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Agenda - Council Work Session - 10/20/2020 - Special
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Agenda - Council Work Session - 10/20/2020 - Special
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Meetings
Meeting Document Type
Agenda
Meeting Type
Council Work Session
Document Title
Special
Document Date
10/20/2020
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7.8.5 <br />7.9 <br />7.9,1 <br />operating conditions of the filters. Control panels (fixed or mobile) will be provided to allow the <br />operators to manually initiate backwashes from the upper revel. <br />Clearwell <br />A clearwell is located adjacent to the gravity filter treatment facility. The clearwell provides <br />storage and operational flexibility (the box shown on Figure lA in Appendix F represents 1 million <br />gallons of storage). This storage is necessary to (1) maintain a volume of water for backwashing <br />filter cells, (2) to provide the flexibility to treat water at a rate different than the raw water pumping <br />rate, and (3) to provide additional storage for the distribution system. <br />To provide operational flexibility and to supplement system storage, a 1 million gallon clearwell is <br />the minimum size recommended. <br />Treatment Alternative 2 — Pressure Filter Layout <br />General <br />In an iron and manganese pressure filtration system, water to be filtered is pumped directly to, <br />and through, the facility's components under pressure. Oxidation occurs inside the pipelines and <br />filter vessels upstream of the filter media. Following the oxidation process, the water flows <br />through the filter vessels from top to bottom. As the water passes through the filter media, the <br />insoluble particles of iron and manganese are removed from the flow. <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 pressure facility, this restriction to flow, <br />called head, is measured in pounds per square inch (psi). As the solids accumulate, the <br />headloss, or difference in pressures between the top and bottom sides of the filter media <br />increases. Due to the design and construction of pressure filters, headless can be driven as high <br />as 15 psi. although 5 to 6 psi is the preferred upper limit to ensure water quality. <br />The advantages to pressure filtration systems are: <br />1. The facilities tend to have less capital cost than gravity facilities. <br />2. Plants are typically constructed on one floor level. <br />3. Provide for greater available headloss than gravity faci[ities which can result in longer filter <br />run times than a comparably sized gravity facility. Longer filter run times require less <br />backwashing which keeps a filter in service longer. <br />The disadvantages lo pressure filtration systems are: <br />1. Pressure filter systems have less ability to add additional treatment processes (aeration, <br />detention) if regulations or water quality changes. <br />2. Closed from view and difficult to access internally. This prevents observation of the systems <br />operation. Condition of the filter media and flow distribution during a backwash cycle cannot <br />be readily monitored. <br />3. Pressure filters are constructed out of steel and require periodic blasting and painting. <br />4. Inspection of the pressure filters requires entry into a confined space which is a safety <br />hazard. <br />FEASIBILITY STUDY -DRAFT RAMSY 154354 <br />Page 30 <br />
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