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SU0005344 ENG DES PLN
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SU0005344 ENG DES PLN
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Last modified
10/29/2020 5:18:25 PM
Creation date
12/27/2019 8:23:37 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2600 - Land Use Program
FileName_PostFix
ENG DES PLN
RECORD_ID
SU0005344
PE
2627
FACILITY_NAME
PA-0500531
STREET_NUMBER
4620
Direction
E
STREET_NAME
WOODBRIDGE
STREET_TYPE
RD
City
ACAMPO
APN
01709002
ENTERED_DATE
8/26/2005 12:00:00 AM
SITE_LOCATION
4620 E WOODBRIDGE RD
RECEIVED_DATE
8/26/2005 12:00:00 AM
P_LOCATION
99
P_DISTRICT
004
QC Status
Approved
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\MIGRATIONS\W\WOODBRIDGE\4620\PA-0500531_PA-0300206\SU0005344\ENG DES PLN.PDF
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__VV_S!7f <br /> If a backwash is insufficient in removing foulants, the backwash efficiency can be enhanced by <br /> adding chemicals into the backwash (Chemically Enhanced Backwash). <br /> The CEB mode consists of a normal backwash procedure, a backwash with chemicals (these can <br /> be dosed after the backwash pump with a dosing unit), a soaking period and then a backwash <br /> to flush-out the chemicals. <br /> One 2-housing element OF membranes will be installed (with 100% redundancy) in the <br /> proposed WCMCRWWTP, along with the chemical enhanced backwash kits. Each element has a <br /> membrane area of 40 mz. The design net filtration flux is 48 L/mz/h and the recovery rate is <br /> 86.4%. <br /> The membranes have an average pore size of 0.025-0.028 pm and an absolute pore size of <br /> 0.03 pm. This ensures removal of all particulate matter larger than 0.03 pm, including colloids, <br /> solids and micro-organisms. There are two 500 micron strainers installed in the pipelines prior <br /> to entry to the membranes. <br /> 3.5 DISINFECTION <br /> The on-site chlorine-based disinfectant generation system is used for the WCMCRWWTP treated <br /> effluent disinfection. The disinfected water is discharged into the existing underground injection <br /> well. <br /> The most common chlorine contact tank configuration to use is a long plug-flow, around-the- <br /> end type of contact basins to assure a given percentage of the flow remains in the tank for a <br /> given period of time. To improve hydraulic performance, baffles are added in the chlorine <br /> contact tank. Figure 3 is a typical chlorine contact tank configuration. <br /> 1 T 1 T <br /> Figure 3 Schematic of typical chlorine contact tank configuration <br /> The theoretical contact time is 120 minutes and the model contact time is 90 minutes at the <br /> peak design flow (52 gpm). The operational volume of chorine contact tank is 6,336 gallons. <br /> The CT value shall be maintained at 450 mg-min/L, based upon Title 22 Disinfected Tertiary <br /> Recycling Water criteria. <br /> The MIOX system generates a chlorine-based disinfectant on-site as needed. The chlorine <br /> production capacity is designed to handle the peak demand for daily operations. One AE-4 unit <br /> shall be furnished and has 4 lbs/d chlorine generation capacity. A 24-hour reserve disinfectant <br /> supply is stored in an oxidant solution tank and injected into the water to be treated. <br /> Wine Cup Motor Coach Resort WWTP Page 8 of 10 8/22/2007 <br /> Preliminary Design Report <br />
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