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BEST ENVIRONMENTAL <br /> Stack Gas Volumetric Flowrate Determination <br /> Facility: ck-f Location: Pt -14 <br /> Date -6-26--`7 Time- 12-5— Run#• <br /> Pitot Factor (Cp): © Pitot#. Personnel: <br /> Assumed %02: Actual Barometric (Pb): O, Cq& <br /> Assumed %CO2. Actual Static Pressure (Pstatic): <br /> Assumed %CO. Actual Stack Diameter, in: <br /> Assumed %Hz0- Actual Stack Area , ft" (As). 73 <br /> Port ID PointDelta P Stack SEIRT 0 Port Dia: Port Depth <br /> & [vent." (-P) Temp -P Downstream Distance, <br /> Point # inches °F, (ts) Avp`20^ Upstream Distance <br /> Q 3 <br /> if 67-7 Pitot Leak Chk 0 5sees@>3"). <br /> (a 1,&12-5- <br /> -4.0 <br /> 2-5-.0 , D t.q -m CALCULATIONS <br /> 4W3 Molecular Weight of Dry Gas, glg mole(MWd) <br />'! MWd = 0 44(%CO2)+0 32(%02)+0 28(%CO+N2) <br /> 2 , L(O I�1 516 Z MWd =`�-Z cf ,22- <br /> t7 <br /> (c �v CS Water Vapor Fraction, (Bwo) <br /> l�C� Bwo = 0.0473*ml/(DSCF + 0 0473*ml) <br /> SIT3,�5 3 O Bwo <br /> Molecular Weight of Stack Gas, g/g mole(MWs) <br /> MWs = MWd*(1-Bwo)+18(Bwo) <br /> ' i MWs = 2�.5 <br /> Stack Pressure, `Hg(Ps) <br />' <br /> IN = Ph + (Pstaf1c lIQ <br /> Stack Gas Velocity,actual feet per sec(Vs) <br /> Vs = 85.49*Cp*(SQRT "P)avg*SQRTI(ts+460)/(Ps*MWs)] <br /> Vs = '7453 1 <br /> Stack Area, ft2(As) <br /> As = (Dianieter/24)2 *3 1416 <br /> As <br /> Stade Gas Flow Rate, DSCFM <br /> DSCFM = 6((I-Bwo)*Vs*As*5281(ts+460)*Psn9.92 <br /> ACFM = <br /> DSCFM = <br /> Comments: (i.e.: diV. or process info ) <br /> z <br /> v�,aGl=s 20 1.s3 <br />