AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 134
... Procedure Modelling The procedures employed for the operation of process plants have traditionally been considered to be outside the scope of process modelling tools , being perhaps more rele- vant to real - time control systems which ...
... Procedure Modelling The procedures employed for the operation of process plants have traditionally been considered to be outside the scope of process modelling tools , being perhaps more rele- vant to real - time control systems which ...
Page 195
... procedure , the modeling lan- guage uses a series of modeling elements ( shown in Couri- er font ) , which capture the following aspects , at any level of abstraction : 1. The structure of the process flowsheet , as a complete system ...
... procedure , the modeling lan- guage uses a series of modeling elements ( shown in Couri- er font ) , which capture the following aspects , at any level of abstraction : 1. The structure of the process flowsheet , as a complete system ...
Page 262
... procedure , Straub and Grossmann ( 1992 ) ) , can also be employed to reduce model size and computa- tional complexity . Finally , note that the above optimiza- tion procedure can be extended to account for the execution of different ...
... procedure , Straub and Grossmann ( 1992 ) ) , can also be employed to reduce model size and computa- tional complexity . Finally , note that the above optimiza- tion procedure can be extended to account for the execution of different ...
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