AIChE Symposium Series, Volume 91, Issue 304American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 98
... energy ; this is a natural phenomenon which will never be overcome . TOTAL PRIMARY ENERGY INPUT ( Ei ) FUEL PRODUCTION SYSTEM EFFICIENCY = Ed / Ei TOTAL DELIVERED ENERGY ( Ed ) as the final link in the delivery chain transporting goods ...
... energy ; this is a natural phenomenon which will never be overcome . TOTAL PRIMARY ENERGY INPUT ( Ei ) FUEL PRODUCTION SYSTEM EFFICIENCY = Ed / Ei TOTAL DELIVERED ENERGY ( Ed ) as the final link in the delivery chain transporting goods ...
Page 99
... energy associated with the sale of fruit juice in two different sizes of aseptic brick . Size ( mL ) Energy per Energy container ( MJ ) litre ( MJ ) per 125 2.19 17.52 1 2 3 m1 m2 m3 2000 7.95 3.98 E1 E2 E3 E1 , E2 and E3 are energy per ...
... energy associated with the sale of fruit juice in two different sizes of aseptic brick . Size ( mL ) Energy per Energy container ( MJ ) litre ( MJ ) per 125 2.19 17.52 1 2 3 m1 m2 m3 2000 7.95 3.98 E1 E2 E3 E1 , E2 and E3 are energy per ...
Page 101
... energy requirements of some fi- nal products of the chemical industry . Transactions of the World Energy Conference , 18 , Section E. Meadows , D.H. , Meadows , D.L. , Randers , J. & Behrens , W.B. ( 1972 ) . The limits to growth . ISBN ...
... energy requirements of some fi- nal products of the chemical industry . Transactions of the World Energy Conference , 18 , Section E. Meadows , D.H. , Meadows , D.L. , Randers , J. & Behrens , W.B. ( 1972 ) . The limits to growth . ISBN ...
Contents
Keynote Address | 1 |
Separation System Synthesis and Design | 7 |
Modeling and Analysis of Multicomponent Separation Processes | 19 |
Copyright | |
30 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