Mass-transfer OperationsMcGraw-Hill, 1980 - 784 pagine |
Dall'interno del libro
Risultati 1-3 di 71
Pagina 231
... plotted against temper- ature on the psychrometric chart . Similarly H for the dry gas can be plotted . Enthalpies for unsaturated mixtures can then be interpolated between the saturated and dry values at the same temperature according ...
... plotted against temper- ature on the psychrometric chart . Similarly H for the dry gas can be plotted . Enthalpies for unsaturated mixtures can then be interpolated between the saturated and dry values at the same temperature according ...
Pagina 319
... plotted on their respective portions . Similarly the counterparts of these equations for RA 1.3 , Rc - 0.7 and RA 1.5 , 0.5 are plotted . By interpolation , the intersections of the curves with the equilibrium lines XA , i = Rc satisfy ...
... plotted on their respective portions . Similarly the counterparts of these equations for RA 1.3 , Rc - 0.7 and RA 1.5 , 0.5 are plotted . By interpolation , the intersections of the curves with the equilibrium lines XA , i = Rc satisfy ...
Pagina 574
... plotted on the ordinate . Points of equal temperature for the vapor pressure of pure acetone and the partial pressure of adsorbate were then plotted . Thus , point A of Fig . 11.1 ( p * 190 mmHg , 100 ° C ) was plotted on Fig . 11.5 at ...
... plotted on the ordinate . Points of equal temperature for the vapor pressure of pure acetone and the partial pressure of adsorbate were then plotted . Thus , point A of Fig . 11.1 ( p * 190 mmHg , 100 ° C ) was plotted on Fig . 11.5 at ...
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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