Mass-transfer OperationsMcGraw-Hill, 1980 - 784 pagine |
Dall'interno del libro
Risultati 1-3 di 69
Pagina 278
... solution without resort to experimental determination . There are four significant characteristics of ideal solutions , all interrelated : 1. The average intermolecular forces of attraction and repulsion in the solution are unchanged on ...
... solution without resort to experimental determination . There are four significant characteristics of ideal solutions , all interrelated : 1. The average intermolecular forces of attraction and repulsion in the solution are unchanged on ...
Pagina 559
... solution is to be extracted with benzene to remove 95 % of the dioxane . The benzene is dioxane - free . ( a ) Calculate the solvent requirement for a single batch operation . ( b ) If the extraction were done with equal amounts of ...
... solution is to be extracted with benzene to remove 95 % of the dioxane . The benzene is dioxane - free . ( a ) Calculate the solvent requirement for a single batch operation . ( b ) If the extraction were done with equal amounts of ...
Pagina 652
... solution and observing the equilibrium color reached in each case . The data , with the quantity of carbon expressed on the basis of the sugar content of the solution , are as follows : kg carbon / kg dry sugar 0 0.005 0.01 0.015 0.02 ...
... solution and observing the equilibrium color reached in each case . The data , with the quantity of carbon expressed on the basis of the sugar content of the solution , are as follows : kg carbon / kg dry sugar 0 0.005 0.01 0.015 0.02 ...
Sommario
Diffusion and Mass Transfer | 19 |
MassTransfer Coefficients | 45 |
Diffusion in Solids | 88 |
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acetone adsorbent adsorption AIChE average azeotrope benzene bubble C₁ calculated carbon Chap Chem Chemical component composition computed concentration condenser constant countercurrent density diagram diameter diffusion dimensionless distillation downspout drier dry air dry gas dry-bulb temperature enthalpy entrainment equation equilibrium curve estimated extraction feed Figure fluid gases h₁ heat-transfer holdup humidity Illustration impeller insoluble interfacial kg/m² kg/m³ kg/s kJ/kmol kmol kmol/m² latent heat lb/ft² leaching m²/s m³/s mass transfer mass-transfer coefficient methanol minimum mixture mmHg mole fraction N/m² operating line overall packed towers partial pressure phase plotted pressure drop Prog Raschig rings reboiler reflux ratio relative Reynolds number saturated shown in Fig slope solid solubility solution solvent stage std atm stream substance surface temperature theoretical trays transfer units tray efficiency tray towers vapor pressure vessel viscosity wet-bulb wet-bulb temperature X₁ Y₁ Y₂
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