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ARCHIVED REPORTS XR0006468
Environmental Health - Public
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EHD Program Facility Records by Street Name
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PACIFIC
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6425
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2900 - Site Mitigation Program
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PR0519189
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ARCHIVED REPORTS XR0006468
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Last modified
8/21/2019 3:56:46 PM
Creation date
8/21/2019 2:54:27 PM
Metadata
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EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0006468
RECORD_ID
PR0519189
PE
2950
FACILITY_ID
FA0014347
FACILITY_NAME
CURRENTLY VACANT
STREET_NUMBER
6425
STREET_NAME
PACIFIC
STREET_TYPE
AVE
City
STOCKTON
Zip
95207
APN
09741031
CURRENT_STATUS
02
SITE_LOCATION
6425 PACIFIC AVE
P_LOCATION
01
QC Status
Approved
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EHD - Public
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• CALCULATIONS <br /> To calculate the pounds ( lb) per day the concentration is <br /> multiplied by the volume of air produced .in one day. <br /> The lab reports the Concentrations (C) of the air sampling in <br /> ug/liter. The first step is to convert this value to lbs/cf <br /> (pounds per cubic foot) . <br /> 1 ug/1 x 0 . 00000#/ug x 0 . 00220516�g x 28 . 321/cf = 0 10000006211b/cf <br /> The volume of air produced in one day, equals the flow rate (Q)x <br /> the time of flow. <br /> V = Q x T = cf/day = cf/min x 1440min/day <br /> The volume must be corrected to standard temperature and <br /> pressure (STP) . <br /> P = Pressure = 14 . 7 lb/inz @ STP <br /> V = Volume cf <br /> T = Temperature in degrees above absolute Zero = 491 . 58°R @ STP. <br /> Using the Ideal Gas Law P1V1/T1 = P2V2/T2 <br /> Solving for V2 =P1V1T2/P2T1 <br /> Assuming P1 = P2 = 14. 7 lb/int , P cancels from the equation <br /> leaving V2 = VZT2/T1 . <br /> V1 = Q cf/m x 1440 min/day <br /> T2 = 491 . 58°R <br /> T1 = 459 . 58 + T°F at sight . <br /> V2 = Q cf/min x 1440 min/day x 491 . 58°R/ ( 459 . 58° + T°F) <br /> X lb/day = C ug/1 x 0 . 0000000621 lb 1/ug of x Q cf/min x <br /> 1440 min/day x 491 . 58°R/ ( 459 . 580 + T°F ) <br /> Q for the Influent sample = The well flow rate + the air flow <br /> Q for the Effluent = The well flow + the air flow + the fuel flow <br /> rate. <br /> The fuel flow rate must be corrected to account for the change in <br /> volume from combustion <br /> Since the gas volume depends on the number of molecules present <br /> the reaction of propane with oxygen produces an increase in <br /> volume . 1C3H8 + 502 -> 3CO2 + 4H20 , which gives an increase from <br /> 6 to 7 molecules per molecule of propane . This effectively means <br /> zhaz after comnustion the volume of flow resulting from the <br /> propane is double the propane flow rate . The reaction of methane <br /> (Natural Gas ) and oxygen does not produce a net change in volume, <br /> CH4 + 2 02 -> CO2 + 2 H2O; therefore a correction for combustion <br /> does not need to be made when methane is burned. <br /> page 6 of R603 , 09/10/92 <br />
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