AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 150
... application domains can be integrat- ed into a spanning model provided they are properly har- monized . Maintenance implies changing the data model . Changing the data model is trivial and the existence of au- tomated mappings to ...
... application domains can be integrat- ed into a spanning model provided they are properly har- monized . Maintenance implies changing the data model . Changing the data model is trivial and the existence of au- tomated mappings to ...
Page 151
... application resource in- formation models , used to support and inte- grate the STEP parts , application protocols ( AP ) , which define the standard in terms specific to the application domain and explain how the standard should be ...
... application resource in- formation models , used to support and inte- grate the STEP parts , application protocols ( AP ) , which define the standard in terms specific to the application domain and explain how the standard should be ...
Page 367
... application to sophisticated simulation soft- ware . Acknowledgements We appreciate the assistance of Professor R. Baker Kear- fott at every step of applying INTBIS to our equations . Fi- nancial support was provided by a graduate ...
... application to sophisticated simulation soft- ware . Acknowledgements We appreciate the assistance of Professor R. Baker Kear- fott at every step of applying INTBIS to our equations . Fi- nancial support was provided by a graduate ...
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