AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 63
... flowsheet and heat integration . Integration with other Process Subsystems Reactor networks are rarely designed in isolation , but rather form an important part of an overall flowsheet . Moreover , since feed preparation , product ...
... flowsheet and heat integration . Integration with other Process Subsystems Reactor networks are rarely designed in isolation , but rather form an important part of an overall flowsheet . Moreover , since feed preparation , product ...
Page 195
... flowsheet , as a complete system ( Flowsheet ) , or in terms of its units ( GenericUnit ) , and their inter- connections ( Port , Stream ) . 2. The characteristics and behavior of units , streams , reactions and materials ( Generic ...
... flowsheet , as a complete system ( Flowsheet ) , or in terms of its units ( GenericUnit ) , and their inter- connections ( Port , Stream ) . 2. The characteristics and behavior of units , streams , reactions and materials ( Generic ...
Page 223
... flowsheet alter- natives at conceptual design stage of the innovation pro- cess . The goal of process synthesis is to develop one or more schemes to implement the conversion of available raw materials into desired product materials ...
... flowsheet alter- natives at conceptual design stage of the innovation pro- cess . The goal of process synthesis is to develop one or more schemes to implement the conversion of available raw materials into desired product materials ...
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