Section R309-535-11 - Iron and Manganese ControlIron and manganese control, as used herein, refers solely to treatment processes designed specifically for this purpose. The treatment process used will depend upon the character of the source water. The selection of one or more treatment processes shall meet specific local conditions as determined by engineering investigations, including chemical analyses of representative samples of water to be treated, and receive approval of the Director. It may be necessary to operate a pilot plant in order to gather all information pertinent to the design. Consideration should be given to adjust the pH of the raw water to increase the rate of the chemical reactions involved.
Removal or treatment of iron and manganese are normally by the following methods:
(1) Removal by Oxidation, Detention and Filtration. (a) Oxidation. Oxidation may be by aeration, or by chemical oxidation with chlorine, potassium permanganate, ozone or chlorine dioxide.
(b) Detention. (i) Reaction time - A minimum detention time of twenty minutes shall be provided following aeration in order to insure that the oxidation reactions are as complete as possible. This minimum detention may be omitted only where a pilot plant study indicates no need for detention. The detention basin shall be designed as a holding tank with no provisions for sludge collection but with sufficient baffling to prevent short circuiting.(ii) Sedimentation - Sedimentation basins shall be provided when treating water with high iron and/or manganese content, or where chemical coagulation is used to reduce the load on the filters. Provisions for sludge removal shall be made.(c) Filtration. (i) General - Minimum criteria relative to number, rate of filtration, structural details and hydraulics, filter media, etc., provided for rapid rate gravity filters shall apply to pressure filters where appropriate, and may be used in this application but cannot be used in the filtration of surface waters or following lime-soda softening.(ii) Details of Design for Pressure Filter - The filters shall be designed to provide for: (A) Loss of head gauges on the inlet and outlet pipes of each filter,(B) An easily readable meter or flow indicator on each battery of filters,(C) Filtration and backwashing of each filter individually with an arrangement of piping as simple as possible to accomplish these purposes,(D) The top of the washwater collectors to be at least twenty-four (24) inches above the surface of the media,(E) The underdrain system to efficiently collect the filtered water and to uniformly distribute the backwash water at a rate capable of not less than 15 gpm/sf of filter area,(F) Backwash flow indicators and controls that are easily readable while operating the control valves,(G) An air release valve on the highest point of each filter,(H) An accessible manhole to facilitate inspections and repairs,(I) Means to observe the wastewater and filters during backwashing, and(J) Construction to prevent cross-connection.(2) Removal by the Lime-soda Softening Process. For removal by the lime-soda softening process refer to Part 4, Section 4.4, Softening, in the Recommended Standards for Water Works (commonly known as "Ten State Standards"), 2007 edition as indicated in R309-535-10. Those standards are hereby incorporated by reference and compliance with those standards shall be required for removal by the lime-soda softening process.
(3) Removal by Manganese Greensand Filtration. This process, consisting of the continuous feed of potassium permanganate to the influent of a manganese greensand filter, is more applicable to the removal of manganese than the removal of iron.
(a) Provisions shall be made to apply the permanganate as far ahead of the filter as practical and at a point immediately before the filter.(b) An anthracite media cap of at least six inches shall be provided over manganese greensand.(c) The normal filtration rate is three gpm/sf.(d) The normal wash rate is 8 to 10 gpm/sf.(e) Air washing shall be provided.(f) Sample taps shall be provided: (i) prior to application of permanganate,(ii) immediately ahead of filtration,(iii) at a point between the anthracite media and the manganese greensand,(iv) halfway down the manganese greensand, and(v) at the filter effluent.(4) Removal by Ion Exchange. This process is not acceptable where either the source water or wash water contains dissolved oxygen.
(5) Sequestration by Polyphosphates. This process shall not be used when iron, manganese or a combination thereof exceeds 1.0 milligram per liter. The total phosphate applied shall not exceed 10 milligrams per liter as PO4. Where phosphate treatment is used, satisfactory chlorine residuals shall be maintained in the distribution system and the following required:
(a) feeding equipment shall conform to the requirements of R309-525-11(7),(b) stock phosphate solution shall be kept covered and disinfected by carrying approximately 10 mg/l free chlorine residual,(c) polyphosphates shall not be applied ahead of iron and manganese removal treatment. If no iron or manganese removal treatment is provided, the point of application shall be prior to any aeration, oxidation or disinfection steps, and(d) phosphate chemicals must comply with ANSI/NSF Standard 60. Sampling taps shall be provided for control purposes. Taps shall be located on each raw water source, and on each treatment unit influent and effluent.
Waste generated by iron and manganese control treatment shall be disposed of in accordance with R309-525-23.
Utah Admin. Code R309-535-11