Heat Exchanger Design Handbook - Online
|
Table of Contents:Heat exchanger theoryContributorsPreface Preface to 1998 Edition of Part 1 Preface to First Edition of Part 1 1.1 DESCRIPTION OF HEAT EXCHANGER TYPES 1.1.0 Structure of the Section, D. Brian Spalding 1.1.1 Types of Flow Configuration, D. Brian Spalding 1.1.2 Types of Interactions between Streams, D. Brian Spalding 1.1.3 Types of Temperature Change Pattern, D. Brian Spalding 1.1.4 Types of Interface between Streams, D. Brian Spalding 1.1.5 Types of Heat Exchange Equipment, D. Brian Spalding 1.1.6 Unsteady Operation, D. Brian Spalding 1.2 DEFINITIONS AND QUANTITATIVE RELATIONSHIPS FOR HEAT EXCHANGERS 1.2.0 Structure of the Section, D. Brian Spalding 1.2.1 Thermodynamics: Brief Notes on Important Concepts, D. Brian Spalding 1.2.2 Flux Relationships, D. Brian Spalding 1.2.3 Transfer Coefficient Dependences, D. Brian Spalding 1.2.4 Balance Equations Applied to Complete Equipment, D. Brian Spalding 1.2.5 The Differential Equations Governing Streams, D. Brian Spalding 1.2.4 Partial Differential Equations for Interpenetrating Continua, D. Brian Spalding 1.3 ANALYTIC SOLUTIONS TO HEAT EXCHANGER EQUATIONS 1.3.1 Uniform-Transfer-Coefficient Solutions for the No-Phase-Change Heat Exchanger, D. Brian Spalding 1.3.2 Other Analytic Solutions, D. Brian Spalding 1.4 NUMERICAL SOLUTION PROCEDURES FOR HEAT EXCHANGER EQUATIONS 1.4.1 Cases with Prescribed Flow Patterns, D. Brian Spalding 1.4.2 Cases in Which the Flow Patterns Must Be Calculated, D. Brian Spalding 1.4.3 Special Applications of Numerical solution Procedures, D. Brian Spalding 1.5 CHARTS FOR MEAN TEMPERATURE DIFFERENCE IN INDUSTRIAL HEAT EXCHANGER CONFIGURATIONS 1.5.1 Introduction, J. Taborek 1.5.2 F and ( Charts for Shell-and-Tube Exchangers, J. Taborek 1.5.3 F and( Charts for Cross-Flow and other Exchangers, J. Taborek 1.6 SHELL-AND-TUBE HEAT EXCHANGERS (CELL METHOD) 1.6.1 Introduction, E. S. Gaddis 1.6.2 Calculation Procedure, E. S. Gaddis 1.6.3 Numerical Examples, E. S. Gaddis 1.6.4 Rules for Highest Heat Exchanger Effectiveness, E. S. Gaddis 1.6.5 Special Case of Two Tube-Side Passes, E. S. Gaddis 1.6.6 Computational Procedure for the Special Case of Two Tube-Tube Passes, E. S. Gaddis 1.6.7 Heat Exchangers with Two Tube-Side Passes, a Constant Cell Effectiveness and a Variable Number of Segmental Baffles, E. S. Gaddis 1.6.8 Special Case of Three Tube-Side Passes and Two Segmental Baffles, E. S. Gaddis 1.6.9 Heat Exchangers with Longitudinal Baffles, E. S. Gaddis 1.6.10 Cell Effectiveness, E. S. Gaddis 1.6.11 Comparison of the Conventional Method and the Cell Method, E. S. Gaddis 1.6.12 General Remarks, E. S. Gaddis 1.7 PINCH ANALYSIS FOR NETWORK DESIGN 1.7.1 Introduction, B. Linnhoff and R. Smith 1.7.2 The Pinch Concept, B. Linnhoff and R. Smith 1.7.3 The Pinch Design Method, B. Linnhoff and R. Smith 1.7.4 Design Without a Pinch and With Multiple Pinches, B. Linnhoff and R. Smith 1.7.5 Utility Selection, B. Linnhoff and R. Smith 1.7.6 Conclusions, B. Linnhoff and R. Smith 1.8 ENTROPY GENERATION MINIMIZATION (EGM) IN HEAT TRANSFER DEVICES 1.8.1 Introduction, A. Bejan 1.8.2 Entropy Generation Minimization at the Elemental Level, A. Bejan 1.8.3 Entropy Generation Minimization at the Component Level, A. Bejan 1.8.4 Entropy Generation Minimization at the System Level, A. Bejan 1.9 EXERGY ANALYSIS 1.9.1 Introduction, D. Limb 1.9.2 The Concept of Exergy, D. Limb 1.9.3 Calculation of the Exergy of a Stream, D. Limb 1.9.4 Reversible (Minimum) Work for some Processes, D. Limb 1.9.5 Assessing Lost Work in Unit Operations, D. Limb INDEX (END OF FIRST VOLUME) |