AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
From inside the book
Results 1-3 of 81
Page 245
... parameters of the optimisation problem include the specifications of the feed streams , the equilibrium con- stants , and the economic parameters of the process . The undistributed organic feed is furnished at a rate of 100 lt / min and ...
... parameters of the optimisation problem include the specifications of the feed streams , the equilibrium con- stants , and the economic parameters of the process . The undistributed organic feed is furnished at a rate of 100 lt / min and ...
Page 308
... parameters while extremely wide confidence intervals will indicate existence of too many parameters . A comparison of the sum of squares of the deviations calcu- lated on a common basis will allow selection of the best model from among ...
... parameters while extremely wide confidence intervals will indicate existence of too many parameters . A comparison of the sum of squares of the deviations calcu- lated on a common basis will allow selection of the best model from among ...
Page 343
... parameters . Entering equations : > eqnset : = { q = CPhot * ( T1 - T2 ) , q = CPcold * ( T4 - T3 ) , q = UA * ( ( T1 - T4 ) / ( T2 - T3 ) ) / ln ( ( T1 - T4 ) / ( T2 - T3 ) ) } : Solve for q , T2 and T4 in terms of the other values ...
... parameters . Entering equations : > eqnset : = { q = CPhot * ( T1 - T2 ) , q = CPcold * ( T4 - T3 ) , q = UA * ( ( T1 - T4 ) / ( T2 - T3 ) ) / ln ( ( T1 - T4 ) / ( T2 - T3 ) ) } : Solve for q , T2 and T4 in terms of the other values ...
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