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ARCHIVED REPORTS_XR0003766
EnvironmentalHealth
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EHD Program Facility Records by Street Name
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H
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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_XR0003766
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Entry Properties
Last modified
2/3/2020 10:15:39 AM
Creation date
2/3/2020 9:08:17 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0003766
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
Tags
EHD - Public
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I <br />' Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons - Continued <br /> SIERRA LUMBER- 375 West Hazelton Avenue, Stockton, CA <br />' 2. 27 APRIL to 07 May 2001 <br />' The average analytical TPH-g concentration for this time interval was determined to be 1,055 jug/l (04-27-01= <br /> 1,970µg/L and 05-07-01 = 140 ,ug/L, avg = 1,055 ,ug/L) The average flow rates during this time was <br />' calculated at 0 51 inches of water or approximately 39 cubic feet per minute(table 5),the operational period was equal <br /> to 240 hours of running time <br /> I <br /> C r 1,055 ug/1=0 001055 kg/in3 <br />' Q = 0 51 inches water = 39 ft3/min <br /> t=240 hours <br />' Converting Q to m/hour yields <br /> Q=(39 ft%rnn)-(60 nun/hour)-(0 0283168m3/ft3)=66 26 m3/hour <br />' M=C - Q• t=(0 001055 kghn3) -(66 26 m3/hour) • (240 hours)= 16 77 kg of gasoline <br /> Converting kg of gasoline to pounds of gasoline yields <br /> 16 77 kg of gas - 2 2046 lbs of gas/kg of gas=37 lbs of gasoline <br /> 10 <br /> Converting pounds of gasoline to gallons of gasoline yields <br /> 37 lbs of gas - 0 16 gal of gas/lbs of gas � 5.92 gallons of gasoline <br />' 3. 07 May �to 14 May 2001 <br />' The average analytical TPH-g concentration for this time interval was determined to be 1,070 /lg/1 (05-07-01= <br /> 140,tg/L and 05-14-01 = 2,000 ktg/L, avg = 1,070 µg/L) The average flow rates during this time was <br /> calculated at 0 56 inches of water or approximately 40 cubic feet per minute(table 5),the operational period was equal <br />' to 168 hours of running time <br /> C 1,070 ug/1=0 001070 kg/m' <br />' Q 0 56 inches water = 40 ft3/min <br /> t= 168 hours <br /> Converting Q to m3/hour yields <br />' Q=(40 ft3/min)•(60 nun/hour)-(0 0283168m3/ft3)=67 96 n0/hour <br /> M=C - Q - t=(0 001070 kg/&) -(67 96 m3/hour) • (168 hours)= 12 22 kg of gasoline <br />' Convertin k of gasoline to pounds of gasoline}yields <br /> Converting g g <br /> 12 22 kg of gas• 2 2046 lbs of gas/kg of gas=2194 lbs of gasoline <br />' Converting pounds of gasolene to gallons of gasoline yields <br /> . 26 94 lbs of gas - 0 16 gal of gas/lbs of gas � 4 31 gallons of gasoline <br /> I <br /> 1 <br />
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