AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
From inside the book
Results 1-3 of 86
Page 221
... Algorithm for MINLP Optimization of Pro- cess Flowsheets . Presented at AIChE Annual Meeting , San Francisco . Tuy , H. , Thieu , T.V. , and Thai , N.Q. ( 1985 ) . A Conical Algorithm for Globally Minimizing a Concave Function over a ...
... Algorithm for MINLP Optimization of Pro- cess Flowsheets . Presented at AIChE Annual Meeting , San Francisco . Tuy , H. , Thieu , T.V. , and Thai , N.Q. ( 1985 ) . A Conical Algorithm for Globally Minimizing a Concave Function over a ...
Page 362
... algorithms successfully tracked the Newton homotopy continuation path to the solution vector at t = 1 , with Algorithm ( iii ) showing the highest efficiency ( see Table 2 for results of path - tracking ) . This was due in part to the ...
... algorithms successfully tracked the Newton homotopy continuation path to the solution vector at t = 1 , with Algorithm ( iii ) showing the highest efficiency ( see Table 2 for results of path - tracking ) . This was due in part to the ...
Page 363
... Algorithm ( ii ) re- quired an increase in the number of LU decompositions of over 100 % in order to correctly trace the path without the monitoring phase . Conclusions Of the three algorithms tested here , the one proposed by Corvalan ...
... Algorithm ( ii ) re- quired an increase in the number of LU decompositions of over 100 % in order to correctly trace the path without the monitoring phase . Conclusions Of the three algorithms tested here , the one proposed by Corvalan ...
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