Laserfiche WebLink
JIr r <br /> l ' <br /> BEST ENVIRONMENTAL <br /> Stack Gas Volumetric Flowrate Determination - <br /> FDate: <br /> ty:�e� _�-fo� o Location: �,,��e �oQ� <br /> g-2 (i Time: 3 ` Run#: <br /> actor [Cpl: K2 9 2 Pitot #: Personnel: <br /> Assumed %02• Actual /Z, Barometric (Ply): <br /> Assumed %CO2: Actual Lt, LY Static Pressure (Pstatic): <br /> l Assumed 96C0: Actual Stack Diameter, in: <br /> Assumed %H10 Actual Stack Area , ft2 (As). <br /> Port ID point Delta P Stack SORT 0 Port Dia: Port Depth: <br /> & Location (-P) Temp "P Downstream Distance <br /> Point# Inches F. (ts) w"°C20° Upstream Distance <br /> OL Iq 91 03-47 Pitot Leak Chk. (15secs@>3"). <br /> 0,5� CALCULATIONS <br /> # Molecular Weight of Dry Gas, g/g mole(MWd <br /> ) <br /> MWd = 0 44(%CO2)+O 32(%02)+0 28(%CO+N2) <br /> 1 ,370 osL,4-; MWd = <br /> 0,5-272- Water Vapor Fraction, (Bwo) <br /> d 5OC6 Bwo = 0 0473*ml/(DSCF + 0 0473*ml) <br /> z d 6 44 Z Bwo = <br /> Molecular Weight of Stack Gas, g/g mole(MWs) <br /> M Ws = MWd*(1-Bwo)+18(Bwo) <br /> MWs = <br /> Stack Pressure, "Hg(Ps) <br /> Ps = Pb + (Pstaticl13.6) <br /> i <br /> StacklGas Velocity, actual feet per sec(Vs) <br /> Vs = 85.49*Cp*(SART "P)avg*SQRT[(ts+460)/(Ps*MWs)) <br /> Vs = <br /> Stack Area, ft-(As) <br /> As = (Diameter124)2 * 3 1426 <br /> As = <br /> Stack Gas Flow Rate, DSCFM <br /> DSCFM = 60(1-Bwo)*Vs*As*528/(ts+460)*Ps/29 92 <br /> ACFM = <br /> DSCFM= <br /> { Comments: G.e.: dog or process info.) <br />-e 6vev 44-4- A0 <br /> a �eu�l <br /> - I 1 9 �.p cJ n$'IYCGvH <br /> AVERAGES t q 3L) c9,523 3 <br />