AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Results 1-3 of 56
Page 21
... solving BTD sys- tems and conclude that SOR methods are more efficient than the Thomas algorithm for systems with large numbers of components . How Should the Initial Guess be Obtained ? Newton's method requires initial estimates for ...
... solving BTD sys- tems and conclude that SOR methods are more efficient than the Thomas algorithm for systems with large numbers of components . How Should the Initial Guess be Obtained ? Newton's method requires initial estimates for ...
Page 176
... solving a sparse nonlinear program using a technique based on a Schur - complement implementation of a sequential quadratic programming approach . An ex- tension of the technique to sparse nonlinear least squares is then outlined . The ...
... solving a sparse nonlinear program using a technique based on a Schur - complement implementation of a sequential quadratic programming approach . An ex- tension of the technique to sparse nonlinear least squares is then outlined . The ...
Page 356
... solving and optimization techniques for solving the phase stability problem may fail to converge or may converge to an incorrect result . A technique for solving the problem with mathe- matical certainty is needed . One approach to ...
... solving and optimization techniques for solving the phase stability problem may fail to converge or may converge to an incorrect result . A technique for solving the problem with mathe- matical certainty is needed . One approach to ...
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