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HMD Modeling and Simulation

Column Feed conditions (Mole fraction) other specs Other conditions [Pg.293]

DE DM Bottom Feed Methane (0.0025), Acetylene (0.0110), Ethylene mole fraction in Column top pressure = [Pg.293]

3200 kPa and 5 °C Methy[acetylene (0.0029), Ethane in bottoms = 155 Pressure drop/tray = 0.7 [Pg.293]

DP 969 kgmol/h (49 398 kg/h) At 2649 kPa And 89 °C Np = 13 Ethane (0.00053), Methylacetylene (0.0111), Propadiene (0.0111), Propene (0.5426), Propane (0.0255), 1,2-Butadiene (0.0121), 1,3-Butadiene (0.1086), Isobutane (0.0382), n-Butane (0.0421), Isobutene (0.0382), c/s-2-Butene (0.0095), trans-2-Butene (0.0095), n-Pentane (0.0744), n-Hexane (0.0716) Propylene mole fraction in overheads = 0.9116 Methylacetylene mole fraction in bottoms = 0.0013 Column top pressure = 576 kFla Pressure drop/tray = 0.7 kFla No. of ideal trays 42 Total condenser Peng-Robinson model [Pg.294]


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