AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 17
... Feed Distillate Bottoms 0.7400 0.8916 0.0900 0.1074 0.1700 0.0010 0.0001 0.0049 0.9950 r = 0.2 S = 7.95 q = 1 0.6 * 2 0.4- 0.2 Liquid Boiling Envelope Bottoms Feed P = 1 atm Stages : Reboiler : 1 Feed : 8 Condenser : 14 Vapor Line ...
... Feed Distillate Bottoms 0.7400 0.8916 0.0900 0.1074 0.1700 0.0010 0.0001 0.0049 0.9950 r = 0.2 S = 7.95 q = 1 0.6 * 2 0.4- 0.2 Liquid Boiling Envelope Bottoms Feed P = 1 atm Stages : Reboiler : 1 Feed : 8 Condenser : 14 Vapor Line ...
Page 32
... Feed L ,, x , In ( 23 ) = Ir dx ln + -X . x2 + Sx , ( α ( x ) − 1 ) ( 1 − x ) x ( B ) Figure 5. Schematic diagram ... Feed A.B ( a ) Recycle Feed A - 8 ( b ) Feed A B dGB ( c ) Figure 6. Cascades for membrane separation processes . ( a ) ...
... Feed L ,, x , In ( 23 ) = Ir dx ln + -X . x2 + Sx , ( α ( x ) − 1 ) ( 1 − x ) x ( B ) Figure 5. Schematic diagram ... Feed A.B ( a ) Recycle Feed A - 8 ( b ) Feed A B dGB ( c ) Figure 6. Cascades for membrane separation processes . ( a ) ...
Page 268
American Institute of Chemical Engineers. Feed D Feed E Feed F 000000 Feed A Feed B Feed C Blend AH Reaction BC_GH Feed GH Distillation GH Reaction_DE_GI Feed Gl Store AH Feed H Store & cool_G 0000 Store G Feed E Reaction_DE_GI ) Feed Gl Y1 ...
American Institute of Chemical Engineers. Feed D Feed E Feed F 000000 Feed A Feed B Feed C Blend AH Reaction BC_GH Feed GH Distillation GH Reaction_DE_GI Feed Gl Store AH Feed H Store & cool_G 0000 Store G Feed E Reaction_DE_GI ) Feed Gl Y1 ...
Contents
Keynote Address | 1 |
Separation System Synthesis and Design | 7 |
Modeling and Analysis of Multicomponent Separation Processes | 19 |
Copyright | |
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Common terms and phrases
acetic acid activities AIChE algorithm alternatives analysis application approach attainable region azeotrope azeotropic distillation batch branch and bound calculations cess Chem Chemical Engineering chemical process complex components composition concepts constraints cost CSTR data models decision-mapping defined described developed distillation column dynamic energy Engng environment equations equilibrium equipment example feed Figure Floudas flow flowsheet formulation function global optimization Grossmann hierarchical implementation industrial integration interface linear liquid logic mass material mathematical methanol methods methyl acetate MILP MINLP mixture n-dim network synthesis Newton's method nonlinear nonlinear programming paper parameters phase pinch plant pressure problem procedure process design process modelling process synthesis programming properties reac reaction reactive distillation reactor network recycle Seider separation system SimRefinery simulation solution solvent solving specific stage strategy stream structure target task techniques temperature tion unit operations values vapor variables