AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 85
... tion Theory and Applications , 1 , 27-39 . Jackson , R. ( 1968b ) . Optimization of Chemical Reactors with Re- spect to Flow Configuration . Journal of Optimization Theory and Applications , 2 , 240 . Jacob , A. ( 1991 ) . Recycling ...
... tion Theory and Applications , 1 , 27-39 . Jackson , R. ( 1968b ) . Optimization of Chemical Reactors with Re- spect to Flow Configuration . Journal of Optimization Theory and Applications , 2 , 240 . Jacob , A. ( 1991 ) . Recycling ...
Page 148
... tion . If Tc can be adjusted to improve the fit of the equa- tion , then Tc is a coefficient . If the value of Tc is the best estimate for a substance then Tc is a point property . A point property is an intrinsic value not subject to ...
... tion . If Tc can be adjusted to improve the fit of the equa- tion , then Tc is a coefficient . If the value of Tc is the best estimate for a substance then Tc is a point property . A point property is an intrinsic value not subject to ...
Page 296
... tion with recycling the reactants . However , the recycling option is infeasible in the current operating scenario . This option might become more attractive if sulfur dioxide emission standards become more stringent or butadiene ...
... tion with recycling the reactants . However , the recycling option is infeasible in the current operating scenario . This option might become more attractive if sulfur dioxide emission standards become more stringent or butadiene ...
Contents
Keynote Address | 1 |
Separation System Synthesis and Design | 7 |
Modeling and Analysis of Multicomponent Separation Processes | 19 |
Copyright | |
29 other sections not shown
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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