LEADER 05112nam 2200625Ia 450 001 9910144003803321 005 20170814190246.0 010 $a1-281-08792-0 010 $a9786611087920 010 $a3-527-60918-0 010 $a3-527-60908-3 035 $a(CKB)1000000000376059 035 $a(EBL)481901 035 $a(OCoLC)180231569 035 $a(SSID)ssj0000198592 035 $a(PQKBManifestationID)11172241 035 $a(PQKBTitleCode)TC0000198592 035 $a(PQKBWorkID)10170486 035 $a(PQKB)10457841 035 $a(MiAaPQ)EBC481901 035 $a(PPN)188670106 035 $a(EXLCZ)991000000000376059 100 $a20060728d2006 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 10$aMass transfer$b[electronic resource] $efrom fundamentals to modern industrial applications /$fKoichi Asano 210 $aWeinheim $cWiley-VCH$dc2006 215 $a1 online resource (291 p.) 300 $aDescription based upon print version of record. 311 $a3-527-31460-1 320 $aIncludes bibliographical references and index. 327 $aMass Transfer; Contents; Preface; 1 Introduction; 1.1 The Beginnings of Mass Transfer; 1.2 Characteristics of Mass Transfer; 1.3 Three Fundamental Laws of Transport Phenomena; 1.3.1 Newton's Law of Viscosity; 1.3.2 Fourier's Law of Heat Conduction; 1.3.3 Fick's Law of Diffusion; 1.4 Summary of Phase Equilibria in Gas-Liquid Systems; References; 2 Diffusion and Mass Transfer; 2.1 Motion of Molecules and Diffusion; 2.1.1 Diffusion Phenomena; 2.1.2 Definition of Diffusional Flux and Reference Velocity of Diffusion [1, 2]; 2.1.3 Binary Diffusion Flux; 2.2 Diffusion Coefficients 327 $a2.2.1 Binary Diffusion Coefficients in the Gas Phase2.2.2 Multicomponent Diffusion Coefficients in the Gas Phase; Example 2.1; Solution; 2.3 Rates of Mass Transfer; 2.3.1 Definition of Mass Flux; 2.3.2 Unidirectional Diffusion in Binary Mass Transfer; 2.3.3 Equimolal Counterdiffusion; 2.3.4 Convective Mass Flux for Mass Transfer in a Mixture of Vapors; Example 2.2; Solution; 2.4 Mass Transfer Coefficients; Example 2.3; Solution; 2.5 Overall Mass Transfer Coefficients; References; 3 Governing Equations of Mass Transfer; 3.1 Laminar and Turbulent Flow 327 $a3.2 Continuity Equation and Diffusion Equation3.2.1 Continuity Equation; 3.2.2 Diffusion Equation in Terms of Mass Fraction; 3.2.3 Diffusion Equation in Terms of Mole Fraction; 3.3 Equation of Motion and Energy Equation; 3.3.1 The Equation of Motion (Navier-Stokes Equation); 3.3.2 The Energy Equation; 3.3.3 Governing Equations in Cylindrical and Spherical Coordinates; 3.4 Some Approximate Solutions of the Diffusion Equation; 3.4.1 Film Model [6]; 3.4.2 Penetration Model; 3.4.3 Surface Renewal Model; Example 3.1; Solution; 3.5 Physical Interpretation of Some Important Dimensionless Numbers 327 $a3.5.1 Reynolds Number3.5.2 Prandtl Number and Schmidt Number; 3.5.3 Nusselt Number; 3.5.4 Sherwood Number; 3.5.5 Dimensionless Numbers Commonly Used in Heat and Mass Transfer; Example 3.2; Solution; 3.6 Dimensional Analysis; 3.6.1 Principle of Similitude and Dimensional Homogeneity; 3.6.2 Finding Dimensionless Numbers and Pi Theorem; References; 4 Mass Transfer in a Laminar Boundary Layer; 4.1 Velocity Boundary Layer; 4.1.1 Boundary Layer Equation; 4.1.2 Similarity Transformation; 4.1.3 Integral Form of the Boundary Layer Equation; 4.1.4 Friction Factor 327 $a4.2 Temperature and Concentration Boundary Layers4.2.1 Temperature and Concentration Boundary Layer Equations; 4.2.2 Integral Form of Thermal and Concentration Boundary Layer Equations; Example 4.1; Solution; 4.3 Numerical Solutions of the Boundary Layer Equations; 4.3.1 Quasi-Linearization Method; 4.3.2 Correlation of Heat and Mass Transfer Rates; Example 4.2; Solution; 4.4 Mass and Heat Transfer in Extreme Cases; 4.4.1 Approximate Solutions for Mass Transfer in the Case of Extremely Large Schmidt Numbers 327 $a4.4.2 Approximate Solutions for Heat Transfer in the Case of Extremely Small Prandtl Numbers [6] 330 $aThis didactic approach to the principles and modeling of mass transfer as it is needed in modern industrial processes is unique in combining a step-by-step introduction to all important fundamentals with the most recent applications. Based upon the renowned author's successful new modeling method as used for the O-18 process, the exemplary exercises included in the text are fact-proven, taken directly from existing chemical plants.Fascinating reading for chemists, graduate students, chemical and process engineers, as well as thermodynamics physicists. 606 $aMass transfer 606 $aTransport theory 615 0$aMass transfer. 615 0$aTransport theory. 676 $a530.475 676 $a660.2832 700 $aAsano$b Ko?ichi$f1926-$0968923 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910144003803321 996 $aMass transfer$92201237 997 $aUNINA