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传递现象 英文PDF|Epub|txt|kindle电子书版本网盘下载
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- (美)伯德(Bird,R.B.)著 著
- 出版社: 北京:化学工业出版社
- ISBN:7502532676
- 出版时间:2002
- 标注页数:899页
- 文件大小:570MB
- 文件页数:914页
- 主题词:理论化学
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图书目录
Chapter 0 The Subject of Transport Phenomena1
Part Ⅰ Momentum TransportChapter 1 Viscosity and the Mechanisms of Momentum Transport11
1.1 Newton's Law of Viscosity(Molecular Momentum Transport)11
Ex.1.1-1 Calculation of Momentum Flux15
1.2 Generalization of Newton's Law of Viscosity16
1.3 Pressure and Temperature Dependence of Viscosity21
Ex.1.3-1 Estimation of Viscosity from Critical Properties23
1.4 Molecular Theory of the Viscosity of Gases at Low Density23
Ex.1.4-1 Computation of the Viscosity of a Gas Mixture at Low Density28
Ex.1.4-2 Prediction of the Viscosity of a Gas Mixture at Low Density28
1.5 Molecular Theory of the Viscosity of Liquids29
Ex.1.5-1 Estimation of the Viscosity of a Pure Liquid31
1.6 Viscosity of Suspensions and Emulsions31
1.7 Convective Momentum Transport34
Questions for Discussion37
Problems37
Chapter 2 Shell Momentum Balances and Velocity Distributions in Laminar Flow40
2.1 Shell Momentum Balances and Boundary Conditions41
2.2 Flow of a Falling Film42
Ex.2.2-1 Calculation of Film Velocity47
Ex.2.2-2 Falling Film with Variable Viscosity47
2.3 Flow Through a Circular Tube48
Ex.2.3-1 Determination of Viscosity from Capillary Flow Data52
Ex.2.3-2 Compressible Flow in a Horizontal Circular Tube53
2.4 Flow through an Annulus53
2.5 Flow of Two Adjacent Immiscible Fluids56
2.6 Creeping Flow around a Sphere58
Ex.2.6-1 Determination of Viscosity from the Terminal Velocity of a Falling Sphere61
Questions for Discussion61
Problems62
Chapter 3 The Equations of Change for Isothermal Systems75
3.1 The Equation of Continuity77
Ex.3.1-1 Normal Stresses at Solid Surfaces for Incompressible Newtonian Fluids78
3.2 The Equation of Motion78
3.3 The Equation of Mechanical Energy81
3.4 The Equation of Angular Momentum82
3.5 The Equations of Change in Terms of the Substantial Derivative83
Ex.3.5-1 The Bernoulli Equation for the Steady Flow of Inviscid Fluids86
3.6 Use of the Equations of Change to Solve Flow Problems86
Ex.3.6-1 Steady Flow in a Long Circular Tube88
Ex.3.6-2 Falling Film with Variable Viscosity89
Ex.3.6-3 Operation ofa Couette Viscometer89
Ex.3.6-4 Shape of the Surface of a Rotating Liquid93
Ex.3.6-5 Flow near a Slowly Rotating Sphere95
3.7 Dimensional Analysis of the Equations of Change97
Ex.3.7-1 Transverse Flow around a Circular Cylinder98
Ex.3.7-2 Steady Flow in an Agitated Tank101
Ex.3.7-3 Pressure Drop for Creeping Flow in a Packed Tube103
Questions for Discussion104
Problems104
Chapter 4 Velocity Distributions with More than One Independent Variable114
4.1 Time-Dependent Flow of Newtonian Fluids114
Ex.4.1-1 Flow near a Wall Suddenly Set in Motion115
Ex.4.1-2 Unsteady Laminar Flow between Two Parallel Plates117
Ex.4.1-3 Unsteady Laminar Flow near an Oscillating Plate120
4.2 Solving Flow Problems Using a Stream Function121
Ex.4.2-1 Creeping Flow around a Sphere122
4.3 Flow of Inviscid Fluids by Use of the Velocity Potential126
Ex.4.3-1 Potential Flow around a Cylinder128
Ex.4.3-2 Flow into a Rectangular Channel130
Ex.4.3-3 Flow near a Corner131
4.4 Flow near Solid Surfaces by Boundary-Layer Theory133
Ex.4.4-1 Laminar Flow along a Flat Plate(Approximate Solution)136
Ex.4.4-2 Laminar Flow along a Flat Plate(Exact Solution)137
