AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 23
... Complex Domain Flash and distillation calculations have been carried out in the complex domain by Lucia and Taylor ( 1992 ) and by Taylor et al . ( 1994 ) who found that a complex code will converge to a real solution , even from a ...
... Complex Domain Flash and distillation calculations have been carried out in the complex domain by Lucia and Taylor ( 1992 ) and by Taylor et al . ( 1994 ) who found that a complex code will converge to a real solution , even from a ...
Page 39
... complex reactions . Complex reaction networks have been tackled in dif- ferent ways in the last decade . Froment and co - workers ( 1984 , 1985 and 1988 ) used a graph theory to generate re- action paths for thermo - cracking and ...
... complex reactions . Complex reaction networks have been tackled in dif- ferent ways in the last decade . Froment and co - workers ( 1984 , 1985 and 1988 ) used a graph theory to generate re- action paths for thermo - cracking and ...
Page 130
... complex unit operations ( such as distillation col- umns ) , called " macros , " may be formed from instances of the basic models . Finally , a model of the entire plant may be formed by combining instances of both models and macros ...
... complex unit operations ( such as distillation col- umns ) , called " macros , " may be formed from instances of the basic models . Finally , a model of the entire plant may be formed by combining instances of both models and macros ...
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