AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 82
... Streams Stream F1 Yi kg / s g / kg g / kg R1 5.0 0.5 0.1 R2 10.0 0.25 0.05 Lean Streams $ / kg Stream S Xj x ; ' t Cj g / kg g / kg LI 0.05 0.7 8.2 L2 0.04 0.6 0.15 The equilibrium governing the contaminant transfer between the rich streams ...
... Streams Stream F1 Yi kg / s g / kg g / kg R1 5.0 0.5 0.1 R2 10.0 0.25 0.05 Lean Streams $ / kg Stream S Xj x ; ' t Cj g / kg g / kg LI 0.05 0.7 8.2 L2 0.04 0.6 0.15 The equilibrium governing the contaminant transfer between the rich streams ...
Page 146
... Stream . " stream ID process simu- sink unit lator ID op source unit op sink Unit operationo source Stream Figure 3. Current PDXI model for simulator topology . Fig . 4 shows two alternate models for representing simulator topology ...
... Stream . " stream ID process simu- sink unit lator ID op source unit op sink Unit operationo source Stream Figure 3. Current PDXI model for simulator topology . Fig . 4 shows two alternate models for representing simulator topology ...
Page 191
... stream to 100 ° F ( cooling water temperature ) and then flash , filter and decant , depending on the phases obtained . Some- times both a high and a low pressure flash are desirable . 6. If the reactor exit stream is a liquid , in some ...
... stream to 100 ° F ( cooling water temperature ) and then flash , filter and decant , depending on the phases obtained . Some- times both a high and a low pressure flash are desirable . 6. If the reactor exit stream is a liquid , in some ...
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