Page 5 - Applied Process Design For Chemical And Petrochemical Plants Volume III
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Contents
Foreword to the Second Edition........... ix Bundle, 116; Horizontal Tube Bundle, 119; Step-
wise Use of Devore Charts, 121; Subcooling, 122;
Film Temperature Estimation for Condensing,
123; Condenser Design Procedure, 123; Example
Preface to the Third Edition................... xi
10-10. Total Condenser, 124; RODbaffled® (Shell-
Side) Exchangers, 129; Condensation Inside
Tubes, 129; Example 10-11. Desuperheating and
10. Heat Transfer.................................... 1 Condensing Propylene in Shell, 134; Example 10-
12. Steam Heated Feed Preheater—Steam in
Types of Heat Transfer Equipment Terminology, Shell, 138; Example 10-13. Gas Cooling and Partial
1; Details of Exchange Equipment Assembly and Condensing in Tubes, 139; Condensing Vapors in
Arrangement, 8; 1. Construction Codes, 8; 2. Ther- Presence of Noncondensable Gases, 143; Example
mal Rating Standards, 8; 3. Exchanger Shell Types, 10-14. Chlorine-Air Condenser, Noncondensables,
8; 4. Tubes, 10; 5. Baffles, 24; 6. Tie Rods, 31; 7. Vertical Condenser, 144; Example 10-15. Con-
Tubesheets, 32; 8. Tube Joints in Tubesheets, 34 densing in Presence of Noncondensables, Col-
Example 10-1. Determine Outside Heat Transfer burn-Hougen Method, 148; Multizone Heat
Area of Heat Exchanger Bundle, 35; Tubesheet Exchange, 154; Fluids in Annulus of Tube-in-Pipe
Layouts, 35; Tube Counts in Shells, 35; Exchanger or Double Pipe Exchanger, Forced Convection,
Surface Area, 50; Effective Tube Surface, 51; 154; Approximation of Scraped Wall Heat Trans-
Effective Tube Length for U-Tube Heat Exchang- fer, 154; Heat Transfer in Jacketed, Agitated Ves-
ers, 51; Example 10-2. Use of U-Tube Area Chart, sels/Kettles, 156; Example 10-16. Heating Oil
51; Nozzle Connections to Shell and Heads, 53; Using High Temperature Heat Transfer Fluid,
Types of Heat Exchange Operations, 53; Thermal 157; Pressure Drop, 160; Falling Film Liquid Flow
Design, 53; Temperature Difference: Two Fluid in Tubes, 160; Vaporization and Boiling, 161;
Transfer, 55; Mean Temperature Difference or Vaporization in Horizontal Shell; Natural Circula-
Log Mean Temperature Difference, 57; Example tion, 164; Vaporization in Horizontal Shell; Nat-
10-3. One Shell Pass, 2 Tube Passes Parallel-Coun- ural Circulation, 165; Pool and Nucleate Boiling
terflow Exchanger Cross, After Murty, 57; Exam- — General Correlation for Heat Flux and Critical
ple 10-4. Performance Examination for Exit Temperature Difference, 165; Reboiler Heat Bal-
Temperature of Fluids, 72; Correction for Multi- ance, 168; Example 10-17. Reboiler Heat Duty
pass Flow through Heat Exchangers, 72; Heat after Kern, 169; Kettle Horizontal Reboilers, 169;
Load or Duty, 74; Example 10-5. Calculation of Nucleate or Alternate Designs Procedure , 173;
Weighted MTD, 74; Example 10-6. Heat Duty of a Kettle Reboiler Horizontal Shells, 174; Horizontal
Condenser with Liquid Subcooling, 74; Heat Bal- Kettle Reboiler Disengaging Space, 174; Kettel
ance, 74; Transfer Area, 75; Example 10-7. Calcu- Horizontal Reboilers, Alternate Designs, 174;
lation of LMTD and Correction, 75; Temperature Example 10-18. Kettle Type Evaporator — Steam
for Fluid Properties Evaluation — Caloric Tem- in Tubes, 176; Boiling: Nucleate Natural Circula-
perature, 75; Tube Wall Temperature, 76; Fouling tion (Thermosiphon) Inside Vertical Tubes or
of Tube Surface, 78; Overall Heat Transfer Coef- Outside Horizontal Tubes, 177; Gilmour Method
ficients for Plain or Bare Tubes, 87; Approximate Modified, 178; Suggested Procedure for Vaporiza-
Values for Overall Coefficients, 90; Example 10-8. tion with Sensible Heat Transfer, 181; Procedure
Calculation of Overall Heat Transfer Coefficient for Horizontal Natural Circulation Thermosiphon
from Individual Components, 90; Film Coeffi- Reboiler, 182; Kern Method, 182; Vaporization
cients with Fluid Inside Tubes, Forced Convection, Inside Vertical Tubes; Natural Thermosiphon
94; Film Coefficients with Fluids Outside Tubes, Action, 182; Fair’s Method, 182; Example 10-19.
101; Forced Convection, 101; Shell-Side Equiva- C3 Splitter Reboiler, 194; Example 10-20. Cyclo-
lent Tube Diameter, 102; Shell-Side Velocities, 107; hexane Column Reboiler, 197; Kern’s Method
Design Procedure for Forced Convection Heat Stepwise, 198; Other Design Methods, 199; Exam-
Transfer in Exchanger Design, 109; Example 10-9. ple 10-21. Vertical Thermosiphon Reboiler, Kern’s
Convection Heat Transfer Exchanger Design, 112; Method, 199; Simplified Hajek Method—Vertical
Spiral Coils in Vessels, 116; Tube-Side Coefficient, Thermosiphon Reboiler, 203; General Guides for
116; Outside Tube Coefficients, 116; Condensa- Vertical Thermosiphon Reboilers Design, 203;
tion Outside Tube Bundles, 116; Vertical Tube Example 10-22. Hajek’s Method—Vertical Ther-
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