Ex.4.4-3 Flow near a Corner139
Questions for Discussion140
Problems141
Chapter 5 Velocity Distributions in Turbulent Flow152
5.1 Comparisons of Laminar and Turbulent Flows154
5.2 Time-Smoothed Equations of Change for Incompressible Fluids156
5.3 The Time-Smoothed Velocity Profile near a Wall159
5.4 Empirical Expressions for the Turbulent Momentum Flux162
Ex.5.4-1 Development of the Reynolds Stress Expression in the Vicinity of the Wall164
5.5 Turbulent Flow in Ducts165
Ex.5.5-1 Estimation of the Average Velocity in a Circular Tube166
Ex.5.5-2 Application of Prandtl's Mixing Length Formula to Turbulent Flow in a Circular Tube167
Ex.5.5-3 Relative Magnitude of Viscosity and Eddy Viscosity167
5.6 Turbulent Flow in Jets168
Ex.5.6-1 Time-Smoothed Velocity Distribution in a Circular Wall Jet168
Questions for Discussion172
Problems172
Chapter 6 Interphase Transport in Isothermal Systems177
6.1 Definition of Friction Factors178
6.2 Friction Factors for Flow in Tubes179
Ex.6.2-1 Pressure Drop Required for a Given Flow Rate183
Ex.6.2-2 Flow Rate for a Given Pressure Drop183
6.3 Friction Factors for Flow around Spheres185
Ex.6.3-1 Determination of the Diameter of a Falling Sphere187
6.4 Friction Factors for Packed Columns188
Questions for Discussion192
Problems193
Chapter 7 Macroscopic Balances for Isothermal Flow Systems197
7.1 The Macroscopic Mass Balance198
Ex.7.1-1 Draining of a Spherical Tank199
7.2 The Macroscopic Momentum Balance200
Ex.7.2-1 Force Exerted by a 1et (Part a)201
7.3 The Macroscopic Angular Momentum Balance202
Ex.7.3-1 Torque on a Mixing Vessel202
7.4 The Macroscopic Mechanical Energy Balance203
Ex.7.4-1 Force Exerted by a Jet(Part b)205
7.5 Estimation of the Viscous Loss205
Ex.7.5-1 Power Requirement for Pipeline Flow207
7.6 Use of the Macroscopic Balances for Steady-State Problems209
Ex.7.6-1 Pressure Rise and Friction Loss in a Sudden Enlargement209
Ex.7.6-2 Performance of a Liquid-Liquid Ejector210
Ex.7.6-3 Thrust on a Pipe Bend212
Ex.7.6-4 The Impinging Jet214
Ex.7.6-5 Isothermal Flow of a Liquid through an Orifice215
7.7 Use of the Macroscopic Balances for Unsteady-State Problems216
Ex.7.7.1 Acceleration Effects in Unsteady Flow from a Cylindrical Tank217
Ex.7.7-2 Manometer Oscillations219
7.8 Derivation of the Macroscopic Mechanical Energy Balance221
Questions for Discussion223
Problems224
Chapter 8 Polymeric Liquids231
8.1 Examples of the Behavior of Polymeric Liquids232
8.2 Rheometry and Material Functions236
8.3 Non-Newtonian Viscosity and the Generalized Newtonian Models240
Ex.8.3-1 Laminar Flow of an Incompressible Power-Law Fluid in a Circular Tube242
Ex.8.3-2 Flow of a Power-Law Fluid in a Narrow Slit243
Ex.8.3-3 Tangential Annular Flow of a Power-Law Fluid244
8.4 Elasticity and the Linear Viscoelastic Models244
Ex.8.4-1 Small-Amplitude Oscillatory Motion247
Ex.8.4-2 Unsteady Viscoelastic Flow near an Oscillating Plate248
8.5 The Corotational Derivatives and the Nonlinear Viscoelastic Models249
Ex.8.5-1 Material Functions for the Oldroyd 6-Constant Model251
8.6 Molecular Theories for Polymeric Liquids253
Ex.8.6-1 Material Functions for the FENE-P Model255
Questions for Discussion258
Problems258
Part Ⅱ Energy Transport263
Chapter 9 Thermal Conductivity and the Mechanisms of Energy Transport263
9.1 Fouriers Law of Heat Conduction(Molecular Energy Transport)266
Ex.9.1-1 Measurement of Thermal Conductivity270
9.2 Temperature and Pressure Dependence of Thermal Conductivity272
