AIChE Symposium Series, Issue 323 |
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Page 88
... defined by Equation ( 8 ) . Let [ H ] be a real symmetric interval matrix such that H1 ( x ) [ H ] , Vx € [ x2 , x2 ] . ( 6 ) U if x " > 0 ifx " < 0 If Univariate Concave Terms : Univariate concave functions are underestimated by their ...
... defined by Equation ( 8 ) . Let [ H ] be a real symmetric interval matrix such that H1 ( x ) [ H ] , Vx € [ x2 , x2 ] . ( 6 ) U if x " > 0 ifx " < 0 If Univariate Concave Terms : Univariate concave functions are underestimated by their ...
Page 280
... defined by Barbosa - Póvoa ( 1994 ) . The process recipes are defined through a State - Task Representation ( STNs , Kondili et al ( 1988 ) ) and the plant is characterised through a normal flowsheet - equipment network of vessels ...
... defined by Barbosa - Póvoa ( 1994 ) . The process recipes are defined through a State - Task Representation ( STNs , Kondili et al ( 1988 ) ) and the plant is characterised through a normal flowsheet - equipment network of vessels ...
Page 436
... defined in KIF ( Knowledge Interchange Format ) on which the ontology server is based . KIF provides a lisp - like syntax for representing first - order logic sentences . Processor Semantic Formatter Syntactic Message Handler message ...
... defined in KIF ( Knowledge Interchange Format ) on which the ontology server is based . KIF provides a lisp - like syntax for representing first - order logic sentences . Processor Semantic Formatter Syntactic Message Handler message ...
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