Louisiana Administrative Code
Title 51 - PUBLIC HEALTH-SANITARY CODE
Part XII - Water Supplies
Chapter 1 - General
Subchapter D - Treatment
Section XII-181 - Softening
Universal Citation: LA Admin Code XII-181
Current through Register Vol. 50, No. 9, September 20, 2024
A. Lime or Lime-Soda Process. Design standards for rapid mix, flocculation and sedimentation are in §175 of this Part. Additional consideration must be given to the following process elements.
1.
Hydraulics. When split treatment is used, the bypass line should be sized to
carry total plant flow, and an accurate means of measuring and splitting the
flow shall be provided.
2. Rapid
Mix. Rapid mix detention times should be instantaneous, but not longer than 30
seconds with adequate velocity gradients to keep the lime particles
dispersed.
3. Stabilization.
Equipment for stabilization of water softened by the lime or lime-soda process
is required. (see §189 of this Part).
4. Sludge Collection. A means for sludge
removal shall be provided in the sedimentation basin.
5. Sludge Disposal. Provisions shall be
included for proper disposal of softening sludges. (see Subchapter F. §257-275
of this Part).
B. Cation Exchange Process. Design criteria for cation exchange process shall be as follows.
1. Pre-treatment requirements. Iron,
manganese, or a combination of the two, should not exceed 0.3 mg/L in the water
as applied to the ion exchange resin. Pre-treatment is required when the
content of iron, manganese, or a combination of the two, is one milligram per
liter or more (see §187 of this Part). Waters having 5 units or more turbidity
should not be applied directly to the cation exchange softener.
2. Design. The units may be of pressure or
gravity type, of either an upflow or downflow design. Automatic regeneration
based on volume of water softened shall be used unless manual regeneration is
justified and is approved by the state health officer. A manual override shall
be provided on all automatic controls.
3. Exchange Capacity. The design capacity
shall be in accordance with the manufacturers specifications for hardness
removal.
4. Depth of Resin. The
depth of the exchange resin shall not be less than three feet.
5. Flow Rates. The rate of softening shall
not exceed seven gallons per minute per square foot of bed area and the
backwash rate shall be between six and eight gallons per minute per square foot
of bed area. Rate-of-flow controllers or the equivalent shall be installed for
the above purposes.
6. Freeboard.
The freeboard will depend upon the size and specific gravity of the resin and
the direction of water flow. Adequate freeboard shall be provided to prevent
loss of media during backwashing.
7. Underdrains and Supporting Gravel. The
bottoms, strainer systems and support for the exchange resin shall conform to
criteria provided for rapid rate gravity filters (see §177. A.6 and §177. A.7 of this Part).
8. Brine
Distribution. Facilities should be included for even distribution of the brine
over the entire surface of both upflow and downflow units.
9. Cross-Connection Control. Backwash, rinse
and air relief discharge pipes shall be installed in such a manner as to
prevent any possibility of back-siphonage.
10. Bypass Piping and Equipment. Bypass shall
be provided around softening units to produce a blended water of desirable
hardness. Totalizing meters shall be installed on the bypass line and on each
softener unit. The bypass line shall have a shutoff valve and should have an
automatic proportioning or regulating device.
11. Additional Limitations. When the applied
water contains a chlorine residual, the cation exchange resin shall be a type
that is not damaged by residual chlorine.
12. Sampling Taps. A means of collecting
samples shall be provided for the collection of representative samples. If
sample taps are provided, they shall be Smooth-nose type. The taps sampling
locations shall be located to provide for sampling of the softener influent,
effluent and blended water. The sampling locations for the blended water shall
be at least 20 feet downstream from the point of blending.
13. Brine and Salt Storage Tanks. Design
criteria for brine and salt storage tanks shall be as follows.
a. Salt dissolving or brine tanks and wet
salt storage tanks shall be covered and must be corrosion-resistant.
b. The make-up water inlet shall be protected
from back-siphonage.
c. Wet salt
storage basins shall be equipped with manholes or hatchways for access and for
direct dumping of salt from truck or railcar. Openings shall be provided with
raised curbs and watertight covers having overlapping edges. Each cover shall
be hinged on one side, and shall have locking device.
d. Overflows, where provided, shall be
protected with corrosion resistant screens and must terminate with either a
turned downed bend having a proper free fall discharge or a self-closing flap
valve.
e. The salt shall be
supported on graduated layers of gravel placed over a brine collection
system.
14.
Stabilization. Refer to §189 of this Part.
15. Waste Disposal. Suitable disposal shall
be provided for brine waste (see Subchapter F. §257-275 of this
Part).
16. Construction Materials.
Pipes and contact materials shall be resistant to the aggressiveness of salt.
Steel and concrete must be coated with a non-leaching protective coating which
is compatible with salt and brine.
17. Housing. Bagged salt and dry bulk salt
storage shall be enclosed and separated from other operating areas in order to
prevent damage to equipment.
AUTHORITY NOTE: Promulgated in accordance with the provisions of R.S. 40:4.A.(8), 40:4.13.D.(1)(2) and 40:5.A.(2)(3)(5)(6)(7)(17).
Disclaimer: These regulations may not be the most recent version. Louisiana may have more current or accurate information. We make no warranties or guarantees about the accuracy, completeness, or adequacy of the information contained on this site or the information linked to on the state site. Please check official sources.
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