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ARCHIVED REPORTS_XR0005114
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ARCHIVED REPORTS_XR0005114
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Last modified
9/24/2020 12:38:23 AM
Creation date
3/17/2020 4:38:44 PM
Metadata
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Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0005114
RECORD_ID
PR0545566
PE
3528
FACILITY_ID
FA0005479
FACILITY_NAME
MANTECA BEAN CO
STREET_NUMBER
229
STREET_NAME
MOFFAT
STREET_TYPE
BLVD
City
MANTECA
Zip
95336
CURRENT_STATUS
02
SITE_LOCATION
229 MOFFAT BLVD
P_LOCATION
04
P_DISTRICT
005
QC Status
Approved
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EHD - Public
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16 <br /> 2 3 31 Longitudinal Dispersivity <br /> ' The longitudinal dispersivity was vaned from 10 ft to 1 ft Figure 2 6 presents the variation in <br /> contaminant and oxygen concentrations along the centerline of the contaminant plume (section A-A. <br /> Figure 2 2) for three values of longitudinal dispersivity It can be seen that the longitudinal dispersivity also <br /> has a slight effect on biodegradation The maximum contaminant concentrations vaned from 29 6 mg/l(10 <br /> ft)to 41 7 mgll (1 ft) The change in biodegraded mass with longitudinal dispersivity is illustrated in Figure <br /> 27 <br /> ' 2 3 3 2 Transverse Dispersivity <br /> The transverse dispersivity was vaned from 1 ft to 5 ft Figure 2 8 shows the variation of contaminant <br /> and oxygen concentrations with transverse dispersivity along a transverse cross section through the <br /> centerline of the plume(cross section B-B, Figure 2 2) The transverse dispersivity does not seem to have <br /> ' an appreciable effect on biodegradation The areal extent of the plume is not very sensitive to the <br /> transverse dispersivity, however,the maximum concentrations exhibit a wide range of vanation The <br /> maximum contaminant concentrations vaned from 26 5 mgll(5 ft)to 35 5 mg/1(1 ft) The change in <br /> biodegraded mass with transverse dispersivity is illustrated in Figure 2 7 <br /> 2 3 4 Variation of Concentrations with Porosity <br /> The porosity was vaned from 0 25 to 0 7 Figure 2 9 shows the variation of contaminant and oxygen <br /> concentrations with porosity along the centerline of the plume(section A-A, Figure 2 2) It is evident that <br /> porosity does not have a significant effect on biodegradation The maximum contaminant concentrations <br /> vaned from 29 0 mgll (n=0 25)to 35 0 mg/1(n=0 5) The change in biodegraded mass with porosity is <br /> illustrated in Figure 2 4b <br /> 2 3 5 Variation of Concentrations with Reaeration Coefficient <br /> The reaeration coefficient, k,was vaned from 0 0 day'to 0 005 day' Figure 2 10 presents the <br /> variation of contaminant and oxygen concentrations with k along the centerline of the plume (cross section <br /> A-A, Figure 2 2) It is evident that the coefficient of reaeration has a significant effect on biodegradation <br /> The areal extent of the contaminant plume as well as the maximum concentrations exhibit a wide range of <br /> variation with k The maximum concentrations vaned from 29 6 mg11 (k= 0 0 day)to 17 6 mgll (k= 0 005 <br /> day ) The change in biodegraded mass with k is presented in Figure 2 4a <br /> 2.4 Model Output <br /> Typical output from BIOPLUME II includes an oxygen and hydrocarbon distribution matrix at selected <br /> ' points in time (see Appendix B) These matrices can be plotted as contour plots(Figure 4 1) or surface <br /> plots using the SURFER graphics package (Golden Software, 1987) The graphics option in the <br /> BIOPLUME II preprocessor will transform the oxygen and hydrocarbon matrices to the required format for <br /> direct use in SURFER <br /> It can be seen from Figure 4 1 that whenever hydrocarbon is present in relatively high concentrations, <br /> then oygen is absent The oxygen plume forms an envelope for the hydrocarbon plume with oxygen <br /> concentrations gradually increasing to initial background levels as one moves away From the contaminant <br /> plume The model output also includes a mass balance computation for oxygen and hydrocarbon at the <br /> selected points in time The dissolved mass present in the system for each is computed, as well as the <br /> biodegraded mass The hydrocarbon mass balance computation details the biodegraded mass due to the <br /> ' different processes available in the model(aerobic, anaerobic, reaeration and radioactive decay) It is <br /> noted at this point that a detailed analysis of mass balance errors computed in BIOPLUME II is being <br /> performed for a variety of conditions and geometries The results of the analysis will be included in future <br /> ' updates to the manual <br /> I <br /> 2-5 <br />
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