Laserfiche WebLink
t <br /> i <br /> POUNDS OF HYDROCARBON IN A <br /> VAPOR STREAM <br /> INPUT DATA <br /> 1)Vapor flow rate acfin(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/M') for ppmv you need molecular weight <br /> 5)Length of time(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 quantities <br /> removed, some assumptions must be made about what was happening between measurements The <br /> ' following assumptions will be used for the sake of consistency <br /> ASSUMPTIONS, <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 enure 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 equal <br /> 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 the <br /> previous period to make the calculations Restart the unit and then take data to start the next period <br /> SAMPLE DATA AND CALCULATIONS <br /> Date Time Temp Press HC conc Vapor flow Calc <br /> deg F in H2O mg/M3 acfm lb rem <br /> ' 1/6/95 11 00 70 -46 2000 120 <br /> 1/7/95 13 00 55 -50 1350 90 <br /> 1/8/95 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 pm) <br /> on the 7th to 10 am on the 8th Pressure and temperature of the measurements(at the flow meter)must be <br /> corrected to the P and T used to report the HC concentration(which are P= 1 atm and T=70 deg F) 1 atm <br /> ' = 14 7psia, 760 mm Hg, or 407 in H2O Tis=460+T deg F <br /> Hours of operation= 21,T=80,P=-13, HC=(1350+750)/2= 1050 mg/M' Flow=95 <br /> (460+70) (407-13) 283 1050 1 <br /> 21 x 60 x 95 x ----------- x ------ x ------ x ------- x------ = 741b <br /> ' (460+80) 407 1000 1000 454 <br /> hr min Cu ft M3 g lb lb <br /> ----- x----- x ----- x TcoR x Pc"n x ------ x ------- x ------ _ ------- <br /> basis hr mm cu ft M3 g basis <br /> 21 x 60 x 95 x 098 x 0 97 x 0 0283 x 1 050 x1/454 = 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/M' ppmv x molecular wt /24 1 = mg/M3 (Use 102 for gasoline) <br />