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a <br /> POUNDS OF HYDROCARBON IN A <br /> VAPOR STREAM <br /> INPUT <br /> 1) Vapor flow rate acfm (usually by Pitot tube) <br /> 2) Vapor pressure at the flow measuring device (in inches of H2O) (use {-} for vacuum) <br /> 3) Vapor temperature at the flow measuring device <br /> 4) Hydrocarbon content of vapor (usually in Mg/M3) for ppmv you need molecular weight <br /> 5) Length of tune (usually hours) over which flow rate occurred) <br /> From periodic measurements, a calculation of total pounds of hydrocarbons removed from a well or from <br /> a system are calculated The input data listed above are measured at a point in time To calculate <br /> quantities removed, some assumptions must be made about what was happening between measurements <br /> The following assumptions will be used for the sake of consistency <br /> ASSUMPTION <br /> 1) Vapor flow for the period equals the average of the initial and final reading for the period <br /> 2) Pressure and temperature for the entire period will be the final reading <br /> 3) Hydrocarbon concentration for the period equals the average of the initial and final reading <br /> 4) The hours of operation can be taken from an hour meter, an electric meter or will be assumed to be <br /> equal to the time between measurements <br /> 5) If the unit is found down - try to determine how many hours it did operate and use the data taken for <br /> the previous period to make the calculations Restart the unit and then take data to start the next period <br /> SAMPLE AND CALCULATIONS <br /> Date Tine Temp Press HC cont Vapor flow Calc <br /> deg F in H2O mg/M3 acfin lb rem <br /> 116195 1100 70 -46 2000 120 <br /> 117195 1300 55 -50 1350 90 <br /> 118195 1000 80 -13 750 100 74 <br /> Calculate the pounds of hydrocarbon removed from the system during the basis period from 13 00 (1 00 <br /> pm) on the 7th to 10 am on the 8th Pressure and temperature of the measurements (at the flow meter) <br /> must be corrected to the P and T used to report the HC concentration(which are P = 1 atm and T = 70 <br /> deg F) 1 atm = 14 7psia, 760 mm Hg, or 407 in H2O Tam = 460 + T deg F <br /> Hours of operation = 21, T = 80, P = -13, HC = (1350+750)12 = 1050 mg/M' Flow = 95 <br /> (460+70) (407-13) 283 1050 1 <br /> 21 x 60 x 95 x ----------- x ----- x ------ x ------- x ------ = 7 4 lb <br /> (460+80) 407 1000 1000 454 <br /> hr min cu ft M3 g lb lb <br /> ----- x ----- x ----- x Tc., x Pin x ------ x ------- — <br /> basns hr min cu ft M3 g basis <br /> 21 x 60 x 95 x 098 x 097 x 0 0283 x 1 050 x11454 = 7 4 lb <br /> cumulative lbs (the running total) = the sum of all the previous periods <br /> . Note If results are given in ppm, an assumption about the molecular weight of the hydrocarbon must be <br /> made to get Mg/M3 ppmv x molecular wt 124 1 = nig/M1 (Use 102 for gasoline) <br />