Preface |
|
xv | |
|
1 Classification of Heat Exchangers |
|
|
1 | (28) |
|
|
1 | (1) |
|
1.2 Recuperation and Regeneration |
|
|
1 | (4) |
|
|
5 | (1) |
|
1.4 Geometry of Construction |
|
|
6 | (14) |
|
1.4.1 Tubular Heat Exchangers |
|
|
7 | (1) |
|
1.4.1.1 Double-Pipe Heat Exchangers |
|
|
8 | (1) |
|
1.4.1.2 Shell-and-Tube Heat Exchangers |
|
|
8 | (2) |
|
1.4.1.3 Spiral-Tube Heat Exchangers |
|
|
10 | (1) |
|
1.4.2 Plate Heat Exchangers |
|
|
10 | (1) |
|
1.4.2.1 Gasketed Plate Heat Exchangers |
|
|
11 | (1) |
|
1.4.2.2 Spiral Plate Heat Exchangers |
|
|
11 | (2) |
|
1.4.2.3 Lamella Heat Exchangers |
|
|
13 | (2) |
|
1.4.3 Extended Surface Heat Exchangers |
|
|
15 | (1) |
|
1.4.3.1 Plate-Fin Heat Exchanger |
|
|
15 | (5) |
|
1.5 Heat Transfer Mechanisms |
|
|
20 | (1) |
|
|
21 | (1) |
|
|
22 | (2) |
|
1.8 Selection of Heat Exchangers |
|
|
24 | (5) |
|
|
26 | (3) |
|
2 Basic Design Methods of Heat Exchangers |
|
|
29 | (40) |
|
|
29 | (1) |
|
2.2 Arrangement of Flow Paths in Heat Exchangers |
|
|
29 | (1) |
|
2.3 Basic Equations in Design |
|
|
29 | (4) |
|
2.4 Overall Heat Transfer Coefficient |
|
|
33 | (4) |
|
2.5 LMTD Method for Heat Exchanger Analysis |
|
|
37 | (11) |
|
2.5.1 Parallel- and Counterflow Heat Exchangers |
|
|
37 | (4) |
|
2.5.2 Multipass and Crossflow Heat Exchangers |
|
|
41 | (7) |
|
2.6 The e-NTU Method for Heat Exchanger Analysis |
|
|
48 | (9) |
|
2.7 Heat Exchanger Design Calculation |
|
|
57 | (1) |
|
2.8 Variable Overall Heat Transfer Coefficient |
|
|
58 | (2) |
|
2.9 Heat Exchanger Design Methodology |
|
|
60 | (9) |
|
|
63 | (5) |
|
|
68 | (1) |
|
3 Forced Convection Correlations for the Single-Phase Side of Heat Exchangers |
|
|
69 | (40) |
|
|
69 | (2) |
|
3.2 Laminar Forced Convection |
|
|
71 | (4) |
|
3.2.1 Hydrodynamically Developed and Thermally Developing Laminar Flow in Smooth Circular Ducts |
|
|
71 | (1) |
|
3.2.2 Simultaneously Developing Laminar Flow in Smooth Ducts |
|
|
72 | (1) |
|
3.2.3 Laminar Flow through Concentric Annular Smooth Ducts |
|
|
73 | (2) |
|
3.3 Effect of Variable Physical Properties |
|
|
75 | (5) |
|
3.3.1 Laminar Flow of Liquids |
|
|
76 | (2) |
|
3.3.2 Laminar Flow of Gases |
|
|
78 | (2) |
|
3.4 Turbulent Forced Convection |
|
|
80 | (3) |
|
3.5 Turbulent Flow in Smooth Straight Noncircular Ducts |
|
|
83 | (4) |
|
3.6 Effect of Variable Physical Properties in Turbulent Forced Convection |
|
|
87 | (3) |
|
3.6.1 Turbulent Liquid Flow in Ducts |
|
|
87 | (1) |
|
3.6.2 Turbulent Gas Flow in Ducts |
|
|
88 | (2) |
|
3.7 Summary of Forced Convection in Straight Ducts |
|
|
90 | (3) |
|
3.8 Heat Transfer from Smooth-Tube Bundles |
