AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 19
... equations are discussed , with particular attention given to the use of Newton's method ( including highlighting ... equations that model equilibrium stages are known as the MESH equations . The M equations are the Material balance ...
... equations are discussed , with particular attention given to the use of Newton's method ( including highlighting ... equations that model equilibrium stages are known as the MESH equations . The M equations are the Material balance ...
Page 365
... equations is one growing application . Many engineering problems require finding roots of nonlinear equations . Application of interval arithmetic is an attractive choice because of the reduced round - off and propagation errors that ...
... equations is one growing application . Many engineering problems require finding roots of nonlinear equations . Application of interval arithmetic is an attractive choice because of the reduced round - off and propagation errors that ...
Page 366
... equations simultaneously for x and y , the four roots for equation ( 4 ) were obtained as intervals . This procedure was also em- ployed on those equations known to have complex roots amongst the remaining 13 chemical engineering ...
... equations simultaneously for x and y , the four roots for equation ( 4 ) were obtained as intervals . This procedure was also em- ployed on those equations known to have complex roots amongst the remaining 13 chemical engineering ...
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