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Ion-Exchange Systems

Resin beds that trade unwanted ions for harmless ones — from hardness removal at the front of the plant to sub-microsiemens polishing at the end.

Chemical exchange SP · DM · MB · CPU · EDI Down to < 0.1 µS/cm Auto regeneration · PLC

Membranes separate by size. Ion exchange works chemically instead: water passes through a bed of resin beads loaded with a sacrificial ion, and the ions you want gone stick to the resin while the sacrificial ion takes their place in the water. Nothing is filtered out — something is swapped in.

That single mechanism covers a wide span of duty. What changes between the five systems is which resin, which sacrificial ion, and how deep the polish goes — and, in the case of EDI, whether regeneration chemicals are needed at all.

Product Conductivity
< 0.1 – 20
µS/cm, by system
Systems In Category
5
pre-treatment to polish
Resin Bed Life
4 – 8
years, typical
Where This Category Sits Ion-exchange stages highlighted

Ion exchange appears twice in a typical train — once ahead of the membranes as protection, once behind them as polish.

The Shared Mechanism Service → exhaustion → regeneration

Four of the five systems run on a cycle. Understanding it explains almost every operating cost and every design decision in this category.

STEP 01
Service
Water flows down through the bed. Target ions bind to the resin; the sacrificial ion — sodium, hydrogen or hydroxide — leaves with the water.
STEP 02
Exhaustion
Every bead has a finite capacity. As it fills, treated quality drifts — rising hardness or conductivity is the signal to stop.
STEP 03
Regeneration
A concentrated regenerant floods the bed and reverses the exchange: brine for a softener, acid and caustic for a DM or mixed bed.
STEP 04
Rinse & Return
The bed is rinsed to spec and returned to service. Duty / standby vessels keep supply continuous through the whole sequence.
Exception
EDI breaks the cycle.

An applied DC field regenerates the resin continuously, so there is no exhaustion, no acid or caustic handling, no regeneration downtime and no neutralisation pit. That is why EDI replaces mixed-bed polishing on most new pharma and semiconductor plants — the trade is that it needs low-conductivity RO permeate as feed.

Bulk Ion Removal Three of five systems

These carry the load — taking raw or filtered water and removing hardness or the full dissolved-salt burden.

SP Lead Product
Softening Plant
Removes Ca²⁺ / Mg²⁺ · brine regenerated
Use when hardness is the problem — scale in boilers and cooling circuits, or protection for a downstream RO. Strong acid cation resin on the sodium cycle; salt is the only consumable.
View specifications →
DM Core Product
De-Mineralisation Plant
Cation + anion · 1 – 20 µS/cm product
Use when all dissolved salts must go and there is no RO in the train — boiler feed for steam generation, process water for chemicals and pharma. Regenerated with acid and caustic.
View specifications →
MB Specialist Duty
Mixed Bed Plant
Cation + anion resin in one vessel
Use as a compact single-vessel polisher after a DM plant or RO — intimately mixed resins act like an infinite series of DM stages, taking conductivity to a fraction of what two-bed exchange reaches.
View specifications →
Final Polishing Two of five systems

These sit at the end of the train, taking already-treated water the last decimal place — or recovering steam condensate so it never has to be made again.

Selection Matrix Coarse → ultra-pure

Read down the column that matches your requirement. Where a softener will do, never buy a DM plant — the regeneration chemistry alone changes the cost of ownership.

Parameter
SP
Softening Plant
DM
De-Mineralisation
MB
Mixed Bed
CPU
Condensate Polishing
EDI
Electrodeionisation
Removes
Hardness (Ca²⁺, Mg²⁺)
All cations & anions
Residual ions, silica, sodium
Iron & copper oxides, ionic traces
Residual ions after RO
Resin
Strong acid cation (Na⁺ form)
SAC + SBA in series
SAC + SBA intimately mixed
Precoat filter + cation / anion / MB
Thin resin cell between membranes
Regenerant
Brine (NaCl)
HCl + NaOH
HCl + NaOH
HCl + NaOH
None — DC field
Product quality
< 5 ppm hardness
1 – 20 µS/cm
< 0.1 µS/cm
Boiler-feed spec
< 1 µS/cm continuous
Position in train
Pre-treatment
Primary treatment
Polish after DM or RO
Steam-cycle return loop
Polish after RO only
Feed requirement
Filtered water
Filtered water (PSF + ACF)
DM or RO permeate
Returned condensate
RO permeate, low conductivity
Typical duty
Cooling towers, boiler make-up, pre-RO
Boiler feed, process water
Final polish, lab & power
HP boilers, captive power
Pharma PW / WFI, semiconductor UPW
Operator burden
Low — salt only
Medium — acid & caustic handling
Medium — acid & caustic handling
Medium
Lowest — no chemicals
Figures are indicative design ranges — final selection follows a feed water analysis.
Reference Installations

Client names withheld under confidentiality. Full commissioning data available on request.

Pharmaceutical · Formulations
RO with EDI polish for PW loop
Formulations plant, Gujarat. EDI behind a double-pass RO feeding a validated purified water loop — chemical regeneration removed from the utility block entirely.
< 1
µS/cm
18
m³/hr
Captive Power · Steam
Condensate polishing on an HP circuit
Captive power block, Maharashtra. Precoat filtration plus mixed-bed polishing on the condensate return, cutting fresh DM make-up and boiler chemical dosing.
82%
condensate returned
60
m³/hr
Textile · Processing
Softening ahead of dyeing and RO
Processing house, Tamil Nadu. Duty / standby softeners on the make-up line protecting both the dye bath and a downstream RO from hardness scaling.
< 5
ppm hardness
2
duty / standby
PDF Technical Datasheet Ion-Exchange Systems — full specification set Resin selection tables, vessel and regeneration data, utility requirements and P&ID references across all five systems.
Download ↓
Next Step
Resin sizing is arithmetic — but only once we know your water.

Send us a feed water analysis and your daily demand. We will return the recommended configuration, resin volumes, regeneration frequency and an indicative footprint.