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'11^' I " Elbow 90` Elbow, R1D = 1.5, S.St1 6 40S &065 CD3-1 0.1 I -- - ' Expansion 1ouu, G-614 6' Expmtsion Joint G ( 40S 5.9 11 CR6-3 024 " Tee 6 x 6 x 1 tee, flow tltru 6 40S 6.065 12 ED5-3 0.26 P23 Piping,G-VCG- 36-W8 6' straight duct,S.Stl 6 40S 6.065 -17.12 CD11-I ARROW Towl •d SI1M(G194:G198) incltcs =rSUMQ194119R) -+6199112 fl 113 Wye Il1 45' Lateral 3rmw3, Flow 6 x 8 40S 6.06518.329" 10 ED5-2 0.61 Pan Curve, NYR Modcl No. 1508 Test Datsity: 0.0553 IbuJcu ft Mechanical Q Ft/ Min V, IN H2O Std Efficiency. 0 12 67,16 500 13.75 67.36 -5004B207 13 67.36 500+0 2 08 11.25 67.36 500+8209 8 67.36 =500+821 D 425 67.36 -500+8211 0 6736 8ackdraft Damper Pressure Drop ReC SN(JPPS 90144 24 x 24 wolotypc For 8" Pipe Area sch 10 Dia. Vs, fpm dP, ntcbcs w.c. Q, ChM sq. R ft 700 0.13 -+8217•ES217 =+PIO•1:217^214 =8.329112 800 0.135 -+8218•ES217 900 0.14 -+8219•E$217 1000 0.145 -+8220•F$217 1500 0.18 =+8227•ES217 2000 0.23 -+8222•ES217 2500 0.27 -+p223.15217 3000 0.32 -+8224•E$2l7 3500 10.36 =+8225•ES217 RPP-24544 REV Id A5-628
i Y" c^ N j of OGTS Bypass External Convection and Thermal Radiation Coefficients Free Convection Correlations for air at 1 atm. (Holman 1990, Table 7-2) Twl = 875 OF Temperature End 1 Tw2 = 250 °F Tem erature End 2 Ts - 562.5 OF Average Wall Temperature To = 115 OF Ambient Temperature dT = 447.5 °F i Temperature difference h = 1.45 Btwhr-ft, ,2-°F Vertical Plane or Cylinder h = 0.19 * dT^l i3 h = 1.38 Btu/hr-ft^2-°F Horizontal Cylinder h = 0.18 * dT^1/3 h = 1.68 ! Btu-'hr-ft^2-°F Horizontal Plate - heated face up h = 0.22 * dT^ 1 /3 Forced convection, flow across a cylinder (Holman 1990, e n. 6-21): 0.61Re^,`Rr"3; Rey, Nufd = 0.3+A*B/C Forced Convection, Nusselt No. A = 0:62Red"2Pr"3 B = 1+(Red/282,000)^5/8]^4/5 1 to .4' D = 8.6 Inch Dia of Pie 1844 meters U = 0.1 Mph Free Stream Air Vel. -~-0.0447 m/s Ts = 5625 OF I Pi e Wall Temperature 294.72 °C To — 115 OF Ambient Temperature 46.11 °C Tf = 338.75 OF Air Film Temperature 170.42 °C = 0.00019 1 sq ft sec Viscosity of Air 1.8E-45 s . m/s Red = 5.45844E+02 Dimensionless Reynolds No Pr = 0.7778 Dimensionless Prandtl No. kf = 0.0146 Btu/hr- ft-°F Thermal Conductive 1) 253 W/m-°C 1v N.p si
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