AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 109
... linear plant model . The best steady - state operating point taking account of the ball size may then be determined by solving a linear programming problem ( assuming a linear objective and linear con- straints ) . Of course , the ...
... linear plant model . The best steady - state operating point taking account of the ball size may then be determined by solving a linear programming problem ( assuming a linear objective and linear con- straints ) . Of course , the ...
Page 204
... Linear Inequalities . Comments Boolean Ex - Representa- pression tion as Linear Inequalities Logical Relation Logical OR Logical AND Implica- tion P1 P2 Equiva- P1 if and only lence if P2 ( P1 P2 ) ^ ( P2⇒ P1 ) P1 v P2 v ... y1 + y2 + ...
... Linear Inequalities . Comments Boolean Ex - Representa- pression tion as Linear Inequalities Logical Relation Logical OR Logical AND Implica- tion P1 P2 Equiva- P1 if and only lence if P2 ( P1 P2 ) ^ ( P2⇒ P1 ) P1 v P2 v ... y1 + y2 + ...
Page 308
... linear expression is a very widely used technique . For example , the Antoine equation ( Eq . 5 ) , which is non- linear in parameter C , can be linearized using the follow- ing transformation : T log P = ( B + AC ) + AT - C logP ( 9 ) ...
... linear expression is a very widely used technique . For example , the Antoine equation ( Eq . 5 ) , which is non- linear in parameter C , can be linearized using the follow- ing transformation : T log P = ( B + AC ) + AT - C logP ( 9 ) ...
Contents
Keynote Address | 1 |
Separation System Synthesis and Design | 7 |
Modeling and Analysis of Multicomponent Separation Processes | 19 |
Copyright | |
29 other sections not shown
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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