Chemical Engineers' Handbook, Volume 4,Parte 1963Robert H. Perry McGraw-Hill, 1963 - 1919 pagine Textbook on chemical industry engineering - covers theoretics, definitions, technical aspects, etc. |
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Risultati 1-3 di 89
Pagina 13-34
... computed as ( 5 ) ( 6αx1 ) / ( 26ax1 ) . Continuing the illustration , mole fraction A 25 0.50 Trace 0.00 5 671 α bati 5 672 B 24 0.48 1 0.02 0.00923 0.00946 5.0 0.0473 0.0421 0.0423 1 0.02 24 0.48 0.396 0.416 2.5 1.040 0.925 0.945 ...
... computed as ( 5 ) ( 6αx1 ) / ( 26ax1 ) . Continuing the illustration , mole fraction A 25 0.50 Trace 0.00 5 671 α bati 5 672 B 24 0.48 1 0.02 0.00923 0.00946 5.0 0.0473 0.0421 0.0423 1 0.02 24 0.48 0.396 0.416 2.5 1.040 0.925 0.945 ...
Pagina 13-40
... computed based upon this assumption . If this assumption cannot be made , it is often helpful to use the approximation of Hengstebeck [ Trans . Am . Inst . Chem . Engrs . , 42 , 309 ( 1946 ) ] to estimate the dis- tribution of the non ...
... computed based upon this assumption . If this assumption cannot be made , it is often helpful to use the approximation of Hengstebeck [ Trans . Am . Inst . Chem . Engrs . , 42 , 309 ( 1946 ) ] to estimate the dis- tribution of the non ...
Pagina 13-42
... computed by the tray - to - tray calculation from the bottom upward ; TFD is the feed - tray composition for the same component as computed from the top down ; w and d are the moles / hr . of component i in the bottoms and distillate ...
... computed by the tray - to - tray calculation from the bottom upward ; TFD is the feed - tray composition for the same component as computed from the top down ; w and d are the moles / hr . of component i in the bottoms and distillate ...
Sommario
Alphabetical Index at back of book | 1-1 |
SECTION | 1-2 |
MATHEMATICS | 1-46 |
Copyright | |
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