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ARCHIVED REPORTS_DRAFT ENVIRONMENTAL IMPACT REPORT
Environmental Health - Public
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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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EHD - Public
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Near and Far Field Dilution Analysis of Manteca Discharge October 2006 <br /> In Figure 17, a plot of plume centerline dilution profiles for the 9.87 MGD cases with the <br /> side bank outfall and with the diffuser shows that the profiles only differ significantly <br /> within about 5,000 feet of the discharge point. <br /> Plan view color contour plots of minimum effluent dilution are shown in Figure 18 <br /> through Figure 20 for each of the discharge rates. <br /> The lowest dilution values at 450' down the plume centerline from the point of discharge <br /> are summarized in Table 1. For the 9.87 MGD simulation, the dilution credit is 2.4:1, <br /> which is slightly less than the 3:1 dilution credit in the permit. This difference is due to <br /> the expanded model and refined critical conditions. <br /> Human Health Simulation Results <br /> For the Human Health simulations, the San Joaquin River flow was set constant at 2,015 <br /> cfs. The downstream tide was set using observed stage data at the CDEC station at Old <br /> River at Head for November 20 through December 5, 2001, a time when San Joaquin <br /> River flows averaged around 2,015 cfs. The Old River at Head stage was smoothed <br /> using a 3 point centered moving average. <br /> Under the higher flow conditions of the Human Health simulation, constant treatment <br /> plant discharge is allowed. <br /> Tidally averaged effluent dilution was computed for each scenario and the times of <br /> lowest dilution were selected for plotting. Figure 21 shows the lowest tidally averaged <br /> dilution profiles along the centerline of the effluent plume for the three side bank <br /> discharge scenarios. At this time, the lowest dilution occurs at the outfall where it is <br /> nearly pure effluent for all flow scenarios. At 10,000 ft downstream of the discharge, <br /> dilution is approximately 134:1 for the 9.87 MGD simulation, 75:1 for the 17.5 MGD <br /> simulation, and 47:1 for the 27 MGD. <br /> Figure 22 shows the lowest hourly average dilution profiles along the centerline of the <br /> effluent plume for the three diffuser scenarios (the lowest dilution for the diffuser case <br /> does not occur at the same time as for the side bank case). At this time, the lowest <br /> dilution occurs at the diffuser. For the 9.87 MGD simulation, the lowest dilution is <br /> approximately 69:1, for the 17.5 MGD simulation 3 8:1 and for the 27 MGD simulation <br /> 25:1. At 10,000 ft downstream of the discharge, dilution is approximately 126:1 for the <br /> 9.87 MGD simulation, 71:1 for the 17.5 MGD simulation, and 46:1 for the 27 MGD, <br /> similar to the side bank scenario. <br /> A plot of plume centerline dilution profiles for the 9.87 MGD cases with the side bank <br /> outfall and with the diffuser is shown in Figure 23 at the time of lowest dilution for the <br /> side bank discharge case. This plot shows that the dilutions differ for the two cases down <br /> to the location where the model transitions to 1-D (approximately 5,400 ft), at which <br /> point the concentrations become fully mixed across the channel cross-section. <br /> Plan view color contour plots of minimum effluent dilution are shown in Figure 24 <br /> through Figure 26 for each of the discharge rates. <br /> The lowest dilution values at 5280' down the plume centerline from the point of <br /> discharge are summarized in Table 1. <br /> 13 <br />
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