AIChE Symposium Series, Issue 323 |
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Page 13
... interactions involving more than one source ) . For the basic organic systems that have been parametrized ... interactions , and the repulsive electron- electron interactions . H = - h2 h2 + Σ - -Σ Ма ΣΣ a ZZ B Ra - RB Zae ΣΣ + r - Ra ΣΣ ...
... interactions involving more than one source ) . For the basic organic systems that have been parametrized ... interactions , and the repulsive electron- electron interactions . H = - h2 h2 + Σ - -Σ Ма ΣΣ a ZZ B Ra - RB Zae ΣΣ + r - Ra ΣΣ ...
Page 107
... Interactions between Process Design and Process Control ( J.D. Perkins , Ed . ) , pp . 75-86 . IFAC Workshop , London . Pergamon . 33. Laing , D.M. and J.W. Ponton ( 1992 ) . In : Interactions between Process De- sign and Process ...
... Interactions between Process Design and Process Control ( J.D. Perkins , Ed . ) , pp . 75-86 . IFAC Workshop , London . Pergamon . 33. Laing , D.M. and J.W. Ponton ( 1992 ) . In : Interactions between Process De- sign and Process ...
Page 372
... interactions on the molecular level . These can be captured , at least partially , by using a cubic equation of state ( EOS ) model , and by then determining the binary interaction coefficients of each component with CO2 . The intrinsic ...
... interactions on the molecular level . These can be captured , at least partially , by using a cubic equation of state ( EOS ) model , and by then determining the binary interaction coefficients of each component with CO2 . The intrinsic ...
Contents
INVITED PAPERS | 1 |
RECENT DEVELOPMENTS | 21 |
The Web and Flow of Information in Pharmaceutical RD | 23 |
Copyright | |
45 other sections not shown
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activities addition AIChE algorithm allow alternatives analysis application approach batch bound calculations changes Chem chemical codes column Comp complex components composition computational concepts considered constraints continuous cost defined described detailed determine distillation dynamic economic effect efficient energy engineering equations equipment et al evaluation example experiments feed Figure Floudas flow flowsheet formulation function given global optimization Grossmann heat important improve increase industry integration involved lifecycle linear material mathematical methods molecular networks nonlinear objective obtained operating parameters particle performance phase plant possible predict presented problem procedure process design process modeling programming properties proposed reaction reactor reduced selection separation shown shows simulation solution solved specific stage step strategy structure synthesis techniques temperature types unit variables