عنوان

Process heat transfer

شابک

0123971950

شابک

9780123971951

شابک اشتباه

9780123977922

شماره

dltt

عنوان اصلي

Process heat transfer

نام عام مواد

[Book]

ساير اطلاعات عنواني

principles, applications and rules of thumb /

نام نخستين پديدآور

Robert W. Serth (Department of Chemical and Natural Gas Engineering, Texas A&M University-Kingsville, Kingsville, Texas, USA), Thomas G. Lestina (Vice President, Research & Engineering Services, Heat Transfer Research, Inc., College Station, Texas, USA).

وضعيت ويراست

Second edition.

محل نشرو پخش و غیره

Amsterdam :

نام ناشر، پخش کننده و غيره

Elsevier/AP, Academic Press is an imprint of Elsevier,

تاریخ نشرو بخش و غیره

2014.

متن يادداشت

Previous edition: published as by R.W. Serth, 2007.

متن يادداشت

Includes bibliographical references and index.

متن يادداشت

Contents note continued: 12.1. Introduction -- 12.2. Equipment Description -- 12.3. Air-Side Heat-Transfer Coefficient -- 12.4. Air-Side Pressure Drop -- 12.5. Overall Heat-Transfer Coefficient -- 12.6. Fan and Motor Sizing -- 12.7. Mean Temperature Difference -- 12.8. Design Guidelines -- 12.9. Design Strategy -- 12.10.Computer Software.

متن يادداشت

Contents note continued: 4.2. Heat-Transfer Coefficients for Exchangers without Fins -- 4.3. Hydraulic Calculations for Exchangers without Fins -- 4.4. Series/Parallel Configurations of Hairpins -- 4.5. Multi-Tube Exchangers -- 4.6. Over-Surface and Over-Design -- 4.7. Finned-Pipe Exchangers -- 4.8. Heat-Transfer Coefficients and Friction Factors for Finned Annuli -- 4.9. Wall Temperature for Finned Pipes -- 4.10.Computer Software -- 5. Design of Shell-and-Tube Heat Exchangers -- 5.1. Introduction -- 5.2. Heat-Transfer Coefficients -- 5.3. Hydraulic Calculations -- 5.4. Finned Tubing -- 5.5. Tube-Count Tables -- 5.6. Factors Affecting Pressure Drop -- 5.7. Design Guidelines -- 5.8. Design Strategy -- 5.9.Computer Software -- 6. The Delaware Method -- 6.1. Introduction -- 6.2. Ideal Tube Bank Correlations -- 6.3. Shell-Side Heat-Transfer Coefficient -- 6.4. Shell-Side Pressure Drop -- 6.5. The Flow Areas -- 6.6. Correlations for the Correction Factors -- 6.7. Estimation of Clearances.

متن يادداشت

Contents note continued: 7. The Stream Analysis Method -- 7.1. Introduction -- 7.2. The Equivalent Hydraulic Network -- 7.3. The Hydraulic Equations -- 7.4. Shell-Side Pressure Drop -- 7.5. Shell-Side Heat-Transfer Coefficient -- 7.6. Temperature Profile Distortion -- 7.7. Good Design Practice -- 7.8. The Wills-Johnston Method -- 7.9.Computer Software -- 8. HEAT-Exchanger Networks -- 8.1. Introduction -- 8.2. An Example: TC3 -- 8.3. Design Targets -- 8.4. The Problem Table -- 8.5.Composite Curves -- 8.6. The Grand Composite Curve -- 8.7. Significance of the Pinch -- 8.8. Threshold Problems and Utility Pinches -- 8.9. Feasibility Criteria at the Pinch -- 8.10. Design Strategy -- 8.11. Minimum-Utility Design for TC3 -- 8.12.Network Simplification -- 8.13. Number of Shells -- 8.14. Targeting for Number of Shells -- 8.15. Area Targets -- 8.16. The Driving Force Plot -- 8.17. Super Targeting -- 8.18. Targeting by Linear Programming -- 8.19.Computer Software.

متن يادداشت

Contents note continued: 8.20.A Case Study: Gasoline Production from Bio-Ethanol -- 9. Boiling Heat Transfer -- 9.1. Introduction -- 9.2. Pool Boiling -- 9.3. Correlations for Nucleate Boiling on Horizontal Tubes -- 9.4. Two-Phase Flow -- 9.5. Convective Boiling in Tubes -- 9.6. Film Boiling -- 10. Reboilers -- 10.1. Introduction -- 10.2. Types of Reboilers -- 10.3. Design of Kettle Reboilers -- 10.4. Design of Horizontal Thermosyphon Reboilers -- 10.5. Design of Vertical Thermosyphon Reboilers -- 10.6.Computer Software -- 11. Condensers -- 11.1. Introduction -- 11.2. Condenser Geometries and Configurations -- 11.3. Condensation on a Vertical Surface: Nusselt Theory -- 11.4. Condensation on Horizontal Tubes -- 11.5. Modifications of Nusselt Theory -- 11.6. Condensation Inside Horizontal Tubes -- 11.7. Condensation on Finned Tubes -- 11.8. Pressure Drop -- 11.9. Mean Temperature Difference -- 11.10. Multi-Component Condensation -- 11.11.Computer Software -- 12. Air-Cooled Heat Exchangers.

متن يادداشت

Machine generated contents note: 1. Heat Conduction -- 1.1. Introduction -- 1.2. Fourier's Law of Heat Conduction -- 1.3. The Heat Conduction Equation -- 1.4. Thermal Resistance -- 1.5. The Conduction Shape Factor -- 1.6. Unsteady-State Conduction -- 1.7. Mechanisms of Heat Conduction -- 2. Convective and Radiative Heat Transfer -- 2.1. Introduction -- 2.2.Combined Conduction and Convection -- 2.3. Extended Surfaces -- 2.4. Forced Convection in Pipes and Ducts -- 2.5. Forced Convection in External Flow -- 2.6. Free Convection -- 2.7. Radiation -- 3. Heat Exchangers -- 3.1. Introduction -- 3.2. Double-Pipe Equipment -- 3.3. Shell-and-Tube Equipment -- 3.4. Plate Heat Exchangers -- 3.5. The Overall Heat-Transfer Coefficient -- 3.6. The LMTD Correction Factor -- 3.7. Analysis of Double-Pipe Exchangers -- 3.8. Preliminary Design of Shell-and-Tube Exchangers -- 3.9. Rating a Shell-and-Tube Exchanger -- 3.10. Heat-Exchanger Effectiveness -- 4. Design of Double-Pipe Heat Exchangers -- 4.1. Introduction.

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موضوع مستند نشده

Heat exchangers-- Design.

موضوع مستند نشده

Heat exchangers.

موضوع مستند نشده

Heat-- Transmission-- Computer programs.

موضوع مستند نشده

Heat-- Transmission.

مستند نام اشخاص تاييد نشده

Serth, R. W.

مستند نام اشخاص تاييد نشده

Lestina, Thomas G.

مستند نام تنالگان تاييد نشده

ScienceDirect (Online service).

تاريخ عمليات

20190124170503.0

نام الکترونيکي

نوع ماده

[Book]

تكميل شده

Y