Ex.9.2-1 Effect of Pressure on Thermal Conductivity273
9.3Theory of Thermal Conductivity of Gases at Low Density274
Ex.9.3-1 Computation of the Thermal Conductivity of a Monatomic Gas at Low Density277
Ex.9.3-2 Estimation of the Thermal Conductivity of a Polyatomic Gas at Low Density278
Ex.9.3-3 Prediction of the Thermal Conductivity of a Gas Mixture at Low Density278
9.4 Theory of Thermal Conductivity of Liquids279
Ex.9.4-1 Prediction of the Thermal Conductivity of a Liquid280
9.5 Thermal Conductivity of Solids280
9.6 Effective Thermal Conductivity of Composite Solids281
9.7 Convective Transport of Energy283
9.8 Work Associated with Molecular Motions284
Questions for Discussion286
Problems287
Chapter 10 Shell Energy Balances and Temperature Distributions in Solids and Laminar Flow290
10.1 Shell Energy Balances;Boundary Conditions291
10.2 Heat Conduction with an Electrical Heat Source292
Ex.10.2-1 Voltage Required for a Given Temperature Rise in a Wire Heated by an Electric Current295
Ex.10.2-2 Heated Wire with Specified Heat Transfer Coefficient and Ambient Air Temperature295
10.3 Heat Conduction with a Nuclear Heat Source296
10.4 Heat Conduction with a Viscous Heat Source298
10.5 Heat Conduction with a Chemical Heat Source300
10.6 Heat Conduction through Composite Walls303
Ex.10.6-1 Composite Cylindrical Walls305
10.7 Heat Conduction in a Cooling Fin307
Ex.10.7-1 Error in Thermocouple Measurement309
10.8 Forced Convection310
10.9 Free Convection316
Questions for Discussion319
Problems320
Chapter 11 The Equations of Change for Nonisothermal Systems333
11.1 The Energy Equation333
11.2 Special Forms of the Energy Equation336
11.3 The Boussinesq Equation of Motion for Forced and Free Convection338
11.4 Use of the Equations of Change to Solve Steady-State Problems339
Ex.11.4-1 Steady-State Forced-Convection Heat Transfer in Laminar Flow in a Circular Tube342
Ex.11.4-2 Tangential Flow in an Annulus with Viscous Heat Generation342
Ex.11.4-3 Steady Flow in a Nonisothermal Film343
Ex.11.4-4 Transpiration Cooling344
Ex.11.4-5 Free Convection Heat Transfer from a Vertical Plate346
Ex.11.4-6 Adiabatic Frictionless Processes in an Ideal Gas349
Ex.11.4-7 One-Dimensional Compressible Flow:Velocity,Temperature,and Pressure Profiles in a Stationary Shock Wave350
11.5 Dimensional Analysis of the Equations of Change for Nonisothermal Systems353
Ex.11.5-1 Temperature Distribution about a Long Cylinder356
Ex.11.5-2 Free Convection in a Horizontal Fluid Layer;Formation of Bénard Cells358
Ex.11.5-3 Surface Temperature of an Electrical Heating Coil360
Questions for Discussion361
Problems361
Chapter 12 Temperature Distributions with More than One Independent Variable374
12.1 Unsteady Heat Conduction in Solids374
Ex.12.1-1 Heatingofa Semi-Infinite Slab375
Ex.12.1-2 Heatingofa Finite Slab376
Ex.12.1-3 Unsteady Heat Conduction near a Wall with Sinusoidal Heat Flux379
Ex.12.1-4 Coolingofa Sphere in Contact with a Well-Stirred Fluid379
12.2Steady Heat Conduction in Laminar,Incompressible Flow381
Ex.12.2-1 Laminar Tube Flow with Constant Heat Flux at the Wall383
Ex.12.2-2 Laminar Tube Flow with Constant Heat Flux at the Wall:Asymptotic Solution for the Entrance Region384
12.3Steady Potential Flow of Heat in Solids385
Ex.12.3-1 Temperature Distribution in a Wall386
12.4Boundary Layer Theory for Nonisothermal Flow387
Ex.12.4-1 Heat Transfer in Laminar Forced Convection along a Heated Flat Plate(the von Kármán Integral Method)388