|
|
93 | (4) |
|
3.9 Heat Transfer in Helical Coils and Spirals |
|
|
97 | (2) |
|
3.9.1 Nusselt Numbers of Helical Coils---Laminar Flow |
|
|
98 | (1) |
|
3.9.2 Nusselt Numbers for Spiral Coils---Laminar Flow |
|
|
98 | (1) |
|
3.9.3 Nusselt Numbers for Helical Coils---Turbulent Flow |
|
|
99 | (1) |
|
3.10 Heat Transfer in Bends |
|
|
99 | (10) |
|
3.10.1 Heat Transfer in 90° Bends |
|
|
100 | (1) |
|
3.10.2 Heat Transfer in 180° Bends |
|
|
101 | (1) |
|
|
102 | (4) |
|
|
106 | (3) |
|
4 Heat Exchanger Pressure Drop and Pumping Power |
|
|
109 | (24) |
|
|
109 | (1) |
|
4.2 Tube-Side Pressure Drop |
|
|
109 | (5) |
|
4.2.1 Circular Cross-Sectional Tubes |
|
|
109 | (3) |
|
4.2.2 Noncircular Cross-Sectional Ducts |
|
|
112 | (2) |
|
4.3 Pressure Drop in Tube Bundles in Crossflow |
|
|
114 | (2) |
|
4.4 Pressure Drop in Helical and Spiral Coils |
|
|
116 | (2) |
|
4.4.1 Helical Coils---Laminar Flow |
|
|
116 | (1) |
|
4.4.2 Spiral Coils---Laminar Flow |
|
|
117 | (1) |
|
4.4.3 Helical Coils---Turbulent Flow |
|
|
117 | (1) |
|
4.4.4 Spiral Coils---Turbulent Flow |
|
|
118 | (1) |
|
4.5 Pressure Drop in Bends and Fittings |
|
|
118 | (6) |
|
4.5.1 Pressure Drop in Bends |
|
|
118 | (2) |
|
4.5.2 Pressure Drop in Fittings |
|
|
120 | (4) |
|
4.6 Pressure Drop for Abrupt Contraction, Expansion, and Momentum Change |
|
|
124 | (1) |
|
4.7 Heat Transfer and Pumping Power Relationship |
|
|
125 | (8) |
|
|
127 | (4) |
|
|
131 | (2) |
|
5 Micro/Nano Heat Transfer |
|
|
133 | (72) |
|
5.1 Part A---Heat Transfer for Gaseous and Liquid Flow in Microchannels |
|
|
133 | (28) |
|
5.1.1 Introduction of Heat Transfer in Microchannels |
|
|
133 | (1) |
|
5.1.2 Fundamentals of Gaseous Flow in Microchannels |
|
|
134 | (1) |
|
|
134 | (1) |
|
|
135 | (1) |
|
|
136 | (1) |
|
|
137 | (1) |
|
5.1.3 Engineering Applications for Gas Flow |
|
|
138 | (1) |
|
5.1.3.1 Heat Transfer in Gas Flow |
|
|
139 | (4) |
|
|
143 | (3) |
|
5.1.3.3 Laminar to Turbulent Transition Regime |
|
|
146 | (3) |
|
5.1.4 Engineering Applications of Single-Phase Liquid Flow in Microchannels |
|
|
149 | (2) |
|
5.1.4.1 Nusselt Number and Friction Factor Correlations for Single-Phase Liquid Flow |
|
|
151 | (5) |
|
5.1.4.2 Roughness Effect on Friction Factor |
|
|
156 | (1) |
|
5.1.5 Engineering Application of MicroChannel Heat Exchangers |
|
|
157 | (1) |
|
5.1.5.1 MicroChannel Heat Exchanger Theoretical Study |
|
|
158 | (2) |
|
5.1.5.2 MicroChannel Heat Exchanger Fabrication |
|
|
160 | (1) |
|
5.2 Part B---Single-Phase Convective Heat Transfer with Nanofluids |
|
|
161 | (44) |
|
5.2.1 Introduction of Convective Heat Transfer with Nanofluids |
