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Introduction to engineering heat transfer / G.F. Nellis, S.A. Klein.

Van Pelt Library TJ260 .N453 2021
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Format:
Book
Author/Creator:
Nellis, Gregory, author.
Klein, Sanford A., 1950- author.
Language:
English
Subjects (All):
Heat--Transmission.
Heat.
Physical Description:
xxiv, 1001 pages : illustrations (some color) ; 26 cm
Other Title:
Engineering heat transfer
Place of Publication:
Cambridge, United Kingdom ; New York, NY : Cambridge University Press, 2021.
Summary:
"This new text integrates fundamental theory with modern computational tools such as EES, MATLAB, and FEHT to equip students with the essential tools for designing and optimizing real-world systems and the skills needed to become effective practicing engineers"-- Provided by publisher.
Contents:
Machine generated contents note: 1. Introduction
1.1. Relevance of Heat Transfer
1.2. Relationship to Thermodynamics
1.3. Problem Solving Methodology
1.4. Heat Transfer Mechanisms
1.4.1. Conduction
1.4.2. Convection
1.4.3. Radiation
1.5. Thermophysical Properties
1.5.1. Real Fluids
1.5.2. Ideal Gas Model
1.5.3. Incompressible Substance Model
1.6. Conclusions and Learning Objectives
Reference
Problems
Projects
2. One-Dimensional, Steady-State Conduction
2.1. Conduction Heat Transfer
2.1.1. Fourier's Law
2.1.2. Thermal Conductivity
2.2. Steady-State 1-D Conduction without Generation
2.2.1. Introduction
2.2.2. The Plane Wall
Define a Differential Control Volume
Carry out an Energy Balance on the Control Volume
Take the Limit as dx[→]0
Substitute Rate Equations into the Differential Equation
Define Boundary Conditions
2.2.3. The Resistance Concept
2.2.4. Radial Conduction
Radial Conduction in a Cylinder
Radial Conduction in a Sphere
2.2.5. Other Resistance Formulae
Convection Resistance
Contact Resistance
Radiation Resistance
2.3. Steady-State 1-D Conduction with Generation
2.3.1. Introduction
2.3.2. Uniform Thermal Energy Generation in a Plane Wall
2.3.3. Uniform Thermal Energy Generation in Radial Geometries
Cylindrical Geometry
Spherical Geometry
2.3.4. Spatially Nonuniform Generation
2.4. Numerical Solutions
2.4.1. Introduction
2.4.2. Developing the Finite Difference Equations
2.4.3. Solving the Equations with EES
2.4.4. Solving the Equations with Matrix Decomposition
2.4.5. Solving the Equations with Gauss
Seidel Iteration
2.4.6. Temperature-Dependent Properties
Implementation in EES
Implementation using Matrix Decomposition
Implementation using Gauss
2.5. Conclusions and Learning Objectives
References
Conduction without Generation: Concepts and Analytical Solutions
Thermal Resistance Problems
Conduction with Generation: Concepts and Analytical Solutions
Numerical Solution Concepts
Numerical Solutions
3. Extended Surface Problems
3.1. Extended Surfaces
3.1.1. The Extended Surface Approximation
3.1.2. The Biot Number
3.2. Analytical Solutions to Extended Surface Problems
3.2.1. Deriving the ODE and Boundary Conditions
3.2.2. Solving the ODE
3.2.3. Applying the Boundary Conditions
3.2.4. Hyperbolic Trigonometric Functions
3.2.5. Solutions to Linear Homogeneous ODEs
3.3. Fins
3.3.1. Fin Efficiency
3.3.2. Convection from the Fin Tip
3.3.3. Fin Resistance
3.3.4. Finned Surfaces
3.4. Numerical Solutions to Extended Surface Problems
3.5. Conclusions and Learning Objectives
The Extended Surface Approximation and the Biot Number
Analytical Solutions to Extended Surface Problems
Fins and Finned Surfaces
Numerical Solutions to Extended Surface Problems
4. Two-Oimensional, Steady-State Conduction
