View File - Development Services - City of Oxnard

View File - Development Services - City of Oxnard View File - Development Services - City of Oxnard

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13.07.2015 Views

WATER RESOURCES TECHNICAL REPORTgroundwater in the Oxnard Plain and Pleasant Valley area. Opportunities for bothcoastal and inland configurations would be considered. As needed to meet agriculturalwater demands, the City would recover the directly injected water either from injectionwells or other wells.• Concentrate Collection System. A new concentrate 3 collection system would bedeveloped to serve the AWTF, the regional desalter, and various existing industrialbrine producers. The concentrate collection system would collect the reverse osmosis(RO) concentrate produced by these facilities instead of allowing it to discharge into theexisting City sewer system. Because the source of secondary effluent for the GREATProgram is the Oxnard WWTP (fed by the City sewer system) the quality of recycledwater produced by the treatment program is dependent upon sewer system inputs. Theconcentrate would be directed to the Oxnard WWTP outfall for disposal.• Permeate Delivery System. A new permeate 3 distribution system would be developedto provide high quality water to industrial users. This would reduce the need to provideRO treatment of City potable water and reduce discharges of concentrate to thecollection system.• Concentrate Disposal. Tertiary filter backwash from the TTF and concentrate from theAWTF and regional desalter would bypass treatment at the Oxnard WastewaterTreatment Plant to avoid contributing to the high TDS levels of the wastewater influent.Instead, backwash and concentrate would be directly disposed into the Pacific Ocean viathe existing Oxnard WWTP outfall.Section 4.3, Phase 1 Elements, and Section 4.4, Phase 2 Elements, describe the generallocation and specific elements of the GREAT Program, to be developed and operated intwo phases.4.3 Phase 1 ElementsWhile full build out of the GREAT Program (i.e. implementation of both Phases 1 and 2) isone of the recommended elements of the City’s Capital Improvement Program to meetprojected water supply needs through year 2020 (Water System Master Plan, January 2003),Phase 1 is intended to construct and implement facilities at a scale sufficient to meet theCity’s near-term needs. In addition, if Port Hueneme Water Agency (PHWA) participates inthe GREAT Program and the Brackish Water Reclamation Demonstration Facility (BWRDF)is converted to advanced treatment of tertiary treated water, Phase 1 would service PHWApotable water customers currently served by the BWRDF. Construction of Phase 1 facilitiesis anticipated to occur over a period of approximately 32 months (2.5 years).4.3.1 Tertiary Treatment FacilityThe Oxnard WWTP (6001 South Perkins Road) currently treats 22 mgd of wastewater tosecondary treatment standards. Up to 5 mgd of the treated wastewater would be diverted3 In situations where brackish groundwater is treated with membrane filtration technology, two products are produced:“permeate” and “concentrate.” Permeate is produced through the removal of salts and is intended for consumption by varioususers. Concentrate is the portion that contains the concentrated salts and requires disposal. The terms “brine” and“concentrate” are used interchangeably for the purposes of discussion in this document.W112003002SCO LW1458.DOC/ 033390002 51

WATER RESOURCES TECHNICAL REPORTfrom the WWTP and treated by a new Tertiary Treatment Facility (TTF). The new 5-mgdTTF and associated facilities are proposed to be located within an approximately 8-acreportion of a vacant parcel along Perkins Road, located north and east of the existing WWTP.The City is seeking to acquire the 8 acre vacant parcel to meet spacing needs for the TTF andassociated facilities under Phase 1 as well as future expansion under Phase 2. However,should the proposed location not be available, the TTF and associated facilities would besited on an approximately 8-acre parcel to be located within 1 mile east or west of PerkinsRoad, south of Hueneme Road, and north of the Pacific Ocean, to be further defined andanalyzed in future environmental documentation.Secondary effluent from the Oxnard WWTP would be conveyed north to the vicinity of theTTF as part of the WWTP Headworks Expansion Project estimated to be completed byMarch 2006. A new east-west pipeline would be required to convey the secondary effluentfrom the WWTP Headworks site (to be located west and adjacent to the AWTF) to the TTF.Secondary effluent would be either gravity fed or pumped from the WWTP Headworks siteto the TTF via approximately 500 linear feet of 36-inch pipeline (secondary effluentpipeline). The secondary effluent pipeline is shown in Figure 4-2.4.3.2 Advanced Water Treatment FacilityAdvanced treatment of tertiary treated water would occur at a 3.8-mgd advanced watertreatment facility (AWTF). One of the following options would be exercised to create theappropriate facility configuration:• AWTF Option 1: Upgrade and convert the existing Brackish Water ReclamationDemonstration Facility (BWRDF) to advanced water treatment• AWTF Option 2: Construct a new AWTF co-located with the proposed TTFThese two options and components required to operate advanced water treatment arediscussed below.AWTF Option 1: Upgrade Existing Brackish Water Reclamation Demonstration Facility.The existing 4-mgd BWRDF, owned by PHWA and currently operated by City staff,desalinates local groundwater supplied by UWCD and supplies drinking water for PHWAmember agencies, including: the City of Port Hueneme, Channel Islands Beach CommunityServices District, Naval Construction Battalion Center Port Hueneme, and Naval AirWeapons Station Point Mugu. Concentrate from the BWRDF treatment process is currentlydischarged to the City sewer system and routed to the headworks of the Oxnard WWTP fortreatment. The GREAT Program would convert the existing BWRDF located along PerkinsRoad from potable water production to advanced water treatment of tertiary water.AWTF Option 2: Construct New Advanced Water Treatment Facility. If PHWAinvolvement in the GREAT Program does not occur, a new advanced water treatmentfacility would be required. With consideration of cost and available space, the AWTF wouldbe co-located with the proposed TTF within the approximate 8-acre vacant parcel the City isseeking to acquire along Perkins Road.The AWTF would include conveyance pipelines; treatment equipment for demineralizationand disinfection; ancillary advanced treatment equipment; and a permeate storage tank. TheW112003002SCO LW1458.DOC/ 033390002 52

