SA2-Problem3-TiffanyParrott

SA2-Problem3-TiffanyParrott - mol/cc .0140594 .0140594...

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Results Summary Streams Material INPUT OUTPUT MIXER MIXER LIQUID LIQUID Substream: MIXED Mole Flow kmol/hr METHY-01 .7500000 .7500000 METHA-01 .2500000 .2500000 Total Flow kmol/hr 1.000000 1.000000 Total Flow kg/hr 63.57012 63.57012 Total Flow l/min 1.185442 1.185442 Temperature K 318.1500 318.1499 Pressure atm 1.000000 1.000000 Vapor Frac 0.0 0.0 Liquid Frac 1.000000 1.000000 Solid Frac 0.0 0.0 Enthalpy cal/mol -93066.05 -93066.05 Enthalpy cal/gm -1463.990 -1463.990 Enthalpy cal/sec -25851.68 -25851.68 Entropy cal/mol-K -81.49523 -81.49524 Entropy cal/gm-K -1.281974 -1.281974 Density
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Unformatted text preview: mol/cc .0140594 .0140594 Density gm/cc .8937609 .8937611 Average MW 63.57012 63.57012 Liq Vol 60F l/min 1.165850 1.165850 *** LIQUID PHASE *** GAMMA METHY-01 1.074988 1.074988 METHA-01 1.794206 1.794206 PHIMX METHY-01 .6922299 .6922275 METHA-01 .7878562 .7878531 PL atm METHY-01 .6439418 .6439395 METHA-01 .4391114 .4391096 TBUB K 326.8808 326.8808 TDEW K 327.0876 327.0876 PDEW atm .7131699 .7131674 PBUB atm .7161366 .7161340 Run:SA2-Problem3-TiffanyParrott Page 1 2/18/2009 04:53:PM...
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