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. |
Dall'interno del libro
Risultati 1-3 di 80
Pagina 11-38
... feed is necessary and feed is cold , steam smaller . my can be improved markedly by preheating the in stages with vapor bled from intermediate effects and H he evaporator . This usually represents little increase Am . total heating ...
... feed is necessary and feed is cold , steam smaller . my can be improved markedly by preheating the in stages with vapor bled from intermediate effects and H he evaporator . This usually represents little increase Am . total heating ...
Pagina 13-25
... feed is introduced above tray 3 ; nine theoretical trays required . 1.0 0.8 Feed introduced above tray Mole fraction ethanol in vapor Q2 0.4 0.6 90 --ZF , Yi Mole fraction ethanol in vapor 1.0 Feed introduced above tray 5 0.8 96 0.6 0.4 ...
... feed is introduced above tray 3 ; nine theoretical trays required . 1.0 0.8 Feed introduced above tray Mole fraction ethanol in vapor Q2 0.4 0.6 90 --ZF , Yi Mole fraction ethanol in vapor 1.0 Feed introduced above tray 5 0.8 96 0.6 0.4 ...
Pagina 22-101
... feed rate can have when both the reflux and boil - up capabilities of a column are overtaxed . It is apparent that the control plate , whether in the top or bottom , Effect of Feed Temperature Saturated liquid feed Subcooled feed XF وه ...
... feed rate can have when both the reflux and boil - up capabilities of a column are overtaxed . It is apparent that the control plate , whether in the top or bottom , Effect of Feed Temperature Saturated liquid feed Subcooled feed XF وه ...
Sommario
DATA AND FUNDAMENTALS Section | 1-1 |
Mathematics 2 | 2-3 |
DIFFERENTIAL EQUATIONS | 2-4 |
Copyright | |
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