Ex.12.4-2 Heat Transfer in Laminar Forced Convection along a Heated Flat Plate(Asymptotic Solution for Large Prandtl Numbers)391
Ex.12.4-3 Foreed Convection in Steady Three-Dimensional Flow at High Prandtl Numbers392
Questions for Discussion394
Problems395
Chapter 13 Temperature Distributions in Turbulent Flow407
13.1 Time-Smoothed Equations of Change for Incompressible Nonisothermal Flow407
13.2 The Time-Smoothed Temperature Profile near a Wall409
13.3 Empirical Expressions for the Turbulent Heat Flux410
Ex.13.3-1 An Approximate Relation for the Wall Heat Flux for Turbulent Flow in a Tube411
13.4 Temperature Distribution for Turbulent Flow in Tubes411
13.5 Temperature Distribution for Turbulent Flow in Jets415
13.6 Fourier Analysis of Energy Transport in Tube Flow at Large Prandtl Numbers416
Questions for Discussion421
Problems421
Chapter 14 Interphase Transport in Nonisothermal Systems422
14.1 Definitions of Heat Transfer Coefficients423
Ex.14.1-1 Calculation of Heat Transfer Coefficients from Experimental Data426
14.2 Analytical Calculations of Heat Transfer Coefficients for Forced Convection through Tubes and Slits428
14.3 Heat Transfer Coefficients for Forced Convection in Tubes433
Ex.14.3-1 Design of a Tubular Heater437
14.4 Heat Transfer Coefficients for Forced Convection around Submerged Objects438
14.5 Heat Transfer Coefficients for Forced Convection through Packed Beds441
14.6 Heat Transfer Coefficients for Free and Mixed Convection442
Ex14.6-1 Heat Loss bu Free Convection from a Horizontal Pipe445
14.7 Heat Transfer Coefficients for Condensation of Pure Vapors on Solid Surfaces446
Ex.14.7-1 Condensation of Steam on a Vertical Surface449
Questions for Discussion449
Problems450
Chapter 15 Macroscopic Balances for Nonisothermal Systems454
15.1 The Macroscopic Energy Balance455
15.2 The Macroscopic Mechanical Energy Balance456
15.3 Use of the Macroscopic Balances to Solve Steady-State Problems with Flat Velocity Profiles458
Ex.15.3-1 The Cooling of an Ideal Gas459
Ex.15.3-2 Mixing of Tuo Ideal Gas Streams460
15.4 The d-Forms of the Macroscopic Balances461
Ex.15.4-1 Parallel-or Counter-Flow Heat Exchangers462
Ex.15.4-2 Power Requirement for Pumping a Compressible Fluid through a Long Pipe464
15.5 Use of the Macroscopic Balances to Solve Unsteady-State Problems and Problems with Nonflat Velocity Profiles465
Ex.15.5-1 Heating ofa Liquid in an Agitated Tank466
Ex.15.5-2 Operation ofa Simple Temperature Controller468
Ex.15.5-3 Flow of Compressible Fluids through Heat Meters471
Ex.15.5-4 Free Batch Expansion of a Compressible Fluid472
Questions for Discussion474
Problems474
Chapter 16 Energy Transport by Radiation487
16.1 The Spectrum of Electromagnetic Radiation488
16.2 Absorption and Emission at Solid Surfaces490
16.3 Planck's Distribution Law,Wien's Displacement Law,and the Stefan-Boltzmann Law493
Ex.16.3-1 Temperature and Radiation-Energy Emission of the Sun496
16.4 Direct Radiation between Black Bodies in Vacuo at Different Temperatures497
Ex.16.4-1 Estimation of the Solar Constant501
Ex.16.4-2 Radiant Heat Transfer between Disks501
16.5 Radiation between Nonblack Bodies at Different Temperatures502
Ex.16.5-1 Radiation Shields503
Ex.16.5-2 Radiation and Free-Convection Heat Losses from a Horizontal Pipe504
Ex.16.5-3 Combined Radiation and Convection505
16.6 Radiant Energy Transport in Absorbing Media506
Ex.16.6-1 Absorption ofa Monochromatic Radiant Beam507
Questions for Discussion508
Problems508
Part Ⅲ Mass Transport513
Chapter 17 Diffusivity and the Mechanisms of Mass Transport513
