Preface |
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viii | |
Conversion Factors |
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x | |
Physical Constants |
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xi | |
Acknowledgements |
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xii | |
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1 | (42) |
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2 | (1) |
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Fourier's Law of Heat Conduction |
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2 | (4) |
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The Heat Conduction Equation |
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6 | (9) |
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15 | (4) |
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The Conduction Shape Factor |
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19 | (5) |
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Unsteady-State Conduction |
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24 | (7) |
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Mechanisms of Heat Conduction |
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31 | (12) |
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43 | (42) |
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44 | (1) |
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Combined Conduction and Convection |
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44 | (3) |
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47 | (6) |
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Forced Convection in Pipes and Ducts |
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53 | (9) |
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Forced Convection in External Flow |
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62 | (3) |
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65 | (20) |
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85 | (42) |
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86 | (1) |
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86 | (1) |
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87 | (6) |
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The Overall Heat-Transfer Coefficient |
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93 | (5) |
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The LMTD Correction Factor |
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98 | (4) |
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Analysis of Double-Pipe Exchangers |
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102 | (4) |
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Preliminary Design of Shell-and-Tube Exchangers |
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106 | (3) |
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Rating a Shell-and-Tube Exchanger |
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109 | (5) |
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Heat-Exchanger Effectiveness |
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114 | (13) |
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Design of Double-Pipe Heat Exchangers |
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127 | (60) |
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128 | (1) |
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Heat-Transfer Coefficients for Exchangers without Fins |
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128 | (1) |
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Hydraulic Calculations for Exchangers without Fins |
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128 | (3) |
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Series/Parallel Configurations of Hairpins |
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131 | (1) |
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132 | (1) |
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Over-Surface and Over-Design |
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133 | (8) |
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141 | (2) |
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Heat-Transfer Coefficients and Friction Factors for Finned Annuli |
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143 | (2) |
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Wall Temperature for Finned Pipes |
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145 | (7) |
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152 | (35) |
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Design of Shell-and-Tube Heat Exchangers |
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187 | (58) |
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188 | (1) |
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Heat-Transfer Coefficients |
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188 | (1) |
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189 | (3) |
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192 | (2) |
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194 | (1) |
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Factors Affecting Pressure Drop |
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195 | (2) |
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197 | (4) |
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201 | (17) |
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218 | (27) |
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245 | (32) |
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246 | (1) |
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Ideal Tube Bank Correlations |
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246 | (2) |
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Shell-Side Heat-Transfer Coefficient |
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248 | (2) |
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250 | (4) |
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254 | (5) |
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Correlations for the Correction Factors |
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259 | (1) |
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260 | (17) |
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The Stream Analysis Method |
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277 | (50) |
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278 | (1) |
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The Equivalent Hydraulic Network |
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278 | (1) |
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279 | (2) |
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281 | (1) |
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Shell-Side Heat-Transfer Coefficient |
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281 | (1) |
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Temperature Profile Distortion |
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282 | (2) |
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The Wills-Johnston Method |
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284 | (11) |
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295 | (32) |
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327 | (58) |
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328 | (1) |
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328 | (1) |
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329 | (1) |
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329 | (2) |
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331 | (3) |
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The Grand Composite Curve |
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334 | (1) |
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Significance of the Pinch |
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335 | (2) |
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Threshold Problems and Utility Pinches |
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337 | (1) |
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Feasibility Criteria at the Pinch |
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337 | (2) |
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339 | (1) |
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Minimum-Utility Design for TC3 |
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340 | (4) |
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344 | (3) |
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347 | (1) |
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Targeting for Number of Shells |
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348 | (5) |
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353 | (3) |
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356 | (2) |
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358 | (1) |
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Targeting by Linear Programming |
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359 | (2) |
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361 | (24) |
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385 | (58) |
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386 | (1) |
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386 | (1) |
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Correlations for Nucleate Boiling on Horizontal Tubes |
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387 | (15) |
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402 | (14) |
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Convective Boiling in Tubes |
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416 | (12) |
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428 | (15) |
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443 | (96) |
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444 | (1) |
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444 | (5) |
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Design of Kettle Reboilers |
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449 | (18) |
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Design of Horizontal Thermosyphon Reboilers |
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467 | (6) |
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Design of Vertical Thermosyphon Reboilers |
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473 | (15) |
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488 | (51) |
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539 | (90) |
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540 | (1) |
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540 | (5) |
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Condensation on a Vertical Surface: Nusselt Theory |
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545 | (4) |
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Condensation on Horizontal Tubes |
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549 | (3) |
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Modifications of Nusselt Theory |
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552 | (10) |
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Condensation Inside Horizontal Tubes |
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562 | (6) |
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Condensation on Finned Tubes |
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568 | (1) |
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569 | (2) |
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Mean Temperature Difference |
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571 | (19) |
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Multi-component Condensation |
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590 | (5) |
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595 | (34) |
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Air-Cooled Heat Exchangers |
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629 | (52) |
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630 | (1) |
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630 | (7) |
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Air-Side Heat-Transfer Coefficient |
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637 | (1) |
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638 | (2) |
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Overall Heat-Transfer Coefficient |
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640 | (1) |
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640 | (3) |
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Mean Temperature Difference |
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643 | (1) |
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643 | (1) |
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644 | (9) |
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653 | (28) |
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681 | (62) |
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Appendix A Thermophysical Properties of Materials |
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682 | (35) |
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Appendix B Dimensions of Pipe and Tubing |
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717 | (12) |
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Appendix C Tube-Count Tables |
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729 | (8) |
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Appendix D Equivalent Lengths of Pipe Fittings |
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737 | (3) |
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Appendix E Properties of Petroleum Streams |
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740 | (3) |
Index |
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743 | |