AIChE Symposium Series, Issue 323 |
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Results 1-3 of 78
Page 33
... plant . This has the merit of eliminating plant construction time . The ability to fit processes into existing plants is an important feature of the training of new development chemists . They must be aware of plant limitations and ...
... plant . This has the merit of eliminating plant construction time . The ability to fit processes into existing plants is an important feature of the training of new development chemists . They must be aware of plant limitations and ...
Page 280
... plant layout problem . Finally , a simultaneous approach to plant design , scheduling and layout was adopted by Realff et al . ( 1996 ) for the case of pipeless batch plants . This paper presents a mathematical formulation for the ...
... plant layout problem . Finally , a simultaneous approach to plant design , scheduling and layout was adopted by Realff et al . ( 1996 ) for the case of pipeless batch plants . This paper presents a mathematical formulation for the ...
Page 299
... plant because there is no pipeline between units . The pipeless batch plant is also called the registered trademark such as AIBOS and MILOX . Raw Materials Products Storage Unit 1 Unit 2 Unit N Storage Mobile Vessel Figure 1 Batch process ...
... plant because there is no pipeline between units . The pipeless batch plant is also called the registered trademark such as AIBOS and MILOX . Raw Materials Products Storage Unit 1 Unit 2 Unit N Storage Mobile Vessel Figure 1 Batch process ...
Contents
INVITED PAPERS | 1 |
RECENT DEVELOPMENTS | 21 |
The Web and Flow of Information in Pharmaceutical RD | 23 |
Copyright | |
45 other sections not shown
Common terms and phrases
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