17.1 Fick's Law of Binary Diffusion(Molecular Mass Transport)514
Ex.17.1-1 Diffusion ofHelium through Pyrex Glass519
Ex.17.1-2 The Equivalence of DAB and DBA520
17.2 Temperature and Pressure Dependence of Diffusivities521
Ex.17.2-1 Estimation of Diffusivity at Low Density523
Ex.17.2-2 Estimation of Self-Diffusivity at High Density523
Ex.17.2-3 Estimation of Binary Diffusivity at High Density524
17.3 Theory of Diffusion in Gases at Low Density525
Ex.17.3-1 Computation of Mass Diffusivity for Low-Density Monatomic Gases528
17.4 Theory of Diffusion in Binary Liquids528
Ex.17.4-1 Estimation of Liquid Diffusivity530
17.5 Theory of Diffusion in Colloidal Suspensions531
17.6 Theory of Diffusion in Polymers532
17.7 Mass and Molar Transport by Convection533
17.8 Summary of Mass and Molar Fluxes536
17.9 The Maxwell-Stefan Equations for Multicomponent Diffusion in Gases at Low Density538
Questions for Discussion538
Problems539
Chapter 18 Concentration Distributions in Solids and Laminar Flow543
18.1 Shell Mass Balances;Boundary Conditions545
18.2 Diffusion through a Stagnant Gas Film545
Ex.18.2-1 Diffusion with a Moving Interface549
Ex.18.2-2 Determination of Diffusivity549
Ex.18.2-3 Diffusion through a Nonisothermal Spherical Film550
18.3 Diffusion with a Heterogeneous Chemical Reaction551
Ex.18.3-1 Diffusion with a Slow Heterogeneous Reaction553
18.4 Diffusion with a Homogeneous Chemical Reaction554
Ex.18.4-1 Gas Absorption with Chemical Reaction in an Agitated Tank555
18.5 Diffusion into a Falling Liquid Film(Gas Absorption)558
Ex.18.5-1 Gas Absorption from Rising Bubbles560
18.6 Diffusion into a Falling Liquid Film(Solid Dissolution)562
18.7 Diffusion and Chemical Reaction inside a Porous Catalyst563
18.8 Diffusion in a Three-Component Gas System567
Questions for Discussion568
Problems568
Chapter 19 Equations of Change for Multicomponent Systems582
19.1 The Equations of Continuity for a Multicomponent Mixture582
Ex.19.1-1 Diffusion,Convection,and Chemical Reaction585
19.2 Summary of the Multicomponent Equations of Change586
19.3 Summary of the Multicomponent Fluxes590
Ex.19.3-1 The Partial Molar Enthalpy591
19.4 Use of the Equations of Change for Mixtures592
Ex.19.4-1 Simultaneous Heat and Mass Transport592
Ex.19.4-2 Concentration Profile in a Tubular Reactor595
Ex.19.4-3 Catalytic Oxidation of Carbon Monoxide596
Ex.19.4-4 Thermal Conductivity of a Polyatomic Gas598
19.5 Dimensional Analysis of the Equations of Change for Nonreacting Binary Mixtures599
Ex.19.5-1 Concentration Distribution about a Long Cylinder601
Ex.19.5-2 Fog Formation during Dehumidification602
Ex.19.5-3 Blending of Miscible Fluids604
Questions for Discussion605
Problems606
Chapter 20 Concentration Distributions with More than One Independent Variable612
20.1 Time-Dependent Diffusion613
Ex.20.1-1 Unsteady-State Evaporation of a Liquid(the“Arnold Problem”)613
Ex.20.1-2 Gas Absorption with Rapid Reaction617
Ex.20.1-3 Unsteady Diffusion with First-Order Homogeneous Reaction619
Ex.20.1-4 Influence of Changing Interfacial Area on Mass Transferat an Interface621
20.2 Steady-State Transport in Binary Boundary Layers623
Ex.20.2-1 Diffusion and Chemical Reaction in Isothermal Laminar Flow along a Soluble Flat Plate625
Ex.20.2-2 Forced Convection from a Flat Plate at High Mass-Transfer Rates627
Ex.20.2-3 Approximate Analogies for the Flat Plate at Low Mass-Transfer Rates632
20.3 Steady-State Boundary-Layer Theory for Flow around Objects633
Ex.20.3-1 Mass Transfer for Creeping Flow around a Gas Bubble636