|
|
161 | (1) |
|
5.2.1.1 Particle Materials and Base Fluids |
|
|
161 | (1) |
|
5.2.1.2 Particle Size and Shape |
|
|
162 | (1) |
|
5.2.1.3 Nanofluid Preparation Methods |
|
|
162 | (1) |
|
5.2.2 Thermal Conductivity of Nanofluids |
|
|
163 | (1) |
|
|
163 | (2) |
|
5.2.2.2 Brownian Motion of Nanoparticles |
|
|
165 | (2) |
|
5.2.2.3 Clustering of Nanoparticles |
|
|
167 | (2) |
|
5.2.2.4 Liquid Layering around Nanoparticles |
|
|
169 | (6) |
|
5.2.3 Thermal Conductivity Experimental Studies of Nanofluids |
|
|
175 | (3) |
|
5.2.4 Convective Heat Transfer of Nanofluids |
|
|
178 | (4) |
|
5.2.5 Analysis of Convective Heat Transfer of Nanofluids |
|
|
182 | (1) |
|
5.2.5.1 Constant Wall Heat Flux Boundary Condition |
|
|
183 | (1) |
|
5.2.5.2 Constant Wall Temperature Boundary Condition |
|
|
184 | (1) |
|
5.2.6 Experimental Correlations of Convective Heat Transfer of Nanofluids |
|
|
185 | (7) |
|
|
192 | (4) |
|
|
196 | (9) |
|
6 Fouling of Heat Exchangers |
|
|
205 | (30) |
|
|
205 | (1) |
|
|
205 | (2) |
|
|
207 | (4) |
|
6.3.1 Effect of Fouling on Heat Transfer |
|
|
207 | (1) |
|
6.3.2 Effect of Fouling on Pressure Drop |
|
|
208 | (2) |
|
|
210 | (1) |
|
|
211 | (5) |
|
6.4.1 Categories of Fouling |
|
|
211 | (1) |
|
6.4.1.1 Particulate Fouling |
|
|
211 | (1) |
|
6.4.1.2 Crystallization Fouling |
|
|
211 | (1) |
|
6.4.1.3 Corrosion Fouling |
|
|
212 | (1) |
|
|
212 | (1) |
|
6.4.1.5 Chemical Reaction Fouling |
|
|
212 | (1) |
|
6.4.2 Fundamental Processes of Fouling |
|
|
212 | (1) |
|
|
212 | (1) |
|
|
213 | (1) |
|
|
213 | (1) |
|
|
213 | (1) |
|
|
214 | (1) |
|
6.4.3 Prediction of Fouling |
|
|
214 | (2) |
|
6.5 Design of Heat Exchangers Subject to Fouling |
|
|
216 | (10) |
|
|
216 | (4) |
|
|
220 | (1) |
|
6.5.3 Percent over Surface |
|
|
221 | (5) |
|
6.6 Operations of Heat Exchangers Subject to Fouling |
|
|
226 | (1) |
|
6.7 Techniques to Control Fouling |
|
|
227 | (8) |
|
6.7.1 Surface Cleaning Techniques |
|
|
228 | (1) |
|
6.7.1.1 Continuous Cleaning |
|
|
228 | (1) |
|
6.7.1.2 Periodic Cleaning |
|
|
228 | (1) |
|
|
228 | (1) |
|
6.7.2.1 Crystallization Fouling |
|
|
228 | (1) |
|
6.7.2.2 Particulate Fouling |
|
|
228 | (1) |
|
6.7.2.3 Biological Fouling |
|
|
228 | (1) |
|
6.7.2.4 Corrosion Fouling |
|
|
229 | (1) |
|
|
229 | (3) |
|
|
232 | (3) |
|
7 Double-Pipe Heat Exchangers |
|
|
235 | (30) |
|
|
235 | (3) |
|
7.2 Thermal and Hydraulic Design of Inner Tube |
|
|
238 | (1) |
|
7.3 Thermal and Hydraulic Analysis of Annulus |
|
|
239 | (12) |
|
7.3.1 Hairpin Heat Exchanger with Bare Inner Tube |
|
|
239 | (4) |
|