4.1. The Governing Differential Equation and Boundary Conditions
4.2. Shape Factors
4.2.1. Definition of Shape Factor
4.2.2. Shape Factor Resistance
4.2.3. The Meaning of a Shape Factor
4.3. Finite Difference Solution
4.3.1. Introduction
4.3.2. Developing the Finite Difference Equations
4.3.3. Solving the Equations with EES
4.3.4. Solving the Equations with Matrix Decomposition
4.3.5. Solving the Equations with Gauss-Seidel Iteration
4.4. Finite Element Solution
4.4.1. Introduction
4.4.2. Specifying the Problem
4.4.3. Specifying the Mesh and Solving
4.4.4. Examination of the Solution
Mesh Convergence
Engineering Judgment
4.5. Conclusions and Learning Objectives
The Governing Differential Equation and Boundary Conditions
Shape Factors
Finite Difference Solutions
Finite Element Method using FEHT
5. Lumped Transient Problems
5.1. The Lumped Capacitance Assumption
5.1.1. The Biot Number
5.1.2. The Lumped Capacitance Time Constant
5.2. Analytical Solutions
5.2.1. Deriving the Differential Equation
5.2.2. Solving the Differential Equation
Step Change in Ambient Temperature
Ramped Ambient Temperature
5.3. Numerical Solutions
5.3.1. Introduction
5.3.2. The Euler Method
5.3.3. Predictor
Corrector Methods
5.3.4. Implicit Methods
5.3.5. Using ODE Solvers
EES' Integral Command
MATLAB's ODE Solvers
5.4. Conclusions and Learning Objectives
The Lumped Capacitance Approximation and the Biot Number
Analytical Solutions
6. Transient Conduction
6.1. Conceptual Tools
6.1.1. Diffusive Energy Transport
6.1.2. The Diffusive Time Constant
6.1.3. The Semi-Infinite Resistance
6.2. Analytical Solution
6.2.1. The Differential Equation
6.2.2. Semi-Infinite Body Solutions
6.2.3. Bounded Problem Solutions
The Plane Wall
Exact Solution
Approximate Solution
The Cylinder
The Sphere
6.3. 1-D Numerical Solutions
6.3.1. Introduction
6.3.2. The State Equations
6.3.3. The Euler Method
6.3.4. Predictor
6.3.5. Implicit Methods
Implementation with EES
Implementation with Matrix Decomposition
Implementation with Gauss
6.3.6. Using ODE Solvers
MATLAB's ODE Solver
6.4. 2-D Numerical Solutions
6.4.1. Introduction
6.4.2. The Finite Difference Solution
Deriving the State Equations
Integrating through Time
6.4.3. The Finite Element Solution
Specifying the Problem
Specifying the Mesh and Solving
6.5. Conclusions and Learning Objectives
Conceptual Tools
The Differential Equation and Boundary Conditions
Semi-Infinite Solutions
Plane Wall, Cylinder, and Sphere Solutions
1-D Transient Numerical Solutions
7. Convection
7.1. The Laminar Boundary Layer
7.1.1. The Velocity Boundary Layer
7.1.2. The Thermal Boundary Layer
7.1.3. A Conceptual Model of Laminar Boundary Layer Growth
7.1.4. The Prandtl Number
7.1.5. A Conceptual Model of Shear Stress and the Heat Transfer Coefficient
7.1.6. The Reynolds Number
7.1.7. The Friction Coefficient and the Nusselt Number
7.1.8. The Reynolds Analogy
7.1.9. Local vs. Average Quantities
The Average Friction Coefficient
The Drag Coefficient
The Average Nusseh Number
7.2. Turbulent Boundary Layer Concepts
7.2.1. Introduction
7.2.2. The Critical Reynolds Number
7.2.3. A Conceptual Model of the Turbulent Boundary Layer
7.3. The Boundary Layer Equations
7.3.1. Introduction
7.3.2. The Governing Equations for Viscous Fluid Flow
The Continuity Equation
The Momentum Equations
The Energy Conservation Equation
7.3.3. The Boundary Layer Simplifications
The x-Momentum Equation
The y-Momentum Equation
7.4. Dimensional Analysis in Convection
7.4.1. Introduction
7.4.2. The Dimensionless Boundary Layer Equations
The Dimensionless Continuity Equation
The Dimensionless Momentum Equation
The Dimensionless Energy Equation
