Mass Transfer From Fundamentals to Modern Industrial Applications

Book Details

Author

Language

Pages

Size

Format

Mass Transfer From Fundamentals to Modern Industrial Applications

PDF Free Download | Mass Transfer From Fundamentals to Modern Industrial Applications by Koichi Asano

Contents of Mass Transfer eBook

  • Introduction
  • The Beginnings of Mass Transfer
  • Characteristics of Mass Transfer
  • Three Fundamental Laws of Transport Phenomena
  • Newton’s Law of Viscosity
  • Fourier’s Law of Heat Conduction
  • Fick’s Law of Diffusion
  • Summary of Phase Equilibria in Gas-Liquid Systems
  • References
  • Diffusion and Mass Transfer
  • Motion of Molecules and Diffusion
  • Diffusion Phenomena
  • Definition of Diffusional Flux and Reference Velocity of Diffusion
  • Binary Diffusion Flux
  • Diffusion Coefficients
  • Binary Diffusion Coefficients in the Gas Phase
  • Multicomponent Diffusion Coefficients in the Gas Phase
  • Example
  • Solution
  • Rates of Mass Transfer
  • Definition of Mass Flux
  • Unidirectional Diffusion in Binary Mass Transfer
  • Equimolal Counterdiffusion
  • Convective Mass Flux for Mass Transfer in a Mixture of Vapors
  • Mass Transfer From Fundamentals to Modern Industrial Applications Koichi Asano
  • Overall Mass Transfer Coefficients
  • References
  • Governing Equations of Mass Transfer
  • Laminar and Turbulent Flow
  • Continuity Equation and Diffusion Equation
  • Continuity Equation
  • Diffusion Equation in Terms of Mass Fraction
  • Diffusion Equation in Terms of Mole Fraction
  • Equation of Motion and Energy Equation
  • The Equation of Motion (Navier–Stokes Equation)
  • The Energy Equation
  • Governing Equations in Cylindrical and Spherical Coordinates
  • Some Approximate Solutions of the Diffusion Equation
  • Film Model
  • Penetration Model
  • Surface Renewal Model
  • Physical Interpretation of Some Important Dimensionless Numbers
  • Reynolds Number
  • Prandtl Number and Schmidt Number
  • Nusselt Number
  • Sherwood Number
  • Dimensionless Numbers Commonly Used in Heat and Mass
  • Dimensional Analysis
  • Principle of Similitude and Dimensional Homogeneity
  • Finding Dimensionless Numbers and Pi Theorem
  • References
  • Mass Transfer in a Laminar Boundary Layer
  • Velocity Boundary Layer
  • Boundary Layer Equation
  • Similarity Transformation
  • Integral Form of the Boundary Layer Equation
  • Friction Factor
  • Temperature and Concentration Boundary Layers
  • Temperature and Concentration Boundary Layer Equations
  • Integral Form of Thermal and Concentration Boundary Layer
  • Equations
  • Numerical Solutions of the Boundary Layer Equations
  • Quasi-Linearization Method
  • Correlation of Heat and Mass Transfer Rates
  • Example
  • Solution
  • Mass and Heat Transfer in Extreme Cases
  • Approximate Solutions for Mass Transfer in the Case of Extremely Large
  • Schmidt Numbers
  • Approximate Solutions for Heat Transfer in the Case of Extremely Small
  • Prandtl Numbers
  • Effect of an Inactive Entrance Region on Rates of Mass Transfer
  • Polynomial Approximation of Velocity Profiles and Thickness of the Velocity Boundary Layer
  • Polynomial Approximation of Concentration Profiles and Thickness of the Concentration Boundary Layer
  • Absorption of Gases by a Falling Liquid Film
  • Velocity Distribution in a Falling Thin Liquid Film According
  • to Nusselt
  • Gas Absorption for Short Contact Times
  • Gas Absorption for Long Exposure Times
  • Example
  • Solution
  • Dissolution of a Solid Wall by a Falling Liquid Film
  • High Mass Flux Effect in Heat and Mass Transfer in Laminar Boundary
  • Layers
  • High Mass Flux Effect
  • Mickley’s Film Model Approach to the High Mass Flux Effect
  • Correlation of High Mass Flux Effect for Heat and Mass Transfer
  • Heat and Mass Transfer in a Laminar Flow inside a Circular Pipe
  • Velocity Distribution in a Laminar Flow inside a Circular Pipe
  • Graetz Numbers for Heat and Mass Transfer
  • Energy Balance over a Small Volume Element of a Pipe
  • Material Balance over a Small Volume Element of a Pipe
  • Heat and Mass Transfer near the Entrance Region of a Circular Pipe
  • Heat Transfer near the Entrance Region at Constant
  • Wall Temperature
  • Mass Transfer near the Entrance Region at Constant Wall
  • Concentration
  • Heat and Mass Transfer in a Fully Developed Laminar Flow inside a Circular Pipe
  • Heat Transfer at Constant Wall Temperature
  • Mass Transfer at Constant Wall Concentration
  • Mass Transfer in Wetted-Wall Columns
  • Motion, Heat and Mass Transfer of Particles
  • Creeping Flow around a Spherical Particle
  • Motion of Spherical Particles in a Fluid
  • Numerical Solution of the Drag Coefficients of a Spherical Particle in the Intermediate Reynolds Number Range
  • Correlation of the Drag Coefficients of a Spherical Particle
  • Terminal Velocity of a Particle
  • Heat and Mass Transfer of Spherical Particles in a Stationary Fluid
  • Heat and Mass Transfer of Spherical Particles in a Flow Field
  • Numerical Approach to Mass Transfer of a Spherical Particle in a Laminar Flow