7.3.2 Hairpin Heat Exchangers with Multitube Finned Inner Tubes |
|
|
243 | (8) |
|
7.4 Parallel-Series Arrangements of Hairpins |
|
|
251 | (2) |
|
|
253 | (1) |
|
7.6 Design and Operational Features |
|
|
254 | (11) |
|
|
257 | (6) |
|
|
263 | (2) |
|
8 Design Correlations for Condensers and Evaporators |
|
|
265 | (46) |
|
|
265 | (1) |
|
|
265 | (1) |
|
8.3 Film Condensation on a Single Tube |
|
|
266 | (3) |
|
8.3.1 Laminar Film Condensation |
|
|
266 | (1) |
|
|
267 | (2) |
|
8.4 Film Condensation in Tube Bundles |
|
|
269 | (8) |
|
8.4.1 Effect of Condensate Inundation |
|
|
270 | (3) |
|
8.4.2 Effect of Vapor Shear |
|
|
273 | (1) |
|
8.4.3 Combined Effects of Inundation and Vapor Shear |
|
|
273 | (4) |
|
8.5 Condensation inside Tubes |
|
|
277 | (7) |
|
8.5.1 Condensation inside Horizontal Tubes |
|
|
277 | (4) |
|
8.5.2 Condensation inside Vertical Tubes |
|
|
281 | (3) |
|
|
284 | (27) |
|
|
284 | (1) |
|
|
285 | (3) |
|
8.6.3 Flow Boiling Correlations |
|
|
288 | (15) |
|
|
303 | (3) |
|
|
306 | (5) |
|
9 Shell-and-Tube Heat Exchangers |
|
|
311 | (56) |
|
|
311 | (1) |
|
|
311 | (15) |
|
|
311 | (2) |
|
|
313 | (2) |
|
9.2.3 Tubes and Tube Passes |
|
|
315 | (4) |
|
|
319 | (4) |
|
9.2.5 Baffle Type and Geometry |
|
|
323 | (2) |
|
9.2.6 Allocation of Streams |
|
|
325 | (1) |
|
9.3 Basic Design Procedure of a Heat Exchanger |
|
|
326 | (7) |
|
9.3.1 Preliminary Estimation of Unit Size |
|
|
327 | (5) |
|
9.3.2 Rating of the Preliminary Design |
|
|
332 | (1) |
|
9.4 Shell-Side Heat Transfer and Pressure Drop |
|
|
333 | (34) |
|
9.4.1 Shell-Side Heat Transfer Coefficient |
|
|
334 | (1) |
|
9.4.2 Shell-Side Pressure Drop |
|
|
335 | (1) |
|
9.4.3 Tube-Side Pressure Drop |
|
|
336 | (4) |
|
9.4.4 Bell-Delaware Method |
|
|
340 | (2) |
|
9.4.4.1 Shell-Side Heat Transfer Coefficient |
|
|
342 | (8) |
|
9.4.4.2 Shell-Side Pressure Drop |
|
|
350 | (11) |
|
|
361 | (5) |
|
|
366 | (1) |
|
10 Compact Heat Exchangers |
|
|
367 | (20) |
|
|
367 | (5) |
|
10.1.1 Heat Transfer Enhancement |
|
|
367 | (3) |
|
10.1.2 Plate-Fin Heat Exchangers |
|
|
370 | (1) |
|
10.1.3 Tube-Fin Heat Exchangers |
|
|
370 | (2) |
|
10.2 Heat Transfer and Pressure Drop |
|
|
372 | (15) |
|
|
372 | (5) |
|
10.2.2 Pressure Drop for Finned-Tube Exchangers |
|
|
377 | (1) |
|
10.2.3 Pressure Drop for Plate-Fin Exchangers |
|
|
378 | (4) |
|
|
382 | (3) |
|
|
385 | (2) |
|
11 Gasketed-Plate Heat Exchangers |
|
|
387 | (38) |
|
|
387 | (1) |
|
|
387 | (5) |
|
11.2.1 Plate Pack and the Frame |
|
|
387 | (3) |
|
|
390 | (2) |
|
11.3 Operational Characteristics |
|
|
392 | (2) |
|
|
392 | (2) |
|
11.3.2 Performance Limits |
|
|
394 | (1) |
|