7.4.3. Correlations
The Friction and Drag Coefficients
The Nusselt Number
7.4.4. The Reynolds Analogy (Revisited)
7.5. Conclusions and Learning Objectives
Laminar Boundary Layer Concepts
Turbulent Boundary Layer Concepts
The Boundary Layer Equations and Dimensional Analysis for Convection
8. External Forced Convection
8.1. Methodology for using a Convection Correlation
8.2. Flow over a Flat Plate
8.2.1. The Friction Coefficient
Local Friction Coefficient for a Smooth Plate
Local Friction Coefficient for a Rough Plate
Average Friction Coefficient
8.2.2. The Nusselt Number
Constant Temperature
Unhealed Starting Length
Constant Heat Flux
8.3. Flow across a Cylinder
8.3.1. The Drag Coefficient
8.3.2. The Nusselt Number
8.4. Flow across other Extrusions
8.5. Flow past a Sphere
8.6. Conclusions and Learning Objectives
Flow over a Flat Plate
Flow over Cylinders and other Extrusions
Flow over a Sphere
9. Internal Forced Convection
9.1. Internal Flow Concepts
9.1.1. Velocity and Momentum Considerations
Internal vs. External Flow
The Developing Region vs. the Fully Developed Region
The Mean Velocity, Hydraulic Diameter, and Reynolds Number
The Laminar Hydrodynamic Entry Length
Turbulent Internal Flow
The Pressure Gradient
The Friction Factor
9.1.2. Thermal Considerations
The Mean Temperature and the Heat Transfer Coefficient
The Laminar Thermal Entry Length
9.2. Internal Flow Correlations
9.2.1. Introduction
9.2.2. Flow Classification
9.2.3. The Friction Factor
Laminar Flow
Contents note continued: Turbulent Flow
EES' Internal Flow Convection Library
9.2.4. The Nusselt Number
Turbulent Flow
9.3. The Energy Balance
9.3.1. Introduction
9.3.2. The Energy Balance
9.3.3. Specified Heat Flux
9.3.4. Specified Wall Temperature
Constant Wall Temperature
9.3.5. Specified External Temperature
9.4. Conclusions and Learning Objectives
Internal Flow Concepts
Internal Flow Correlations
The Energy Balance
10. Free Convection
10.1. Free Convection Flow
10.2. Dimensionless Parameters
10.2.1. The Characteristic Buoyancy Velocity
10.2.2. The Volumetric Thermal Expansion Coefficient
The Volumetric Thermal Expansion Coefficient of an Ideal Gas
10.2.3. The Grashof Number and the Rayleigh Number
10.3. External Free Convection Correlations
10.3.1. Introduction
10.3.2. Plate
Heated or Cooled Vertical Plate
Horizontal Plate
Heated Upward Facing or Cooled Downward Facing
Heated Downward Facing or Cooled Upward Facing
Plate at an Arbitrary Angle
10.3.3. Sphere
10.3.4. Cylinder
Horizontal Cylinder
Vertical Cylinder
10.4. Internal Free Convection Correlations
10.4.1. Introduction
10.4.2. Vertical Parallel Plate Channels
10.4.3. Enclosures
10.5. Combined Free and Forced Convection
10.6. Conclusions and Learning Objectives
Free Convection Concepts
Free Convection from Plates, Spheres, and Cylinders
Free Convection in Channels
Free Convection in Enclosures
Combined Free and Forced Convection
11. Boiling and Condensation
11.1. Relevance
11.2. Pool Boiling
11.2.1. Introduction
11.2.2. The Boiling Curve
11.2.3. Pool Boiling Correlations
11.3. Flow Boiling
11.3.1. Introduction
11.3.2. Flow Boiling Correlations
11.4. Film Condensation
11.4.1. Introduction
11.4.2. Correlations for Film Condensation
Vertical Wall
Horizontal, Downward Facing Plate
Horizontal, Upward Facing Plate
Single Horizontal Cylinder
Bank of Horizontal Cylinders
Single Horizontal Finned Tube
11.5. Flow Condensation
11.5.1. Introduction
11.5.2. Flow Condensation Correlations
11.6. Conclusions and Learning Objectives
Pool Boiling
Flow Boiling
Film Condensation
Flow Condensation
12. Heat Exchangers
12.1. Introduction to Heat Exchangers
