http://www.loc.gov/mods/v3 http://www.loc.gov/standards/mods/v3/mods-3-2.xsd
Design of gas-handling systems and facilities
1 online resource (685 pages) : illustrations
Updated and better than ever, Design of Gas-Handling Systems and Facilities, 3rd Edition includes greatly expanded chapters on gas-liquid separation, gas sweetening, gas liquefaction, and gas dehydration -information necessary and critical to production and process engineers and designers. Natural gas is at the forefront of today''s energy needs, and this book walks you through the equipment and processes used in gas-handling operations, including conditioning and processing, to help you effectively design and manage your gas production facility. Taking a logical approach from theory.
Front Cover; Surface Production Operations: Design of Gas-Handling Systems and Facilities ; Copyright ; Contents ; Preface; Acknowledgments; Chapter One: Overview of Gas-Handling, Conditioning, and Processing Facilities; 1.1. Heating; 1.2. Separation; 1.3. Cooling; 1.4. Stabilization; 1.5. Compression; 1.6. Gas Treating; 1.7. Gas Dehydration; 1.8. Gas Processing; Chapter Two: Basic Principles; 2.1. Introduction; 2.2. Fluid Analysis; 2.3. Physical Properties; 2.3.1. Equations of State; 2.3.2. Molecular Weight and Apparent Molecular Weight; 2.3.3. Gas Specific Gravity.
2.3.4. Nonideal Gas Equations of State2.3.5. Liquid Density and Specific Gravity; 2.3.6. Liquid Volume; 2.3.7. Viscosity; 2.4. Flash Calculations; 2.4.1. Determine Gas and Liquid Compositions; 2.5. Characterizing the Flow Stream; 2.6. Use of Computer Programs for Flash Calculations; 2.7. Approximate Flash Calculations; 2.8. Other Properties; 2.9. Phase Equilibrium; Chapter Three: Heat Transfer Theory; 3.1. Objectives; 3.2. What Is a Heat Exchanger?; 3.2.1. Commonly Used Types of Heat Exchangers; Shell-and-Tube; Plate-and-Frame; Plate-Fin; Air-Cooled; 3.2.2. Heat Exchangers-The Bad News.
3.2.3. General Considerations3.2.4. Company Engineering Standards and Specifications; 3.2.5. Tube Vibration and Tube Rupture; 3.2.6. Acoustic Resonance and Vibration; 3.3. Process Specification; 3.3.1. Process Specification Sheet; 3.3.2. Design Data Sheet; 3.3.3. Required Physical/Thermal Properties; 3.4. Pressure Drop Considerations; 3.4.1. Key Parameter for Design and Troubleshooting; Tube side; Shell side; Other ways; Typical Pressure gradients (DeltaP/L); Flow path lengths, ft or m (L); 3.5. Basic Heat Transfer Theory; 3.5.1. Heat Transfer Mechanisms; 3.5.2. Basic Equations.
3.5.3. Flow of Heat3.5.4. Multiple Transfer Mechanisms; 3.6. Determination of Mean Temperature Difference; 3.6.1. Mean Temperature Difference; 3.6.2. Log Mean Temperature Difference; 3.6.3. Nonconstant "U" ; 3.6.4. Different Flow Arrangements; 3.6.5. Nonlinear Temperature Profile; 3.7. Selection of Temperature Approach (T2); 3.8. Determination of Heat Transfer Coefficient; 3.8.1. Overview; 3.8.2. Area Basis; 3.8.3. Heat Transfer Coefficient-Clean Tube; 3.8.4. Heat Transfer Coefficient-Fouled Tube; 3.8.4.1. Fouling Factors; 3.8.4.2. Fouling Considerations; 3.8.4.3. Fouling Mechanisms.
3.8.5. Evaluating Performance3.8.6. Heat Transfer Research Inc. Computer Simulation Programs; 3.9. Calculation of Film Coefficients; 3.9.1. Inside Film Coefficient; 3.9.2. Mass Velocity of a Fluid; 3.9.3. Outside Film Coefficient in a Liquid Bath; 3.9.4. Outside Film Coefficient for Shell-and-Tube Exchangers; 3.10. Tube Metal Resistance; 3.11. Approximate Overall Heat Transfer Coefficients; 3.12. Determination of Process Heat Duty; 3.12.1. Overview; 3.12.2. Sensible Heat; 3.12.3. Latent Heat; 3.12.4. Heat Duty for Multiphase Streams; 3.12.5. Natural Gas Sensible Heat Duty at Constant Pressure.
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Includes bibliographical references at the end of each chapters and index.
Surface Production Operations ; Volume 2
Waltham, Massachusetts ; Oxford, England : Elsevier, ©2014