarantees.

Typical Removal Efficiencies:

  • Sodium: ≥ 99.9% removal
  • Silica (SiO₂): Up to 99% removal
  • Boron: Up to 96% removal

Operating limits

  • Recovery: Up to 96%
  • Voltage: 0–300 VDC
  • Amperage: 0–5.2 ADC
  • Inlet Pressure: ≤ 6.9 bar (100 psi)
  • Pressure Drop: 1.4–2.8 bar (20–40 psi) at nominal flow and 25°C.

Feed water

  • Total Exchangeable Anions (TEA as CaCO₃): ≤ 63.6 ppm. (Represents concentration of all anions, including OH⁻, CO₂, and SiO₂. This value is at minimum flow and maximum temperature; Winflows software must be used to confirm acceptability for specific applications.)
  • Conductivity Equivalent: ≤ 109 μS/cm
  • Temperature: 4.4–40˚C (40–104˚F)
  • Total Hardness (as CaCO₃):
    • ≤ 1.0 ppm for standard counter-current flow operation.
    • Decreases to 0.1 ppm for co-current flow operation.
  • Silica (SiO₂):
    • ≤ 1.0 ppm.
    • Allowable limit decreases above nominal flow.
    • Decreases to 0.5 ppm with feed water hardness above 0.5 ppm as CaCO₃.
  • Total Organic Carbon (TOC as C): ≤ 0.5 ppm
  • Total Chlorine: ≤ 0.05 ppm
  • Fe, Mn, H₂S: ≤ 0.01 ppm
  • Boron:
    • ≤ 1.0 ppm.
    • Limited to 0.3 ppm as B when a silica guarantee or resistivity guarantee above 10 MOhm-cm is required.
  • pH: 4 to 11
  • Oil & Grease: None detectable
  • Particulate: RO permeate or equivalent. RO permeate is specified because EDI stacks contain packed beds of ion exchange medium that cannot be backwashed/fluidized to remove particulate matter. Systems with an open system between an RO system and E-Cell must be fitted with filters immediately preceding the E-Cell (generally 5 µm absolute or 1 µm nominal).
  • Oxidizing Agents: None detectable
  • Color: ≤ 5 APHA (APHA is a color standard/scale defined by ASTM D1209).

Disclaimer: This summary is based on extracted text and may not include all figures, footnotes, or the latest revisions. Contractual data for any project must match the specific OEM PDF revision used on that project.

Official datasheet (PDF)

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Curated from selected public technical reference material for discovery and preliminary comparison. This summary is not a substitute for a current certified manufacturer datasheet. Verify revisions and design limits before use.