EDI frente a DI de lecho mixto: selección industrial, dimensionamiento y OPEX

septiembre 23, 2025

This practical guide compares edi vs mixed bed polishing in an industrial sistema di water. You’ll get a decision matrix, field-tested sizing rules, typical OPEX differences, feed-water windows, polishing steps, and a concise BOM you can send to procurement. Focus: commercial/industrial users — electronics, laboratories, food & beverage, hotels, plating, and light pharma (note: DI is not WFI).

After RO, choose EDI for continuous operation without bulk chemicals, or mixed bed for tolerance and simple retrofits.

1) Basics: What They Do

In most industrial trains, RO removes bulk salts first. A polisher then drives ionic content to the final target: EDI (electrodeionization) uses ion-exchange resins and membranes under an electric field for continuous polishing without bulk acid/caustic handling; a cama mixta uses separate cation/anion resins in one vessel that you regenerate with acid and caustic between runs.

Quality is specified as resistividad (MΩ-cm) o conductividad (μS/cm). Quick conversion: conductividad (μS/cm) = 1 / resistividad (MΩ-cm). Many plants target 1–10 MΩ·cm; Type I lab water requires ~18 MΩ·cm with a polished loop.

Selection flow: feed stability, chemical policy, uptime and staffing often decide edi vs mixed bed.

2) EDI vs Mixed Bed — Decision Matrix

Criterios	Pulido EDI	Mixed bed DI
Modo de funcionamiento	Continuous, automated; no bulk chemicals	Batch; periodic acid/caustic regeneration and neutralization
Feed-water window	Best with stable RO permeate; low hardness/CO₂/silica; low TOC	More tolerant to swings; handles intermittent operation well
Quality stability	Very stable resistivity at constant load	High resistivity achievable; may drift as resin exhausts
Uptime & staffing	High uptime; commissioning requires expertise	Simpler hardware; regeneration skills and safety training needed
OPEX	Electrical power; occasional CIP	Acid/caustic, rinse water, neutralization, PPE & handling
Footprint	Compact skid; power supply & controls	Vessels + chemical storage + neutralization system
When to prefer	Continuous production, limited chemical handling, tight specs	Retrofits, frequent stops/starts, wide feed variability, lower capex

Regla de oro: if your site restricts bulk chemicals or aims for continuous lights-out operation, pick EDI. If you need tolerance to irregular feeds, stop–start shifts, or want the lowest upfront cost, start with a mixed bed.

3) Sizing Rules & Quick Formulas

3.1 EDI Sizing

Confirm RO permeate meets vendor window (low hardness; low CO₂, silica and TOC; temperature factor applied).
Select stacks by caudal de producto (m³/h) and expected carga iónica; request the vendor’s sizing sheet and add a seasonal safety margin.
Provide bypass/recirculation and measure resistivity y flow at the skid outlet; alarm on deviations.

3.2 Mixed Bed Capacity (rule-of-thumb)

Express ionic load after RO as meq/L. Estimate resin volume for a target run time:

Resin volume (L) ≈ [meq/L × product flow (m³/h) × run time (h)] ÷ [resin capacity (eq/L)] × safety factor

Choose run time (e.g., 8–24 h) to align with shifts. Use the resin supplier’s capacity (depends on grade and regeneration regime).

3.3 Regeneration Chemical Estimate (general form)

Define required equivalents to restore the bed (from vendor). A general stoichiometric form is:

Acid volume (L)  ≈  required eq ÷ acid normality (N) ÷ efficiency
Caustic volume (L) ≈ required eq ÷ caustic normality (N) ÷ efficiency

“Efficiency” reflects practical overfeed and contact losses; confirm with your resin datasheet and SOP before ordering chemicals.

3.4 Quality Conversion (Resistivity ↔ Conductivity)

Resistivity (MΩ·cm) Conductivity (μS/cm)

Tip: conductivity (μS/cm) = 1 / resistivity (MΩ·cm).

4) OPEX, Footprint & Operations

EDI OPEX: primarily electrical power; watch temperature/CO₂–driven ionic load swings; run vendor-recommended CIP as needed.
Mixed Bed OPEX: acid/caustic consumption, rinse water, neutralization system operation, PPE and handling/safety training.
Downtime & variability: EDI prefers continuous duty; mixed beds tolerate stop–start operation and load spikes better.
Compliance & safety: chemical storage with secondary containment, ventilation, eyewash/shower, and documented regeneration/neutralization SOPs.

At steady load with chemical restrictions, EDI tends to win; under variable feeds or frequent stops, mixed bed is simpler.

5) Pulido, almacenamiento y distribución

UV (254 nm) for microbial control; add 185 nm UV for TOC if SOP requires.
Filtro final de 0,2 μm before points of use or loop return.
Use a stainless-steel storage tank with vent filter and spray ball; keep loop velocity high enough to maintain quality.

6) Materiales e instrumentación

Pipes: UPVC/PP for pretreatment; SS316L or sanitary plastics downstream of polishing.
Metros clave: resistivity/conductivity (RO permeate, polisher outlet, loop return), TOC (if required), SDI, flow, and ΔP.
Controls: PLC/HMI with interlocks on quality deviations and alarms; data logging for audits.

7) BOM Template & Related Products

Pretratamiento: MMF, GAC, dosificación de suavizante o antiincrustante, filtros de cartucho
RO skid: high-pressure pump, vessels/elements, instrumentation, CIP ports
Pulidor: Pilas EDI o mixed bed resin vessel with regeneration/CIP kit
Polishing: UV 254 (option 185), 0.2 μm final filter
Storage/loop: SS316L tank, recirculation pump, resistivity at outlet/return, TOC if needed
Documentos: P&ID, diseño, listas de comprobación FAT/SAT, plantillas IQ/OQ

8) PREGUNTAS FRECUENTES

Is EDI always better than a mixed bed?

No. EDI is ideal when chemicals are restricted and operation is continuous. Mixed beds are cheaper to start and tolerate feed swings and stop–start duty.

How do I know my RO permeate is good enough for EDI?

Check hardness, CO₂, silica and TOC against your vendor’s window. Stable temperature and load improve EDI performance and power efficiency.

What resistivity should I target after polishing?

Follow your SOP or industry guidance: many plants target 1–10 MΩ·cm; Type I lab water requires ~18 MΩ·cm and a polished loop.

Can I retrofit EDI to replace my mixed bed?

Yes — validate RO permeate window and utilities first, then size EDI stacks. Many sites keep a small mixed bed as emergency backup.

9) Referencias (externas)

Equipo de Ingeniería del Agua de Stark — Field experience in RO, EDI and mixed-bed DI for electronics, labs, F&B and hospitality.

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