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DOWEX Ion Exchange Resins WATER CONDITIONING MANUAL

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Designing an <strong>Ion</strong> <strong>Exchange</strong> system<br />

Table 23. Typical regeneration efficiencies for different resin types and combinations.<br />

Resin Type/Configuration<br />

Regeneration<br />

System<br />

Typical Regeneration Efficiency<br />

(%)<br />

Strong acid cation Co-current HCl 200–250<br />

Counter-current HCl 120–150<br />

Co-current H2SO4<br />

Counter-current<br />

H2SO4<br />

250–300<br />

150–200<br />

Weak acid cation 105–115<br />

Weak acid + strong acid cation 105–115<br />

Strong base anion type 1 Co-current 250–300<br />

Counter-current 140–220<br />

Strong base anion type 2 Co-current 150–200<br />

Counter-current 125–140<br />

Weak base anion 120–150<br />

Layered bed anion 120–130<br />

11.5 Atmospheric Degasifier<br />

The decision to install an atmospheric degasifier is principally economic. Removing carbon dioxide before<br />

it reaches the anion resins will reduce NaOH chemical consumption, and this should be balanced against<br />

the cost of the degasifier. Generally, the economic balance is not in favor of a degasifier for small plants<br />

(up to approximately 45 gpm or 10 m 3 /h). For larger plants, if the total CO2 is greater than 50–100 ppm<br />

(mg/L), the payback time for a degasifier should be short.<br />

Atmospheric degasifiers usually reduce residual CO2 down to 5 ppm (mg/L). A residual value of 10 ppm<br />

(mg/L) CO2 is recommended as a safety margin for design.<br />

A vacuum degasifier is used for systems requiring very low levels of residual CO2,. This reduces the CO2<br />

to below 1 ppm (mg/L).<br />

11.6 Resin Operating Capacities and Regenerant Levels<br />

In co-current operation, the product water quality requirements will define the minimum levels of acid and<br />

caustic regenerant to be used. The regenerant levels and the feed water composition will then define the<br />

resin operating capacity. Although high regenerant levels result in increased capacity and lower ionic<br />

leakages, the chemical efficiency of the system (Section 11.4) becomes worse.<br />

<strong>Ion</strong>ic leakage and operating capacity curves are available as a function of feed composition and<br />

regenerant levels in the engineering brochures for <strong>DOWEX</strong> resin or from the CADIX computer design<br />

program.<br />

<strong>DOWEX</strong> <strong>Ion</strong> <strong>Exchange</strong> <strong>Resins</strong> 66 Water Conditioning Manual

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