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ARCHIVED REPORTS_SEPARATE PHASE HYDROCARBON INVESTIGATION UNOCAL EXTRACTION WELL PILOT STUDY 2011
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ARCHIVED REPORTS_SEPARATE PHASE HYDROCARBON INVESTIGATION UNOCAL EXTRACTION WELL PILOT STUDY 2011
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Last modified
2/13/2020 6:26:46 PM
Creation date
2/13/2020 2:35:54 PM
Metadata
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Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
SEPARATE PHASE HYDROCARBON INVESTIGATION UNOCAL EXTRACTION WELL PILOT STUDY 2011
RECORD_ID
PR0009302
PE
2960
FACILITY_ID
FA0004002
FACILITY_NAME
MORTON-ALCO
STREET_NUMBER
55
Direction
S
STREET_NAME
LINCOLN
STREET_TYPE
ST
City
STOCKTON
Zip
95203
APN
13737004
CURRENT_STATUS
01
SITE_LOCATION
55 S LINCOLN ST
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
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Stantec <br /> Report of Findings for the Waterfront Towers Separate Phase Hydrocarbon Investigation <br /> and Unocal Extraction Well Pilot Study <br /> Waterfront Towers Parking Lot <br /> March 4, 2011 <br /> were not calculated individually because those laboratory results were all non-detect and are <br /> also assumed to be incorporated within the TPHg results as part of the applicable carbon range. <br /> During TPE on GWE-1, approximately 3.96 lbs of TPHg were removed by SVE. The removal <br /> rate was approximately 4.03 lbs/day. Calculations of mass removal by SVE are presented in <br /> Table 6. <br /> During TPE on GWE-1, the removal of chemical constituents is not directly calculated because <br /> groundwater analytical samples were not collected during TPE and also due to low groundwater <br /> production and flow rates. During the majority of the TPE test on GWE-1, the stinger tube orifice <br /> was lowered into the well casing approximately 13 feet bgs, which was approximately the level <br /> of the air/water interface inside the well. On November 19, 2010, during a short period of <br /> additional runtime, the stinger tube orifice was lowered to the bottom of the well casing which <br /> could have the effect of increasing groundwater production. Lowering the stinger tube orifice <br /> farther for the majority of the test was not possible because of the high soil vapor flow rates at <br /> very low applied casing vacuum and stinger tube vacuum. The low applied vacuum was not <br /> sufficient to simultaneously entrain substantial quantities of groundwater along with the soil <br /> vapors. Raising vapor flow rates in an attempt to increase casing vacuum and entrain more <br /> groundwater corresponded to increased chemical mass in the soil vapors, based on FID results. <br /> . The rich fuel/air mixture caused a corresponding increase in oxidizer temperatures approaching <br /> unsafe and/or inadequate % destruction levels which are evident in the oxidizer temperatures <br /> presented in Table 2. The fact that the burner temperature was maintained higher than the stack <br /> temperature indicates that % destruction maintained was adequate and that fuels had fully <br /> combusted prior to discharge. <br /> Presentation of groundwater chemical constituent total removal and removal rates are reserved <br /> for the GWE test data and results sections below, where the information collected is more viable <br /> and meaningful for such an analysis. <br /> 4.10 GWE-2 TWO-PHASE EXTRACTION TESTS DATA AND RESULTS <br /> GWE-2 was operated in the TPE mode continuously for approximately 23 hours from November <br /> 18 through 19, 2010. Field notes are included in Appendix H. The following is a summary of the <br /> data collected during the test. <br /> FID soil vapor concentration readings ranged from 1,206.0 ppmv near the start of the test to <br /> 295.0 ppmv at the end of the test (Table 2). Laboratory analysis indicated influent soil vapor <br /> concentrations of TPHg ranging from 52 to 86 ppmv. Field and laboratory analytical results are <br /> included in Table 2 and Table 4. Laboratory analytical reports and chain of custody <br /> documentation are included in Appendix I. <br /> Well field flow from monitoring GWE-2 ranged from 78 scfm at 15.7 in. H2O applied casing <br /> vacuum gauge pressure to 148.9 scfm at 16.2 in. H2O applied casing vacuum gauge pressure. <br /> Well field flow rates and applied casing vacuum data are shown on Table 2. <br /> 4.12 <br />
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