AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 248
... defined equivalence relation . Example 4. Let us revisit Example 2 ; the closure of decision - mapping d1 [ m , ] , 8 , ' [ m ] , follows Definition 4 . Domain m1 is the union of set m1 and the set of materials involved in the operating ...
... defined equivalence relation . Example 4. Let us revisit Example 2 ; the closure of decision - mapping d1 [ m , ] , 8 , ' [ m ] , follows Definition 4 . Domain m1 is the union of set m1 and the set of materials involved in the operating ...
Page 328
... definition of the term " multifaceted " tasks and associated problems are defined for the same plant compo- nent . Thus different models of the same plant coexist in the same project . Computer - aided modelling addresses the problem of ...
... definition of the term " multifaceted " tasks and associated problems are defined for the same plant compo- nent . Thus different models of the same plant coexist in the same project . Computer - aided modelling addresses the problem of ...
Page 329
... defined as consisting of a single phase or a pseudo phase ( an average of several phases such that it appears as a single phase ) . The term system is very much used as it is defined in axi- omatic thermodynamics . The equations ...
... defined as consisting of a single phase or a pseudo phase ( an average of several phases such that it appears as a single phase ) . The term system is very much used as it is defined in axi- omatic thermodynamics . The equations ...
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