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PROJ00001
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Last modified
11/19/2009 11:22:19 AM
Creation date
10/5/2006 11:28:58 PM
Metadata
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Template:
Loan Projects
Contract/PO #
C153168
Contractor Name
Delta, City of
Contract Type
Loan
Water District
40
County
Delta
Bill Number
SB 77-35
Loan Projects - Doc Type
Feasibility Study
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<br />I <br /> <br />I <br /> <br />Chemical Treatment Works <br /> <br />I <br /> <br />I <br /> <br />The existing chemical treatment works consist of a small <br />two story chemical building and a 20-foot by approximately 80-foot <br />open concrete reaction basin. The chemical treatment works are <br />located adjacent to the Delta Control Reservoir at an approximate <br />elevation of 5,330 feet above mean sea level. The facilities were <br />constructed in 1968 with the filtration plant and replaced the old <br />chlorinator and fluoridation houses. <br /> <br />I <br /> <br />I <br /> <br />Raw water enters a five foot by six foot flash mlxlng <br />chamber in the chemical building from the Delta Control Reservoir. <br />The rate of flow is controlled by a flow tube located ahead <br />of a cylinder operated butterfly control valve. The pressure differ- <br />ential across the flow tube is converted into an electrical signal <br />which is used to pace the chemical feeders and rate of chlorination. <br />A small electrically operated service pump draws water from a tap on <br />the main influent line. A portion of this water may be fed into a gas <br />chlorinator and then into the mixing chamber. The rest of the water <br />pumped from the effluent line may be piped into separate dissolver <br />chambers where lime (Calcium Hydroide) and Alum (Aluminum Sulphate) <br />may be added from separate hoppers. Lime is added to partially <br />remove calcium and magnesium bicarbonate which cause hardness. <br />Alum is added as a coagulant to form chemical floc particles <br />that adsorb, entrap, or otherwise bring together suspended matter. <br /> <br />I <br /> <br />I <br /> <br />I <br /> <br />I <br /> <br />I <br /> <br />Concentrated solutions of lime and alum are theoretically <br />introduced into the flash mlxlng chamber at suitable ratios for <br />balanced reactions to occur. From the mixing chamber, the water flows <br />over a weir and through four 12-inch sluice gates into the reaction <br />basin. The reaction basin is divided into three sections separated by <br />over and under weirs. The velocity of flow in the reaction basin <br />should be such to allow the floc particles to settle to the bottom of <br />the basin. At the end of the reaction basin, the upper layer of water <br />flows over a weir and into the main effluent pipeline and eventually <br />to the filtration plant. The water level below the effluent weir is <br />monitored and a signal is sent to the control valve on the main <br />influent line. The control valve is throttled to maintain a preset <br />level in the influent chamber. <br /> <br />I <br /> <br />I <br /> <br />I <br /> <br />I <br /> <br />At frequent intervals, the particles which have settled out and <br />collected in the reaction basin must be flushed out. This is <br />accomplished by temporarily interrupting plant operation and draining <br />the reaction basin through strategically located 12-inch drain lines. <br /> <br />I <br /> <br />A schematic diagram of <br />treatment works is shown in <br />such as sensing lines and drain <br /> <br />the main operations at the chemical <br />Figure 111-5. Secondary functions <br />lines have not been shown. <br /> <br />I <br /> <br />I <br /> <br />III - 8 <br /> <br />I <br />
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