AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 113
... Design of resilient process- ing plants . I. process design under consideration of dy- namic aspects . Chem . Eng . Sci . , 37 , 245-258 . Lin , W.J. , J.D. Seader , and T.L. Wayburn ( 1987 ) . Computing mul- tiple solutions to systems ...
... Design of resilient process- ing plants . I. process design under consideration of dy- namic aspects . Chem . Eng . Sci . , 37 , 245-258 . Lin , W.J. , J.D. Seader , and T.L. Wayburn ( 1987 ) . Computing mul- tiple solutions to systems ...
Page 260
American Institute of Chemical Engineers. FLEXIBILITY , RELIABILITY AND MAINTENANCE IN PROCESS DESIGN Thomas V. Thomaidis and Efstratios N. Pistikopoulos ' Department of Chemical Engineering Imperial College London SW7 2BY Abstract In ...
American Institute of Chemical Engineers. FLEXIBILITY , RELIABILITY AND MAINTENANCE IN PROCESS DESIGN Thomas V. Thomaidis and Efstratios N. Pistikopoulos ' Department of Chemical Engineering Imperial College London SW7 2BY Abstract In ...
Page 317
... design stage to improve controllability without decreasing profitability . With this goal in mind , we investigate improving controllability by intro- ducing physical or ... Process Designs Braatz, B A Ogunnaike, J S Schwaber and W Rose.
... design stage to improve controllability without decreasing profitability . With this goal in mind , we investigate improving controllability by intro- ducing physical or ... Process Designs Braatz, B A Ogunnaike, J S Schwaber and W Rose.
Contents
Keynote Address | 1 |
Separation System Synthesis and Design | 7 |
Modeling and Analysis of Multicomponent Separation Processes | 19 |
Copyright | |
29 other sections not shown
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