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cell growth. Settled sludge is removed by mixing chlorine gas and water. The are combined and pumped to the <br /> from the bottom of the clarifiers. Return chlorine solution is added at the flash digesters. The sludge is processed in <br /> activated sludge(RAS)is used to seed mixer to disperse the chemical. After an airless(anaerobic)environment <br /> the new influent wastewater to produce disinfection,some residual chlorine is by bacteria that stabilizes the material <br /> the mixed liquor and repeat the cycle. To present and represents a toxic hazard to and creates a useful material called <br /> prevent overpopulation of the organism the aquatic life in the Delta. To remove biosohds that is distributed with plant <br /> and a shortage of air and food,a portion this threat,the chlorine is neutralized effluent onto agricultural land. The <br /> of the activated sludge is pumped to the by the addition of sulfur dioxide digestion process also produces methane <br /> sludge thickeners. (dechlorination). gas;this gas is recycled on site,firing <br /> boilers which keep the digesters' <br /> © DISINFECITONANDDECHLORINATYON O AIR FLOTATION THICKENERS temperatures between 95 and 100 <br /> Disinfection and dechlorination of the The solids removed from the secondary degrees F,the optimum environment <br /> wastewater is performed prior to clarifiers are pumped to the flotation for peak biological activity. <br /> discharge to White Slough. The effluent thickeners to be thickened before being O INDUSTRIAL TREA1rIENT <br /> leaving the secondary clarifiers contains sent to the anaerobic digesters. Following preliminary treatment, <br /> large numbers of biological organisms. industrial flows are first treated in the <br /> Some of these may be pathogenic(disease O ANAEROBIC DIGESTERS aerated lagoon. They then pass into the <br /> causing)organisms. To protect public Sludge and scum from the primary skimming pond and on to the storage <br /> health,the effluent is disinfected using a sedimentation basins and the thickened ponds. Flows are pumped to irrigation <br /> chlorine solution produced at the plant sludge from the flotation thickeners from the equalization pond. <br /> CHLORINE <br /> MON SECONDARY FLASH CONTACT FLOW <br /> CLARIFIERS MIXER TANKS MEASUREMENT <br /> O <br /> TO IRRIGATION/ <br />■ or OUTFALL <br /> ---- L2 ----- SOLUTION <br /> I o <br /> _ _-__ <br /> - ------------ -----I SULFUR <br /> DIOXIDE <br /> CI-2 I METERING TANK <br /> TO •-_ -----I <br /> HEADWORKS I CL2 <br /> WAS LN I SOLUTION <br /> - <br /> SECONDARY SLUDGE -nCHLORINE <br /> PUMPING BUILDING METERING TANK <br /> STORAGE EQUALIZATION IRRIGATION <br /> PONDS POND <br /> LOW CHART <br /> Irrigation Pumping Heat Exchangers <br /> Pumps................................_............_....................._..3 Number—..................................................._..3 <br /> W SWD......................2 Capacity each,gpm...._.............................................45011 Capacity each.Btu/hr..................................$00.000 <br /> :q Fl/day ..........541 <br /> Flotation Thickeners Sludge Lagoons <br /> ............3 Number......................................................................2 Numb _ _2 <br /> ec......-... ................ ................................. <br /> _..........._...._..__...........2,000 Surface Area,sq fL:................._........__ Valu....................1®600 Volume,total cuu itk................ ..531i000 <br /> G 300 <br /> s........__..._...................q 1 <br /> ........__...........................100 Hydraulic Loading,gpm/sq k...............................0.3030 <br /> Sludge Digestion <br /> n...................................182 Digesters <br /> Size:45diameter x 25'SwD_..._.........._.....3 <br /> y....................................2 Detenaon Time,days....................................16-22 <br /> ...............---..................I Cas Preducfiogcuk/day...........................111,400 <br /> y.................._................2 <br />