20.4 Boundary Layer Mass Transport with Complex Interfacial Motion637
Ex.20.4-1 Mass Transfer with Nonuniform Interfacial Deformation641
Ex.20.4-2 Gas Absorption with Rapid Reaction and Interfacial Deformation642
20.5 “Taylor Dispersion”in Laminar Tube Flow643
Questions for Discussion647
Problems648
Chapter 21 Concentration Distributions in Turbulent Flow657
21.1 Concentration Fluctuations and the Time-Smoothed Concentration657
21.2 Time-Smoothing of the Equation of Continuity of A658
21.3 Semi-Empirical Expressions for the Turbulent Mass Flux659
21.4 Enhancement of Mass Transfer by a First-Order Reaction in Turbulent Flow659
21.5 Turbulent Mixing and Turbulent Flow with Second-Order Reaction663
Questions for Discussion667
Problems668
Chapter 22 Interphase Transport in Nonisothermal Mixtures671
22.1 Definition of Transfer Coefficients in One Phase672
22.2 Analytical Expressions for Mass Transfer Coefficients676
22.3 Correlation of Binary Transfer Coefficients in One Phase679
Ex.22.3-1 Evaporation from a Freely Falling Drop682
Ex.22.3-2 The Wet and Dry Bulb Psychrometer683
Ex.22.3-3 Mass Transfer in Creeping Flow through Packed Beds685
Ex.22.3-4 Mass Transfer to Drops and Bubbles687
22.4 Definition of Transfer Coefficients in Two Phases687
Ex.22.4-1 Determination of the Controlling Resistance690
Ex.22.4-2 Interaction of Phase Resistances691
Ex.22.4-3 Area Averaging693
22.5 Mass Transfer and Chemical Reactions694
Ex.22.5-1 Estimation of the Interfacial Area in a Packed Column694
Ex.22.5-2 Estimation of Volumetric Mass Transfer Coefficients695
Ex.22.5-3 Model-Insensitive Correlations for Absorption with Rapid Reaction696
22.6 Combined Heat and Mass Transfer by Free Convection698
Ex.22.6-1 Additivity of Grashof Numbers698
Ex.22.6-2 Free-Convection Heat Transfer as a Source of Forced-Convection Mass Transfer698
22.7 Effects of Interfacial Forces on Heat and Mass Transfer699
Ex.22.7-1 Elimination of Circulation in a Rising Gas Bubble701
Ex.22.7-2 Marangoni Instability in a Falling Film702
22.8 Transfer Coefficients at High Net Mass Transfer Rates703
Ex.22.8-1 Rapid Evaporation of a Liquid from a Plane Surface710
Ex.22.8-2 Correction Factors in Droplet Evaporation711
Ex.22.8-3 Wet-Bulb Performance Corrected for Mass-Transfer Rate711
Ex.22.8-4 Comparison of Film and Penetration Models for Unsteady Evaporation in a Long Tube712
Ex.22.8-5 Concentration Polarization in Ultrafiltration713
22.9 Matrix Approximations for Multicomponent Mass Transport716
Questions for Discussion721
Problems722
Chapter 23 Macroscopic Balances for Multicomponent Systems726
23.1 The Macroscopic Mass Balances727
Ex.23.1-1 Disposal of an Unstable Waste Product728
Ex.23.1-2 Binary Splitters730
Ex.23.1-3 The Macroscopic Balances and Dirac's Separative Capacity”and“Value Function”731
Ex.23.1-4 Compartmental Analysis733
Ex.23.1-5 Time Constants and Model Insensitivity736
23.2 The Macroscopic Momentum and Angular Momentum Balances738
23.3 The Macroscopic Energy Balance738
23.4 The Macroscopic Mechanical Energy Balance739
23.5 Use of the Macroscopic Balances to Solve Steady-State Problems739
Ex.23.5-1 Energy Balances for a Sulfur Dioxide Converter739
Ex.23.5-2 Heighht of a Packed-Tower Absorber742
Ex.23.5-3 Linear Cascades746
Ex.23.5-4 Expansion ofa Reactive Gas Mixture through a Frictionless Adiabatic Nozzle749
23.6 Use of the Macroscopic Balances to Solve Unsteady-State Problems752
Ex.23.6-1 Start-Up of a Chemical Reactor752
Ex.23.6-2 Unsteady Operation of a Packed Column753
