AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 145
... Figure 2 presents an alternate model of a port from one of our earlier papers [ 1 ] . In this figure a piping compo- nent , such as an elbow , pipe or tee , has pipe nodes . Thus a pipe has two nodes and a tee has three nodes ...
... Figure 2 presents an alternate model of a port from one of our earlier papers [ 1 ] . In this figure a piping compo- nent , such as an elbow , pipe or tee , has pipe nodes . Thus a pipe has two nodes and a tee has three nodes ...
Page 239
... Figure 1. Tetrahedral phase diagram with sim- ple eutectics . Figure 2.a shows the equipment configuration for the separation of three solutes , A , B and C , which exhibit the phase behavior depicted in Figure 2.b. The stream num- bers ...
... Figure 1. Tetrahedral phase diagram with sim- ple eutectics . Figure 2.a shows the equipment configuration for the separation of three solutes , A , B and C , which exhibit the phase behavior depicted in Figure 2.b. The stream num- bers ...
Page 240
... Figure 5. The use of two loops to separate a three - component mixture . Figure 4. Process flowsheet for the separation of components whose joint solubilities increase with increasing temperature . A sequence of ( n - 1 ) loops can be ...
... Figure 5. The use of two loops to separate a three - component mixture . Figure 4. Process flowsheet for the separation of components whose joint solubilities increase with increasing temperature . A sequence of ( n - 1 ) loops can be ...
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