AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 82
... temperature specifications on these streams , a hot and a cold utility , with given inlet and exit temperatures and per unit costs , shown in Table 4 , may be utilized . Specific heat informa- tion for these streams is also provided in ...
... temperature specifications on these streams , a hot and a cold utility , with given inlet and exit temperatures and per unit costs , shown in Table 4 , may be utilized . Specific heat informa- tion for these streams is also provided in ...
Page 310
... temperature is allowed to vary freely . We will first consider a PFR : Find the optimal starting temperature ; the temperature yielding the maximum initial se- lectivity . Example We use the van der Vusse reaction scheme using the ...
... temperature is allowed to vary freely . We will first consider a PFR : Find the optimal starting temperature ; the temperature yielding the maximum initial se- lectivity . Example We use the van der Vusse reaction scheme using the ...
Page 311
... temperature : At low temperatures the shapes are con- cave , indicating a CSTR reactor . At high temperatures the shapes are fully convex , and a PFR would then yield the best product distribution . Fig . 4 shows an isothermal ...
... temperature : At low temperatures the shapes are con- cave , indicating a CSTR reactor . At high temperatures the shapes are fully convex , and a PFR would then yield the best product distribution . Fig . 4 shows an isothermal ...
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