AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 159
... dim n - dim is an information modeling environment on which the three authors of the this article from Carnegie Mellon University , along with others in the n - dim group , have been working for the last four years . From observing ...
... dim n - dim is an information modeling environment on which the three authors of the this article from Carnegie Mellon University , along with others in the n - dim group , have been working for the last four years . From observing ...
Page 160
... n - dim . These models relate to two of the views shown in Fig . 2 . A user can also include any number of user - defined , labeled links to express relationships between pairs of model parts ( including self links ) . For example , one ...
... n - dim . These models relate to two of the views shown in Fig . 2 . A user can also include any number of user - defined , labeled links to express relationships between pairs of model parts ( including self links ) . For example , one ...
Page 161
American Institute of Chemical Engineers. Storage of Objects . Each n - dim object has several at- tributes such as a unique n - dim identification string , the name of an owner , a time of creation , a time of publishing , and a ...
American Institute of Chemical Engineers. Storage of Objects . Each n - dim object has several at- tributes such as a unique n - dim identification string , the name of an owner , a time of creation , a time of publishing , and a ...
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