Acknowledgement Wolverine Tube Inc. wishes to express its appreciation to Dr. K. J. Bell and Dr. A. C. Mueller for autho
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Acknowledgement Wolverine Tube Inc. wishes to express its appreciation to Dr. K. J. Bell and Dr. A. C. Mueller for authorship of this manual. Acknowledgement is made in the text for material which has been used from other sources.
© 2001, electronic distribution by Wolverine Tube, Inc. Research and Development Team
© 1984, original paper distribution by Wolverine Division of UOP Inc. All rights reserved.
TABLE OF CONTENTS Chapter 1 Basic Heat Transfer Section 1
Section 2
Section 3
Section 4
Section 5
Basic Mechanisms of Heat Transfer Conduction
6
Single Phase Convection
8
Two Phase (Liquid-Gas/Vapor) Flow
11
Condensation
14
Vaporization
17
Radiation
19
Basic Heat Exchanger Equations The Overall Heat Transfer Coefficient
21
The Design Integral
23
The Mean Temperature Difference The Logarithmic Mean Temperature Difference (LMTD)
25
Configuration Correction Factors on the LMTD
27
Construction of Shell and Tube heat Exchangers Why a Shell and Tube Heat Exchanger?
32
Basic Components of Shell and Tube Heat Exchangers
32
Provisions for Thermal Stress
35
Mechanical Stresses
37
The Vibration Problem
37
Erosion
38
Cost of Shell and Tube Heat Exchangers
38
Allocation of Streams in a Shell and Tube Exchanger
39
Application of Extended Surfaces to Heat Exchangers The Concept of the Controlling Resistance
40
Types of Extended Surface
40
Fin Efficiencies and Related Concepts
41
The Fin Resistance Method
43
Some Applications of Finned Tubes
45
1
Section 6
Fouling in Heat Exchangers Typical Fouling Resistances
45
Types of Fouling
45
Effect of Fouling on Heat Transfer
46
Materials Selection for Fouling Services
46
Removal of Fouling
47
Chapter 2 Sensible Heat Transfer Section 1
Section 2
Section 3
Section 4
Section 5
Section 6
Heat Exchangers with Low- and Medium-Finned Trufin Areas of Application
58
Description of Low- and Medium-Finned Trufin
59
Basic Equations for Heat Exchanger Design The Basic Design Equation and Overall Heat Transfer Coefficient
60
Fin Efficiency and Fin Resistance
61
Mean Temperature Difference, F Factors
62
Heat Transfer and Pressure Drop during Flow across Banks of Trufin Tubes Heat Transfer In Trufin Tube Banks
72
Pressure Drop During Flow Across Banks of Low-Finned Trufin Tubes
74
Effect of Fouling on Trufin
76
Heat Transfer and Pressure Drop Inside Tubes Heat Transfer and Pressure Drop in Single Phase Flow inside Round Tubes
77
Heat Transfer in Two-Phase Flow Inside Tubes
83
Preliminary Design of Shell and Tube Heat Exchangers Basic Principles of Design
85
Preliminary Design Decisions
86
Procedure for Approximate Size Estimation
89
Delaware Method for Shell-Side Rating of Shell and Tube Heat Exchangers Introduction
96
Calculation of Shell-Side Geometrical Parameters
97
Shell-Side Heat Transfer Coefficient Calculation
106
Shell-Side Pressure Drop Calculation
107
2
Section 7
Examples of Design Problems for Low- and Medium-Finned Trufin in Shell and Tube Heat Exchangers Design of a Compressor After-cooler
116
Design of a Gas Oil to Crude Heat Recovery Exchanger
122
Chapter 3 Condensing Heat Transfer Section 1
Section 2
Section 3
Section 4
Trufin Tubes in Condensing Heat Transfer Modes of Condensation
142
Areas of Application
142
Types of Tubes Available
143
Condensation of Vapor inside High-Finned Trufin Tubes Vapor-Liquid Two-Phase Flow
144
Condensation Heat Transfer
154
Mean Temperature Difference for In-Tube Condensation
162
Condensation of Vapor outside Low- and Medium-Finned Trufin Tubes Shell and Tube Heat Exchangers for Condensing Applications
166
The Basic Design Equations
172
Mean Temperature Difference
173
Condensation of a Superheated Vapor
173
Condensation with Integral Sub-cooling On the Shell-side
174
Film-wise Condensation on Plain and Trufin Tubes
178
Film-wise Condensation on Tube Banks
180
Pressure Drop during Shell-side Condensation
181
Examples of Design Problems for Low- and Medium-Finned Trufin in Shell and Tube Condensers Condenser Design for a Pure Component: Example Problem
182
Condenser Design for a Multi-component Mixture: Example Problem
192
Chapter 4 Trufin Tubes in Air-cool Heat Exchangers Section 1
Heat Exchangers with High-Finned Trufin Tubes Areas of Application
208
High-Finned Trufin
209
Description of Equipment
210
3
Section 2
Section 3
Section 4
Section 5
Heat Transfer with High-Finned Trufin Tubes Fin Temperature Distribution and Fin Efficiency
215
Effect of Fouling on High-Finned Trufin
217
Contact Resistance in Bimetallic Tubes
218
Heat Transfer and Pressure Drop in High-Finned Trufin Tube Banks Heat Transfer Coefficients in Cross-flow
219
Mean Temperature Difference in Cross-flow
221
Pressure Drop in Cross-flow
223
Other Air-Side Pressure Effects
225
Preliminary Design Procedures Principles of the Design Process
226
Selection of Preliminary Design Parameters
226
Fundamental Limitations Controlling Air-cool Heat Exchanger Design
228
Final Design
235
Chapter 5 Trufin Tubes in Boiling Heat Transfer Section 1
Section 2
Section 3
Boiling Theory Pool Boiling Curve
240
Nucleation
242
Nucleate Boiling Curve
243
Maximum or Critical Heat Flux
244
Film Boiling
245
Boiling Inside Tubes
246
Sub-cooling and Agitation
246
Vaporizers - Types and Usage General
248
Boiling Outside Tubes
248
Boiling Inside Tubes
250
Other Types of Evaporators
252
Boiling Heat Transfer Pool Boiling - Single Tube
254
Single Tube in Cross Flow
258
Boiling on Outside of Tubes in a Bundle
258
4
Section 4
Section 5
Section 6
Boiling Inside Tubes
259
Boiling of Mixtures
263
Falling Film Heat Transfer Vertical In-Tube Vaporizer
266
Horizontal Shell-Side Vaporizer
267
Dry Spots - Film Breakdown
267
Special Surfaces Boiling on Fins
268
Mean Temperature Difference
269
Pressure Drop Tube-Side Pressure Drop
271
Shell-Side Pressure Drop
273
Section 7
Fouling
275
Section 8
Design Procedures
Section 9
Selection of Re-boiler Type
278
Pool Type Re-boilers
278
In-tube or Thermosyphon Re-boilers
279
Special Considerations Examples of Design Problems
Section 10
283
Example of Design Problems for Trufin in Boiling Heat Transfer Design Example - Kettle Re-boiler
284
In-Tube Thermosyphon - Example Problem
287
Boiling Outside Trufin Tubes - Example Problem
292
5