11.4 Passes and Flow Arrangements |
|
|
394 | (2) |
|
|
396 | (4) |
|
|
397 | (2) |
|
|
399 | (1) |
|
11.6 Heat Transfer and Pressure Drop Calculations |
|
|
400 | (15) |
|
11.6.1 Heat Transfer Area |
|
|
400 | (1) |
|
11.6.2 Mean Flow Channel Gap |
|
|
401 | (1) |
|
11.6.3 Channel Hydraulic Diameter |
|
|
401 | (1) |
|
11.6.4 Heat Transfer Coefficient |
|
|
401 | (6) |
|
11.6.5 Channel Pressure Drop |
|
|
407 | (2) |
|
11.6.6 Port Pressure Drop |
|
|
409 | (1) |
|
11.6.7 Overall Heat Transfer Coefficient |
|
|
410 | (1) |
|
11.6.8 Heat Transfer Surface Area |
|
|
410 | (1) |
|
11.6.9 Performance Analysis |
|
|
411 | (4) |
|
|
415 | (10) |
|
|
417 | (4) |
|
|
421 | (4) |
|
12 Condensers and Evaporators |
|
|
425 | (46) |
|
|
425 | (1) |
|
12.2 Shell-and-Tube Condensers |
|
|
425 | (8) |
|
12.2.1 Horizontal Shell-Side Condensers |
|
|
425 | (4) |
|
12.2.2 Vertical Shell-Side Condensers |
|
|
429 | (1) |
|
12.2.3 Vertical Tube-Side Condensers |
|
|
430 | (1) |
|
12.2.4 Horizontal in-Tube Condensers |
|
|
430 | (3) |
|
12.3 Steam Turbine Exhaust Condensers |
|
|
433 | (1) |
|
|
433 | (1) |
|
12.5 Air-Cooled Condensers |
|
|
434 | (1) |
|
12.6 Direct-Contact Condensers |
|
|
435 | (1) |
|
12.7 Thermal Design of Shell-and-Tube Condensers |
|
|
436 | (9) |
|
12.8 Design and Operational Considerations |
|
|
445 | (2) |
|
12.9 Condensers for Refrigeration and Air-Conditioning |
|
|
447 | (4) |
|
12.9.1 Water-Cooled Condensers |
|
|
448 | (1) |
|
12.9.2 Air-Cooled Condensers |
|
|
449 | (1) |
|
12.9.3 Evaporative Condensers |
|
|
449 | (2) |
|
12.10 Evaporators for Refrigeration and Air-Conditioning |
|
|
451 | (4) |
|
12.10.1 Water-Cooling Evaporators (Chillers) |
|
|
452 | (1) |
|
12.10.2 Air-Cooling Evaporators (Air Coolers) |
|
|
453 | (2) |
|
|
455 | (4) |
|
|
455 | (2) |
|
12.11.2 Kandlikar Correlation |
|
|
457 | (1) |
|
12.11.3 Gungor and Winter ton Correlation |
|
|
458 | (1) |
|
12.12 Standards for Evaporators and Condensers |
|
|
459 | (12) |
|
|
464 | (4) |
|
|
468 | (3) |
|
13 Polymer Heat Exchangers |
|
|
471 | (28) |
|
|
471 | (3) |
|
13.2 Polymer Matrix Composite (PMC) Materials |
|
|
474 | (3) |
|
|
477 | (1) |
|
13.4 Application of Polymers in Heat Exchangers |
|
|
478 | (8) |
|
13.5 Polymer Compact Heat Exchangers |
|
|
486 | (4) |
|
13.6 Potential Applications for Polymer Film Compact Heat Exchangers |
|
|
490 | (2) |
|
13.7 Thermal Design of Polymer Heat Exchangers |
|
|
492 | (7) |
|
|
494 | (5) |
Appendix A Physical Properties of Metals and Nonmetals |
|
499 | (4) |
Appendix B Physical Properties of Air, Water, Liquid Metals, and Refrigerants |
|
503 | (18) |
Index |
|
521 | |