Illinois Administrative Code
Title 35 - ENVIRONMENTAL PROTECTION
Part 604 - DESIGN, OPERATION, AND MAINTENANCE CRITERIA
Subpart H - SOFTENING
Section 604.805 - Cation Exchange Process
Current through Register Vol. 48, No. 38, September 20, 2024
a) Pre-treatment under Section 604.1010(b) or (c) is required when the content of iron, manganese, or a combination of the two is 1 mg/L or more.
b) Design requirements must provide:
c) The design capacity for hardness removal must not exceed 20,000 grains per cubic foot when resin is regenerated with 0.3 pounds of salt per 1000 grains of hardness removed.
d) The depth of the exchange resin must not be less than 3 feet.
e) Flow Rates
f) The freeboard must be calculated based on the size and specific gravity of the resin and the direction of water flow. Unless otherwise approved by the Agency under Section 604.145(b), the washwater collector must be 24 inches above the top of the resin on downflow units.
g) The bottoms, strainer systems, and support for the exchange resin must conform to the criteria provided for rapid rate gravity filters in Section 604.605(f) and (g).
h) Brine must be evenly distributed over the entire surface of both upflow and downflow units.
i) Backwash, rinse, and air relief discharge pipes must be installed to prevent any possibility of back-siphonage.
j) Bypass Piping and Equipment
k) When the applied water contains a chlorine residual, the cation exchange resin must be a type that is not damaged by residual chlorine.
l) Sampling Taps
m) Brine and Salt Storage Tanks
n) Corrosion control must be provided under Subpart I.
o) Suitable disposal must be provided for brine waste.
p) Pipes and contact materials must be resistant to the aggressiveness of salt. Plastic and red brass are acceptable piping materials. Steel and concrete must be coated with a non-leaching protective coating that is compatible with salt and brine.
q) Dry bulk salt storage must be enclosed and separated from other operating areas to prevent damage to equipment.