Heat exchangers : types, design, and applications / Spencer T. Branson.

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Bibliographic Details
Main Author: Branson, Spencer T.
Format: eBook
Language:English
Published: Hauppauge, N.Y. : Nova Science Publishers, ©2011.
Series:Energy science, engineering and technology series.
Subjects:
Online Access:Click for online access

MARC

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245 1 0 |a Heat exchangers :  |b types, design, and applications /  |c Spencer T. Branson. 
264 1 |a Hauppauge, N.Y. :  |b Nova Science Publishers,  |c ©2011. 
300 |a 1 online resource 
336 |a text  |b txt  |2 rdacontent 
337 |a computer  |b c  |2 rdamedia 
338 |a online resource  |b cr  |2 rdacarrier 
490 1 |a Energy science, engineering and technology 
504 |a Includes bibliographical references and index. 
588 0 |a Print version record. 
546 |a English. 
505 0 |a HEAT EXCHANGERS: TYPES, DESIGN, AND APPLICATIONS; HEAT EXCHANGERS: TYPES, DESIGN, AND APPLICATIONS ; CONTENTS ; PREFACE ; LIGHTWEIGHT COMPACT HEAT EXCHANGERS WITH OPEN-CELL METAL FOAMS ; ABSTRACT ; 1. INTRODUCTION ; 2. TOPOLOGIES OF OPEN-CELL METAL FOAMS ; 2.1. Macro/Micro Topologies ; 2.2. Fabrication Methods of Metal Foams ; 3. SINGLE PHASE FORCED CONVECTION IN OPEN-CELL METAL FOAMS ; 3.1. Pressure Drop (Loss) ; 3.1.1. Overall Pressure drop Behavior; 3.1.2. Empirical Correlations for Homogeneous Isotropic Foams with Open Cells. 
505 8 |a 3.1.3. Contribution of Overall Foam Shape and Size to Pressure Drop 3.1.4. Effect of Porosity on Pressure Drop ; 3.1.5. Effect of Pore Density (Pore Size) on Pressure Drop ; 3.2. Heat Transfer ; 3.2.1. Forced Convection Heat Transfer in Open-Cell Metal Foams ; 3.2.2. Analytical Modeling of Heat Transfer ; 3.2.3. Effect of Porosity (f) ; 3.2.4. Effect of Pore Size (Dp) and Pore Density (PPI) ; 3.2.5. Effect of Thermal Conductivity ; 3.3. Comparison of Overall Performance for Different Types of Heat Dissipation Medium ; 4. IMPINGING JETS ON OPEN-CELL METAL FOAMS ; 4.1. Impinging Round Jet. 
505 8 |a 4.2. Single Jet Flow Structures 4.3. Heat Transfer Enhancement ; 4.4. Effects of Topological Parameters ; 4.4.1. Effect of Porosity ; 4.4.2. Effect of Pore Density (Pore Size) ; 4.4.3. Effect of Foam Height ; 4.4.4. Effect of Foam Width ; 4.4.5. Effect of Nozzle-to-Foam Tip Distance ; 4.5. Impinging Annular Jet ; 4.5.1. Exit Flow Structures ; 4.5.2. Heat Transfer Enhancement ; 5. OPEN-CELL METAL FOAMS FOR ELECTRONICS COOLING ; 5.1. Background ; 5.2. Conventional Heat Sink (Exchanger) for Electronics Cooling ; 5.3. Open-Cell Metal Foam Heat Sink: Flow Field and Overall Thermal Performance. 
505 8 |a 5.5. Lightweight Compact Heat Sinks Acknowledgments ; APPENDIX A ; NOMENCLATURE ; Greek Symbols ; Abbreviations ; REFERENCES ; THE NTU-EFFECTIVENESS METHOD ; ABSTRACT ; 1. INTRODUCTION ; 2. THE PARALLEL FLOW HEAT EXCHANGER; 3. THE COUNTER FLOW HEAT EXCHANGER; 4. THE 1-2 HEAT EXCHANGER; 4.1. First Configuration (Inlets on the Same Side); 4.2. Second Configuration (Inlets on Opposite Sides); 5. THE 1-2N HEAT EXCHANGER ; 6. THE CROSS FLOW HEAT EXCHANGERS; 6.1. Unmixed-Mixed Configuration; 6.2. Mixed-Mixed Configuration; 6.1. Unmixed-Unmixed Configuration; 7. HEAT EXCHANGER NETWORKS. 
505 8 |a 7.1. Heat Exchangers Globally in a Counter Flow Configuration 7.2. Heat Exchangers Globally in a Parallel Flow Configuration ; 7.3. Heat Exchangers in Paralle/Serial Flow Configuration ; 8. EXAMPLES ; 8.1. Comparison of Counter Flow and Parallel Flow Heat Exchangers ; 8.2. Counter Flow Heat Exchanger (Variable Properties); 8.3. Cross Flow Heat Exchanger; 8.4. Coupled Heat Exchangers (Identical Effectiveness); 8.5. Coupled Heat Exchangers (Identical Heat Exchangers); 8.6. Determination of the Heat Exchanger Type and of the Overall Heat Transfer Coefficient. 
650 0 |a Heat exchangers. 
650 7 |a heat exchangers.  |2 aat 
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830 0 |a Energy science, engineering and technology series. 
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