  • The Ranz–Marshall Correlation and Comparison with Numerical Data
  • Liquid-Phase Mass Transfer of a Spherical Particle in Stokes’ Flow
  • Drag Coefficients, Heat and Mass Transfer of a Spheroidal Particle
  • Heat and Mass Transfer in a Fluidized Bed Void Function
  • Interaction of Two Spherical Particles of the Same Size in a Coaxial
  • Mass Transfer of Drops and Bubbles
  • Shapes of Bubbles and Drops
  • Drag Force of a Bubble or Drop in a Creeping Flow (Hadamard’s Flow)
  • Hadamard’s Stream Function
  • Drag Coefficients and Terminal Velocities of Small Drops and Bubbles
  • Motion of Small Bubbles in Liquids Containing Traces of Contaminants
  • Flow around an Evaporating Drop
  • Effect of Mass Injection or Suction on the Flow around a Spherical Particle
  • Effect of Mass Injection or Suction on Heat and Mass Transfer of a
  • Spherical Particle
  • Evaporation of Fuel Sprays
  • Drag Coefficients, Heat and Mass Transfer of an Evaporating Drop
  • Behavior of an Evaporating Drop Falling Freely in the Gas Phase
  • Absorption of Gases by Liquid Sprays
  • Mass Transfer of Small Bubbles or Droplets in Liquids
  • Continuous-Phase Mass Transfer of Bubbles and Droplets in Hadamard Flow
  • Dispersed-Phase Mass Transfer of Drops in Hadamard Flow
  • Mass Transfer of Bubbles or Drops of Intermediate Size in the Liquid Phase
  • Turbulent Transport Phenomena
  • Fundamentals of Turbulent Flow
  • Turbulent Flow
  • Reynolds Stress
  • Eddy Heat Flux and Diffusional Flux
  • Eddy Transport Properties
  • Mixing Length Model
  • Velocity Distribution in a Turbulent Flow inside a Circular Pipe and
  • Friction Factors
  • Universal Velocity Distribution Law for Turbulent Flow inside a Circular Pipe
  • Friction Factors for Turbulent Flow inside a Smooth Circular Pipe
  • Analogy between Momentum, Heat, and Mass Transfer
  • Reynolds Analogy
  • Chilton–Colburn Analogy
  • Von Ka’rman Analogy
  • Deissler Analogy
  • Friction Factor, Heat, and Mass Transfer in a Turbulent Boundary Layer
  • Velocity Distribution in a Turbulent Boundary Layer
  • Friction Factor
  • Heat and Mass Transfer in a Turbulent Boundary Layer
  • Turbulent Boundary Layer with Surface Mass Injection or Suction
  • Evaporation and Condensation
  • Characteristics of Simultaneous Heat and Mass Transfer
  • Mass Transfer with Phase Change
  • Surface Temperatures in Simultaneous Heat and Mass Transfer
  • Wet-Bulb Temperatures and Psychrometric Ratios
  • Film Condensation of Pure Vapors
  • Nusselt’s Model for Film Condensation of Pure Vapors
  • Effect of Variable Physical Properties
  • Condensation of Binary Vapor Mixtures
  • Total and Partial Condensation
  • Characteristics of the Total Condensation of Binary Vapor Mixtures
  • Rate of Condensation of Binary Vapors under Total Condensation
  • Condensation of Vapors in the Presence of a Non-Condensable Gas
  • Accumulation of a Non-Condensable Gas near the Interface
  • Calculation of Heat and Mass Transfer
  • Experimental Approach to the Effect of a Non-Condensable Gas
  • Condensation of Vapors on a Circular Cylinder
  • Condensation of Pure Vapors on a Horizontal Cylinder
  • Heat and Mass Transfer in the case of a Cylinder with Surface
  • Mass Injection or Suction
  • Calculation of the Rates of Condensation of Vapors on a Horizontal Tube in the Presence of a Non Condensable Gas
  • Mass Transfer in Distillation
  • Classical Approaches to Distillation and their Paradox
  • Tray Towers and Packed Columns
  • Tray Efficiencies in Distillation Columns
  • HTU as a Measure of Mass Transfer in Packed Distillation Columns
  • Paradox in Tray Efficiency and HTU
  • Characteristics of Heat and Mass Transfer in Distillation
  • Physical Picture of Heat and Mass Transfer in Distillation
  • Rate-Controlling Process in Distillation
  • Effect of Partial Condensation of Vapors on the Rates of Mass Transfer in Binary Distillation
  • Dissimilarity of Mass Transfer in Gas Absorption and Distillation
  • Simultaneous Heat and Mass Transfer Model for Packed Distillation Columns
  • Wetted Area of Packings
  • Apparent End Effect
  • Correlation of the Vapor-Phase Diffusional Fluxes in Binary Distillation
  • Correlation of Vapor-Phase Diffusional Fluxes in Ternary Distillation
  • Simulation of Separation Performance in Ternary Distillation on a Packed
  • Column under Total Reflux Conditions
  • Calculation of Ternary Distillations on Packed Columns under Finite Reflux Ratio
  • Material Balance for the Column
  • Convergence of Terminal Composition
  • Cryogenic Distillation of Air on Packed Columns
  • Air Separation Plant
  • Mass and Diffusional Fluxes in Cryogenic Distillation
  • Simulation of Separation Performance of a Pilot-Plant-Scale Air
  • Separation Plant
  • Industrial Separation of Oxygen- by Super Cryogenic Distillation
  • Oxygen- as Raw Material for PET Diagnostics
  • A New Process for Direct Separation of Oxygen- from Natural Oxygen
  • Construction and Operation of the Plant

Related Books

What's the problem with this file?

There is a temporary issue with downloading files and we are working on.
In the meantime, we appreciate your patience.