Laserfiche WebLink
7.5 <br />7.6 <br />7.7 <br />7.8 <br />7.8.1 <br />Pilot Study Results <br />A pilot study was performed by John Thom of SEH of Ramsey's water in January 2020. The Pilot <br />Study Report is included in Appendix E. The objectives of the pilot study were to evaluate the <br />effectiveness of detention time prior to filtration, and to determine the optimal filter media. <br />The pilot study found no significant difference between direct filtration and utilizing 30 minutes of <br />detention time prior to filtration, and found no significant difference between the silica <br />sand/anthracite and greensand/anthracite filter media. Because the manganese oxide coating on <br />manganese greensand filters is helpful for manganese removal, greensand/anthracite filter media <br />is recommended. <br />Filter Sizing <br />The required filter area is determined by dividing the nominal filtration capacity by a flux rate <br />(filtration rate). Ten States Standards requires sand filtration rates from 2 to 4 gpm / ft2. Because <br />the required filtration capacity is 10 MGD under normal operating conditions, the facility will be <br />designed for 10 MGD at 2 gpm / ft2. Therefore, if 15 MGD is necessary for short periods of time, <br />the filtration rate will still be in the acceptable range. With a capacity of 10 MGD and a filtration <br />rate of 2 gpm / ft2, it is necessary to have 3,200 ft2 of filter media. To have reasonable backwash <br />rates and operational flexibility, this will be broken into eight filters. <br />Operator Input <br />Ramsey operators and City Staff toured existing water treatment plants in Andover and Brooklyn <br />Center as part of this feasibility study. Operator feedback from the tours was gathered and <br />incorporated into the building layouts discussed in the following sections. <br />Treatment Alternative 1 - Gravity Filter Layout <br />General <br />In an iron and manganese gravity filtration system, water to be filtered is pumped, under low <br />pressure, to the treatment facility where it flows by gravity through the various treatment <br />processes. Following the oxidation process, the water flows through the filter cells from top to <br />bottom. As the water passes through the filter media, the insoluble particles of iron and <br />manganese are removed. <br />As more and more water is filtered, the restriction to flow, created by the accumulation of iron and <br />manganese solids on the media, steadily increases. In a gravity facility, this restriction to flow, <br />called head, is measured in feet of water depth in the filter cells. As the solids accumulate, the <br />depth of water in the filter cells increases. Due to the physical nature of a gravity filter, when the <br />depth of water in a cell reaches its maximum designed head (high water level) backwashing is <br />required. Failure to backwash at the proper time could result in the filter overflowing or poor <br />effluent water quality being produced. Gravity filters are typically constructed of concrete or steel. <br />Steel filters are generally found in smaller water systems. Because of the large size of the filters <br />required for Ramsey, steel filters are not being considered. <br />FEASIBILITY STUDY RAMSY 154354 <br />Page 29 <br />