Table of ContentsNonequilibrium Modelling Stage Model Equilibrium Stage (1) Equilibrium Stage (2) Efficiency and HETP Exact Model (1) Exact Model (2) Mass Transfer Modelling (1) Large Scale Mixing (1) Large Scale Mixing (2) Near Interfaces Mass Transfer (1) Mass Transfer (2) Simple Nonequilibrium Stage Variations Physical Data Equipment Data Examples Depropaniser Flow Rates Component Profiles, Liquid Mass Transfer Rates Murphree Efficiencies Murphree Efficiency (2) For a Binary McCabe Thiele Diagram DepropaniserTray Layouts Acetone Absorber Temp’s Mass Transfer HETP’s HETP’s (2) Extractive Distillation Component Profiles Difficult? Problems? The End |
Author: J. A. Wesselingh |