My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
ARCHIVED REPORTS_XR0003755
EnvironmentalHealth
>
EHD Program Facility Records by Street Name
>
H
>
HAZELTON
>
375
>
2900 - Site Mitigation Program
>
PR0540905
>
ARCHIVED REPORTS_XR0003755
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
2/3/2020 10:09:16 AM
Creation date
2/3/2020 8:56:34 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0003755
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
Scanner
SJGOV\sballwahn
Tags
EHD - Public
There are no annotations on this page.
Document management portal powered by Laserfiche WebLink 9 © 1998-2015
Laserfiche.
All rights reserved.
/
68
PDF
Print
Pages to print
Enter page numbers and/or page ranges separated by commas. For example, 1,3,5-12.
After downloading, print the document using a PDF reader (e.g. Adobe Reader).
View images
View plain text
I <br />' Mass-Volume Calculations Of Extracted Gasoline Hydrocarbons <br /> SIERRA LUMBER - 375 West Hazelton Avenue, Stockton, CA <br />' Assumptions <br />' Utilizing analytical data collected from air samples(Table 4)and from field measurements collected during the <br /> SVE pilot test (Table 5), the average concentration of extracted gasoline hydrocarbons at the site can be <br /> approximated <br /> 1 The hydrocarbon mass removed during the operating period can be calculated using the following equation <br /> M=C - Q - t <br />' where M=cumulative mass recovered(kg) <br /> C=vapor concentration(kg/m') <br />' Q=extraction flow rate(m'/hr) <br /> t=operational period (hrs) <br />' The average inlet TPH-g concentration and average flow rates during each time interval were utilized for calculating the <br /> approximate mass/volume of extracted gasoline hydrocarbons <br /> 1. 23 June 2003 to 24 July 2003 <br /> l <br /> The average analytical TPH-g concentration for this time interval was determined to be 138 5 pg/1(06-23-03=250 pg/1 <br /> ie and 07-24-03 =27 ug/L, avg — 138 5,ug/L) The average flow rates during this time was calculated at 0 375 inches of <br /> water or approximately 33 5 cubic feet per minute(table 6), the operational period was equal to 744 hours of running <br /> time <br /> C = 138 5 pg11=0 0001385 kglm' <br /> Q = 0 375 inches water = 33 5 ft'/min <br /> t=744 hours(3 t days) <br /> Converting Q to m'/hour yields <br /> Q=(33 5 ft'/min) •(60 min/hour)-(0 0283168m'/ft')=56 92 m'/hour <br /> M=C • Q- t=(0 0001385 kg/m')•(56 92 m'/hour)• (744 hours)=5 87 kg of gasoline <br /> Converting kg of gasoline to pounds of gasoline yields <br />' 5 87 kg of gas • 2 2046 lbs of gas/kg of gas= 12 93 lbs of gasoline <br /> 12 93 lbs gas/26 days=0 42 lbs/day <br /> Converting pounds of gasoline to gallons of gasoline yields <br /> 12 93 lbs of gas • 0 16 gal of gas/lbs of gas z 2 07 gallons of gasoline <br /> r <br />
The URL can be used to link to this page
Your browser does not support the video tag.