AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 90
... mixture in fce EVENT 62 ( 0.100 ) People present at 40K fce TP = emerg sd EVENT 63 ( 0.500 ) Hit by expl / fire TP = emerg shutdown EVENT 64 ( 0.100 ) Delayed ignition of flammable mixture in fce M.C.S. No. 4 Prob . Rate = 1/10000000 ...
... mixture in fce EVENT 62 ( 0.100 ) People present at 40K fce TP = emerg sd EVENT 63 ( 0.500 ) Hit by expl / fire TP = emerg shutdown EVENT 64 ( 0.100 ) Delayed ignition of flammable mixture in fce M.C.S. No. 4 Prob . Rate = 1/10000000 ...
Page 147
... mixtures . Such a recursive structure often occurs with models . Recursion provides a natural way to represent a hierarchy of arbitrary depth . For example , tar sands could be treated as a mixture of sand and tar . One could regard the ...
... mixtures . Such a recursive structure often occurs with models . Recursion provides a natural way to represent a hierarchy of arbitrary depth . For example , tar sands could be treated as a mixture of sand and tar . One could regard the ...
Page 191
... mixture of three phases , i.e. aqueous liquid , organic liquid , sol- id , we normally use a liquid - solid separator to remove the solids first , and then split the two liquid phases in a decanter . Normally , we filter before we ...
... mixture of three phases , i.e. aqueous liquid , organic liquid , sol- id , we normally use a liquid - solid separator to remove the solids first , and then split the two liquid phases in a decanter . Normally , we filter before we ...
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