AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 21
... values at intermediate values of the continua- tion parameters . Negative mole fractions at intermediate . parameter values ( as encountered by Vickery and Taylor ( 1986 ) and by Burton and Morton , 1987 ) lead to difficul- ties in the ...
... values at intermediate values of the continua- tion parameters . Negative mole fractions at intermediate . parameter values ( as encountered by Vickery and Taylor ( 1986 ) and by Burton and Morton , 1987 ) lead to difficul- ties in the ...
Page 47
... values ( by roughly one order of magnitude for every 3 sin- gular values ) . Table 2. Singular Values of the Concentration Change Matrix , in the Reaction - space Reduction Experiment . 7-9 The identification of the number of dominant ...
... values ( by roughly one order of magnitude for every 3 sin- gular values ) . Table 2. Singular Values of the Concentration Change Matrix , in the Reaction - space Reduction Experiment . 7-9 The identification of the number of dominant ...
Page 306
... values can often be set to round numbers , which are more convenient for calculations , such numbers will rarely be obtained in measured values of the dependent variable . The original source of this data ( Olson et al . , 1950 ) ...
... values can often be set to round numbers , which are more convenient for calculations , such numbers will rarely be obtained in measured values of the dependent variable . The original source of this data ( Olson et al . , 1950 ) ...
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