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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Pagina 13-33
... components . Returning to the ethanol - propanol - bu- tanol example , suppose the input moles and desired output moles are as follows : Moles / hr . of component in Component Feed Overhead Bottoms Ethanol . Propanol . Butanol . 100 85 ...
... components . Returning to the ethanol - propanol - bu- tanol example , suppose the input moles and desired output moles are as follows : Moles / hr . of component in Component Feed Overhead Bottoms Ethanol . Propanol . Butanol . 100 85 ...
Pagina 13-35
... component A Component is chosen as 2.0 X 10-4 2.33 X 10-4 3.0 X 10-4 A 0.346 0.504 0.677 B 0.630 0.477 0.310 C D 0.0237 0.00000963 0.0186 0.00000767 0.0129 0.00000552 If all the non - key components are appreciably lighter than the ...
... component A Component is chosen as 2.0 X 10-4 2.33 X 10-4 3.0 X 10-4 A 0.346 0.504 0.677 B 0.630 0.477 0.310 C D 0.0237 0.00000963 0.0186 0.00000767 0.0129 0.00000552 If all the non - key components are appreciably lighter than the ...
Pagina 13-36
... Component A Component Light key Component Heavier - than - heavy key -Feed tray- Component 4 2 Reboiler 0.1 0.2 0.3 0.4 0.5 0.6 Composition , mole fraction 0.7 0.8 0.9 FIG . 13-38 . Typical variation of tray composition with position in ...
... Component A Component Light key Component Heavier - than - heavy key -Feed tray- Component 4 2 Reboiler 0.1 0.2 0.3 0.4 0.5 0.6 Composition , mole fraction 0.7 0.8 0.9 FIG . 13-38 . Typical variation of tray composition with position in ...
Sommario
DATA AND FUNDAMENTALS Section | 1-1 |
Mathematics 2 | 2-3 |
DIFFERENTIAL EQUATIONS | 2-4 |
Copyright | |
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