Mass-transfer OperationsMcGraw-Hill, 1980 - 784 pagine |
Dall'interno del libro
Risultati 1-3 di 42
Pagina 664
... drier . This is largely the result of inadequate and nonuniform air movement inside the drier . It is important to eliminate stagnant air pockets and to maintain reasonably uniform air humidity and temperature throughout the drier . In ...
... drier . This is largely the result of inadequate and nonuniform air movement inside the drier . It is important to eliminate stagnant air pockets and to maintain reasonably uniform air humidity and temperature throughout the drier . In ...
Pagina 687
... drier and consequently its exit temperature and humidity . For this reason also it is used to avoid case hardening and other problems associated with batch drying . Tunnel Driers These direct driers are essentially adaptations of the truck ...
... drier and consequently its exit temperature and humidity . For this reason also it is used to avoid case hardening and other problems associated with batch drying . Tunnel Driers These direct driers are essentially adaptations of the truck ...
Pagina 692
... drier is frequently used when recovery of the evaporated liquid is necessary . 4. Direct - indirect . These driers ... drier , the hot gas may enter the center tube at 650 to 980 ° C ( 1200 to 1800 ° F ) , cool to 200 to 480 ° C ( 400 to ...
... drier is frequently used when recovery of the evaporated liquid is necessary . 4. Direct - indirect . These driers ... drier , the hot gas may enter the center tube at 650 to 980 ° C ( 1200 to 1800 ° F ) , cool to 200 to 480 ° C ( 400 to ...
Sommario
Diffusion and Mass Transfer | 19 |
MassTransfer Coefficients | 45 |
Diffusion in Solids | 88 |
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Parole e frasi comuni
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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Use of Adsorbents for the Removal of Pollutants from Wastewater Gordon McKay Anteprima limitata - 1995 |