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ARCHIVED REPORTS_DRAFT ENVIRONMENTAL IMPACT REPORT
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ARCHIVED REPORTS_DRAFT ENVIRONMENTAL IMPACT REPORT
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Last modified
7/23/2020 5:02:58 PM
Creation date
7/23/2020 4:33:19 PM
Metadata
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Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
DRAFT ENVIRONMENTAL IMPACT REPORT
RECORD_ID
PR0506303
PE
2965
FACILITY_ID
FA0001086
FACILITY_NAME
MANTECA PUBLIC WORKS
STREET_NUMBER
2450
Direction
W
STREET_NAME
YOSEMITE
STREET_TYPE
AVE
City
MANTECA
Zip
95336
APN
24130050
CURRENT_STATUS
01
SITE_LOCATION
2450 W YOSEMITE AVE
P_LOCATION
04
P_DISTRICT
005
QC Status
Approved
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Near and Far Field Dilution Analysis of Manteca Discharge October 2006 <br /> Model Simulations <br /> Near field dilution analysis simulations were performed for three San Joaquin River flow <br /> conditions, three treatment plant discharge rates and two discharge methods. <br /> The three river flow conditions corresponding to SIP Table 3 are: <br /> Acute—"1Q10 river flow," or 564 cfs; <br /> Chronic—"7Q 10 river flow," or 615 cfs; and <br /> Human health—Harmonic mean river flow, or 2015 cfs. <br /> For each of the above river flows, average daily treatment plant discharge rates of 9.87 <br /> MGD, 17.5 MGD and 27 MGD were simulated. <br /> Each of these nine flow-discharge combinations was simulated with a side bank <br /> discharge and with a diffuser. For the side bank discharge scenarios, the treatment plant <br /> discharge was input to two elements as shown in Figure 7. For the diffuser scenarios, the <br /> treatment plant discharge was distributed among 16 elements in a 140' long diffuser as <br /> shown in Figure 8. Flows into each diffuser element varied based on channel depth, with <br /> greater flows into the elements in the deeper area of the channel. This method resulted in <br /> a relatively even effluent concentration distribution across the width of the diffuser. <br /> The treatment plant discharge was tagged with a tracer concentration of 100 so that <br /> effluent dilution could be computed. The upstream boundary concentration was set to <br /> zero. Because the effluent does reach the downstream boundary at some low <br /> concentration and, therefore, returns on the incoming tide, for the acute and chronic <br /> simulations the downstream boundary concentration is set to a rough average of the <br /> concentration that occurs on the outgoing tide. This concentration is applied on the <br /> incoming tide only. Sensitivity tests were done and this number has no effect on the <br /> results within 10,000 feet of the discharge. Further downstream, this has the conservative <br /> effect of slightly reducing dilution near the downstream boundary. Overall, the effect is <br /> minimal. For the human health simulations, only one brief flow reversal occurs, so the <br /> downstream concentration boundary condition is not an issue. <br /> Acute Simulations <br /> For the Acute simulations, the San Joaquin River flow was set constant at 564 cfs. The <br /> downstream tide was set using observed stage data at the CDEC station at Old River at <br /> Head for July 1992, a time when San Joaquin River flows were similar to the acute river <br /> flow conditions. The Old River at Head stage was smoothed using a 3 point centered <br /> moving average. <br /> Under the low flow conditions of the Acute simulation, timed treatment plant discharge is <br /> required. The discharge schedule defined in the thermal exemption request is used to <br /> determine allowable discharge. The following points summarize the method used to <br /> determine the times to start and stop the discharge. <br /> When, under an ebb (falling) tide, San Joaquin River flow at Mossdale Bridge exceeds <br /> 800 cfs in the downstream direction, discharge from the outfall restarts. <br /> 10 <br />
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