12.1.1. Applications of Heat Exchangers
12.1.2. Heat Exchanger Classifications and Flow Configurations
12.1.3. Overall Energy Balance
12.1.4. Heat Exchanger Conductance
Fouling Resistance
12.1.5. Flow across Tube Banks
12.1.6. Compact Heat Exchanger Correlations
12.2. The Heat Exchanger Problem
12.2.1. Introduction
12.2.2. The Counter-Flow Heat Exchanger Solution
12.3. The Log-Mean Temperature Difference Method
12.3.1. Introduction
12.3.2. Counter-Flow and Parallel-Flow Heat Exchangers
12.3.3. Shell-and-Tube and Cross-Flow Heat Exchangers
12.4. The Effectiveness
NTU Method
12.4.1. Introduction
12.4.2. Effectiveness, Number of Transfer Units, and Capacitance Ratio
12.4.3. Effectiveness
NTU Solution for a Counter-Flow Heat Exchanger
12.4.4. Effectiveness
NTU Solutions
12.4.5. Further Discussion of Heat Exchanger Effectiveness
Behavior as CR Approaches Zero
Behavior as NTU Approaches Zero
Behavior as NTU Becomes Infinite
Heat Exchanger Design
12.5. Conclusions and Learning Objectives
Heat Exchanger Conductance, Tube Banks, and Compact Heat Exchangers
Log-Mean Temperature Difference Solution
Effectiveness
NTU Solution
13. Mass Transfer
13.1. Composition Relationships
13.1.1. Ideal Gas Mixtures
13.2. Mass Diffusion
13.2.1. Fick's Law
13.2.2. The Diffusion Coefficient for Binary Mixtures
Gas Mixtures
Liquid Mixtures
Solids
13.2.3. Concentrations at Interfaces
Gas Mixture in Contact with Pure Liquid or Solid
Liquid Mixture in Contact with Pure Solid
Liquid Mixture in Contact with Gas
13.3. Transient Diffusion through a Stationary Solid
13.4. Diffusion of a Species in a Fluid
13.4.1. Diffusive and Advective Mass Transfer
13.4.2. Evaporation through a Layer of Gas
13.5. Momentum, Energy, and Mass Transfer Analogies
13.6. Simultaneous Heat and Mass Transfer
13.7. Conclusions and Learning Objectives
Concentration Relationships
The Diffusion Coefficient and Boundary Conditions
Transient Diffusion through a Solid
Diffusion of a Species in a Fluid
Heat Mass Transfer Analogy
Simultaneous Heat and Mass Transfer
14. Radiation
14.1. Introduction
14.1.1. Electromagnetic Radiation
14.1.2. The Electromagnetic Spectrum
14.2. Emission of Radiation by a Blackbody
14.2.1. Introduction
14.2.2. Blackbody Emission
Planck's Law
Blackbody Emission in Specified Wavelength Bands
14.3. Radiation Exchange between Black Surfaces
14.3.1. Introduction
14.3.2. View Factors
Inspection
The View Factor Integral
The Enclosure Rule
Reciprocity
Other View Factor Relationships
The Crossed and Uncrossed Strings Method
The View Factor Libraries
14.3.3. Blackbody Radiation Calculations
The Space Resistance
N-Surface Solutions
14.4. Radiation Characteristics of Real Surfaces
14.4.1. Introduction
14.4.2. Emission from Real Surfaces
Spectral, Directional Emissivity
Hemispherical Emissivity
Total Hemispherical Emissivity
The Diffuse Surface Approximation
The Diffuse Gray Surface Approximation
14.4.3. Reflectivity, Absorptivity, and Transmissivity
Diffuse and Specular Surfaces
Hemispherical and Total Hemispherical Reflectivity, Absorptivity, and Transmissivity
Kirchhoff's Law
14.5. Diffuse Gray Surface Radiation Exchange
14.5.1. Introduction
14.5.2. Radiosity
14.5.3. Diffuse Gray Surface Radiation Calculations
Resistance Network
14.6. Conclusions and Learning Objectives
Blackbody Radiation and the Electromagnetic Spectrum
View Factors
Blackbody Radiation Exchange
Properties of Real Surfaces
Diffuse Gray Surface Radiation Exchange
Projects.
Notes:
Includes bibliographical references and index.
ISBN:
9781107179530
110717953X
OCLC:
1099539610
Publisher Number:
99987477194

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