WATER RESOURCES TECHNICAL REPORTgroundwater in the <strong>Oxnard</strong> Plain and Pleasant Valley area. Opportunities for bothcoastal and inland configurations would be considered. As needed to meet agriculturalwater demands, the <strong>City</strong> would recover the directly injected water either from injectionwells or other wells.• Concentrate Collection System. A new concentrate 3 collection system would bedeveloped to serve the AWTF, the regional desalter, and various existing industrialbrine producers. The concentrate collection system would collect the reverse osmosis(RO) concentrate produced by these facilities instead <strong>of</strong> allowing it to discharge into theexisting <strong>City</strong> sewer system. Because the source <strong>of</strong> secondary effluent for the GREATProgram is the <strong>Oxnard</strong> WWTP (fed by the <strong>City</strong> sewer system) the quality <strong>of</strong> recycledwater produced by the treatment program is dependent upon sewer system inputs. Theconcentrate would be directed to the <strong>Oxnard</strong> WWTP outfall for disposal.• Permeate Delivery System. A new permeate 3 distribution system would be developedto provide high quality water to industrial users. This would reduce the need to provideRO treatment <strong>of</strong> <strong>City</strong> potable water and reduce discharges <strong>of</strong> concentrate to thecollection system.• Concentrate Disposal. Tertiary filter backwash from the TTF and concentrate from theAWTF and regional desalter would bypass treatment at the <strong>Oxnard</strong> WastewaterTreatment Plant to avoid contributing to the high TDS levels <strong>of</strong> the wastewater influent.Instead, backwash and concentrate would be directly disposed into the Pacific Ocean viathe existing <strong>Oxnard</strong> WWTP outfall.Section 4.3, Phase 1 Elements, and Section 4.4, Phase 2 Elements, describe the generallocation and specific elements <strong>of</strong> the GREAT Program, to be developed and operated intwo phases.4.3 Phase 1 ElementsWhile full build out <strong>of</strong> the GREAT Program (i.e. implementation <strong>of</strong> both Phases 1 and 2) isone <strong>of</strong> the recommended elements <strong>of</strong> the <strong>City</strong>’s Capital Improvement Program to meetprojected water supply needs through year 2020 (Water System Master Plan, January 2003),Phase 1 is intended to construct and implement facilities at a scale sufficient to meet the<strong>City</strong>’s near-term needs. In addition, if Port Hueneme Water Agency (PHWA) participates inthe GREAT Program and the Brackish Water Reclamation Demonstration Facility (BWRDF)is converted to advanced treatment <strong>of</strong> tertiary treated water, Phase 1 would service PHWApotable water customers currently served by the BWRDF. Construction <strong>of</strong> Phase 1 facilitiesis anticipated to occur over a period <strong>of</strong> approximately 32 months (2.5 years).4.3.1 Tertiary Treatment FacilityThe <strong>Oxnard</strong> WWTP (6001 South Perkins Road) currently treats 22 mgd <strong>of</strong> wastewater tosecondary treatment standards. Up to 5 mgd <strong>of</strong> the treated wastewater would be diverted3 In situations where brackish groundwater is treated with membrane filtration technology, two products are produced:“permeate” and “concentrate.” Permeate is produced through the removal <strong>of</strong> salts and is intended for consumption by varioususers. Concentrate is the portion that contains the concentrated salts and requires disposal. The terms “brine” and“concentrate” are used interchangeably for the purposes <strong>of</strong> discussion in this document.W112003002SCO LW1458.DOC/ 033390002 51

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