Mass-transfer OperationsMcGraw-Hill, 1967 - 717 pagine Author's purpose is "to provide a vehicle for teaching, either through a formal course or through self-study, the techniques of, and principles of equipment design for, the mass-transfer operations of chemical engineering." As before, these operations are largely the responsibility of the chemical engineer, but increasingly practitioners of other engineering disciplines are finding them necessary for their work. This is especially true for those engaged in pollution control and environment protection, where separation processes predominate, and in, for example, extractive metallurgy, where more sophisticated and diverse methods of separation are increasingly relied upon. |
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Sommario
PART ONE DIFFUSION AND MASS TRANSFER | 13 |
Molecular Diffusion in Fluids | 15 |
Masstransfer Coefficients | 38 |
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acetone adsorbent adsorption AIChE azeotrope batch benzene Btu/lb mole bubble point C₁ calculated carbon centipoise Chem chemical components composition computed concentration condenser constant countercurrent cross section density diagram diameter diffusion dimensionless distillation drier dry air dry solid effluent enthalpy equation equilibrium curve ethanol extraction feed flow fluid ft/sec gases humidity ideal trays Illustration insoluble interfacial latent heat lb dry lb mole lb water/lb dry lb/cu ft lb/hr leaching liquid mass transfer mass-transfer coefficient minimum mixture moisture content mole fraction molecular operating line overall partial pressure particles phase plotted pressure drop R₁ raffinate Raschig rings reboiler reflux ratio relative residue saturated separation shown in Fig slope solubility solution solvent sq ft stream substance surface temperature theoretical trays tie line transfer units vapor pressure velocity viscosity volatile weight wet-bulb temperature X₁ Y₁ Y₂ zone
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