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ARCHIVED REPORTS_XR0003594
Environmental Health - Public
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EHD Program Facility Records by Street Name
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HAZELTON
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375
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2900 - Site Mitigation Program
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PR0540905
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ARCHIVED REPORTS_XR0003594
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Last modified
2/3/2020 9:45:27 PM
Creation date
2/3/2020 8:53:25 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0003594
RECORD_ID
PR0540905
PE
2960
FACILITY_ID
FA0023406
FACILITY_NAME
SIERRA LUMBER MANUFACTURERS
STREET_NUMBER
375
Direction
W
STREET_NAME
HAZELTON
STREET_TYPE
AVE
City
STOCKTON
Zip
95205
APN
147120808
CURRENT_STATUS
01
SITE_LOCATION
375 W HAZELTON AVE
P_LOCATION
01
QC Status
Approved
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SJGOV\sballwahn
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EHD - Public
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I Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons <br /> SIERRA LUMBER-375 West Hazelton Avenue, Stockton, CA <br /> IAssumptions <br /> • Utilizing analytical data collected from air samples (Table 5) and from field measurements collected during <br /> I SVE remediation (Table 6),the average concentration of extracted gasoline hydrocarbons at the site can be <br /> approximated <br /> IThe hydrocarbon mass removed during the operating period can be calculated using the following equation <br /> M = C •Q • t <br /> I where M = cumulative mass recovered (kg) <br /> C =vapor concentration(kg/m3) <br /> Q =extraction flow rate (m3/hr) <br />' t=operational period(hrs) <br /> The average inlet TPH-g concentration were interpreted as the maximum concentration conservatively at the analytical <br />' method detection limit (eg 50 pg/L) and average flow rates during each time interval were utilized for calculating the <br /> approximate mass/volume of extracted gasoline hydrocarbons <br /> 1. 07 September 2005 to 18 October 2005 <br /> The average analytical TPH-g concentration for this time interval was determined to be 50/ig/1(09-07-05=<50,g/l and <br /> 10-18-05 =<50 pg/1 , avg - 50 yg/L) The average flow rates during this time was calculated at 0 65 inches of water <br /> or approximately 44 cubic feet per minute (table 6),the operational period was equal to 984 hours of running time <br />' C = 50 Icgll= 0 000050 kg/m3 <br /> Q - 0 65 inches water = 44 ft3/min <br />' t= 984 hours (41 days operation) <br /> Converting Q to m3/hour yields <br />' Q = (44 ft3/min) •(60 min/hour) •(0 0283168m3/ft3) =74 75 m3/hour <br /> M = C • Q •t= (0 000050 kg/m3) •(74 75 m3/hour) • (984 hours) = 3 68 kg of gasoline <br />' Converting kg of gasoline to pounds of gasoline yields <br /> 3 68 kg of gas •2 2046 lbs of gas/kg of gas= 8 11 lbs of gasoline <br />' 8 11 lbs gas/41 days =0 20 lbs/day <br /> I Converting pounds of gasoline to gallons of gasoline yields <br /> 8 It lbs of gas •0 16 gal of gas/lbs of gas = 130 gallon of gasoline <br /> I <br />
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