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ARCHIVED REPORTS XR0008125
EnvironmentalHealth
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EHD Program Facility Records by Street Name
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EL DORADO
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1448
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3500 - Local Oversight Program
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PR0544673
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ARCHIVED REPORTS XR0008125
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Last modified
7/16/2020 6:26:41 AM
Creation date
7/18/2019 3:24:51 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
3500 - Local Oversight Program
File Section
ARCHIVED REPORTS
FileName_PostFix
XR0008125
RECORD_ID
PR0544673
PE
3528
FACILITY_ID
FA0006182
FACILITY_NAME
REGAL STATION #604
STREET_NUMBER
1448
Direction
N
STREET_NAME
EL DORADO
STREET_TYPE
ST
City
STOCKTON
Zip
95202
CURRENT_STATUS
02
SITE_LOCATION
1448 N EL DORADO ST
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
Scanner
SJGOV\wng
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EHD - Public
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REMOX 06/08/92 <br /> . 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/l x 0 . 000001g/ug x 0 .0022051g/g x 28 . 321/cf = 0 . 000000621lb/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 = V1T2/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 . 580 + T°F ) <br /> X lb/day = C ug/l x 0 . 0000000621 lb 1/ug cf 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 + 4H2O , which gives an increase from <br /> 6 to 7 molecules per molecule of propane. This effectively means <br /> that after combustion 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 /> 5 <br />
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