Ex.23.6-3 The Utility of Low-Order Moments756
Questions for Discussion758
Problems759
Chapter 24 Other Mechanisms for Mass Transport764
24.1 The Equation of Change for Entropy765
24.2 The Flux Expressions for Heat and Mass767
Ex.24.2-1 Thermal Diffusion and the Clusius-Dickel Column770
Ex.24.2-2 Pressure Diffusion and the Ultra-centrifuge772
24.3 Concentration Diffusion and Driving Forces774
24.4 Applications of the Generalized Maxwell-Stefan Equations775
Ex.24.4-1 Centrifugation of Proteins776
Ex.24.4-2 Proteins as Hydrodynamic Particles779
Ex.24.4-3 Diffusion of Salts in an Aqueous Solution780
Ex.24.4-4 Departures from Local Electroneutrality:Electro-Osmosis782
Ex.24.4-5 Additional Mass-Transfer Driving Forces784
24.5 Mass Transport across Selectively Permeable Membranes785
Ex.24.5-1 Concentration Diffusion between Preexisting Bulk Phases788
Ex.24.5-2 Ultrafiltration and Reverse Osmosis789
Ex.24.5-3 Charged Membranes and Donnan Exclusion791
24.6 Mass Transport in Porous Media793
Ex.24.6-1 Knudsen Diffusion795
Ex.24.6-2 Transport from a Binary External Solution797
Questions for Discussion798
Problems799
Postface805
Appendices807
Appendix A Vector and Tensor Notation807
A.1 Vector Operations from a Geometrical Viewpoint808
A.2 Vector Operations in Terms of Components810
Ex.A.2-1 Proof of a Vector Identity814
A.3 Tensor Operations in Terms of Components815
A.4 Vector and Tensor Differential Operations819
Ex.A.4-1 Proof of a Tensor Identity822
A.5 Vector and Tensor Integral Theorems824
A.6 Vector and Tensor Algebra in Curvilinear Coordinates825
A.7 Differential Operations in Curvilinear Coordinates829
Ex.A.7-1 Differential Operations in Cylindrical Coordinates831
Ex.A.7-2 Differential Operations in Spherical Coordinates838
A.8 Integral Operations in Curvilinear Coordinates839
A.9 Further Comments on Vector-Tensor Notation841
Appendix B Fluxes and the Equations of Change843
B.1 Newton's Law of Viscosity843
B.2 Fourier's Law of Heat Conduction845
B.3 Fick's(First)Law of Binary Diffusion846
B.4 The Equation of Continuity846
B.5 The Equation of Motion in Terms of ?847
B.6 The Equation of Motion for a Newtonian Fluid with Constantρandμ848
B.7 The Dissipation Functionφv for Newtonian Fluids849
B.8 The Equation of Energy in Terms of q849
B.9 The Equation of Energy for Pure Newtonian Fluids with Constantρand k850
B.10 The Equation of Continuity for Speciesαin Terms of jα850
B.11 The Equation of Continuity for Species A in Terms of ωA for ConstantρDAB851
Appendix C Mathematical Topics852
C.1 Some Ordinary Differential Equations and Their Solutions852
C.2 Expansions of Functions in Taylor Series853
C.3 Differentiation of Integrals(the Leibniz Formula)854
C.4 The Gamma Function855
C.5 The Hyperbolic Functions856
C.6 The Error Function857
Appendix D The Kinetic Theory of Gases858
D.1 The Boltzmann Equation858
D.2 The Equations of Change859
D.3 The Molecular Expressions for the Fluxes859
D.4 The Solution to the Boltzmann Equation860
D.5 The Fluxes in Terms of the Transport Properties860
D.6 The Transport Properties in Terms of the Intermolecular Forces861
D.7 Concluding Comments861
Appendix E Tables for Prediction of Transport Properties863
E.1 Intermolecular Force Parameters and Critical Properties864
E.2 Functions for Prediction of Transport Properties of Gases at Low Densities866
Appendix F Constants and Conversion Factors867
F.1 Mathematical Constants867
F.2 Physical Constants867
F.3 Conversion Factors868
Notation872
Author Index877
Subject Index885