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Gas injection for disposal and enhanced recovery / edited by Ying Wu, John J. Carroll, Qi Li.

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Format:
Book
Contributor:
Wu, Ying (Petroleum engineer), editor.
Carroll, John J., 1958- editor.
Li, Qi (Geologist), editor.
Series:
Advances in natural gas engineering.
Advances in Natural Gas Engineering
Language:
English
Subjects (All):
Oil wells--Gas lift.
Oil wells.
Gas wells.
Carbon dioxide--Industrial applications.
Carbon dioxide.
Geological carbon sequestration.
Atmospheric carbon dioxide--Storage.
Atmospheric carbon dioxide.
Physical Description:
1 online resource (421 p.)
Edition:
1st ed.
Place of Publication:
Hoboken, New Jersey ; Salem, Massachusetts : Scrivener Publishing : Wiley, 2014.
Language Note:
English
Summary:
This is the fourth volume in a series of books focusing on natural gas engineering, focusing on two of the most important issues facing the industry today: disposal and enhanced recovery of natural gas. This volume includes information for both upstream and downstream operations, including chapters on shale, geological issues, chemical and thermodynamic models, and much more. Written by some of the most well-known and respected chemical and process engineers working with natural gas today, the chapters in this important volume represent the most cutting-edge and state-of-the-art processes
Contents:
Cover; Title Page; Copyright Page; Contents; Preface; Section 1: Data and Correlations; 1 Densities of Carbon Dioxide-Rich Mixtures Part I: Comparison with Pure CO2; 1.1 Introduction; 1.2 Density; 1.3 Literature Review; 1.3.1 CO2 + Methane; 1.3.2 CO2 + Nitrogen; 1.4 Calculations; 1.4.1 Kay's Rule; 1.4.2 Modified Kay's Rule; 1.4.3 Prausnitz-Gunn; 1.5 Discussion; 1.6 Conclusion; References; 2 Densities of Carbon Dioxide-Rich Mixtures Part II: Comparison with Thermodynamic Models; 2.1 Introduction; 2.2 Literature Review; 2.3 Calculations; 2.4 Lee Kesler; 2.5 Benedict-Webb- Rubin (BWR)
2.6 Peng-Robinson2.7 Soave-Redlich-Kwong; 2.8 AQUAlibrium; 2.9 Discussion; 2.10 Conclusion; References; 3 On Transferring New Constant Pressure Heat Capacity Computation Methods to Engineering Practice; 3.1 Introduction; 3.2 Materials and Methods; 3.3 Results and Discussion; 3.4 Conclusions; References; 4 Developing High Precision Heat Capacity Correlations for Solids, Liquids and Ideal Gases; 4.1 Introduction; 4.2 Databases and Methods; 4.3 Results and Discussion; 4.4 Conclusion; References; 5 Method for Generating Shale Gas Fluid Composition from Depleted Sample; 5.1 Introduction
5.2 Theory of Chemical Equilibrium Applied to Reservoir Fluids5.3 Reservoir Fluid Composition from a Non-Representative Sample; 5.3.1 Depleted Gas Condensate Samples; 5.3.2 Samples from Tight Reservoirs; 5.4 Numerical Examples; 5.4.1 Depleted Gas Condensate Samples; 5.4.2 Samples from Tight Reservoirs; 5.5 Discussion of the Results; 5.6 Conclusions; 5.7 Nomenclature; Greek letters; Sub and super indices; References; 6 Phase Equilibrium in the Systems Hydrogen Sulfide + Methanol and Carbon Dioxide + Methanol; 6.1 Introduction; 6.2 Literature Review; 6.2.1 Hydrogen Sulfide + Methanol
6.2.2 Carbon Dioxide + Methanol6.3 Modelling With Equations Of State; 6.4 Nomenclature; Greek; References; 7 Vapour-Liquid Equilibrium, Viscosity and Interfacial Tension Modelling of Aqueous Solutions of Ethylene Glycol or Triethylene Glycol in the Presence of Methane, Carbon Dioxide and Hydrogen Sulfide; 7.1 Introduction; 7.2 Results and Discussion; 7.2.1 Experimental; 7.2.2 Vapour Liquid Equilibrium and Phase Density Modeling; 7.2.3 Liquid-Phase Viscosity Modeling; 7.2.4 Interfacial Tension Modeling; 7.2.5 Commercial Software Comparison; 7.3 Conclusions; 7.4 Nomenclature
7.5 AcknowledgementReferences; Appendix 7.A; Section 2: Process Engineering; 8 Enhanced Gas Dehydration using Methanol Injection in an Acid Gas Compression System; 8.1 Introduction; 8.2 Methodology; 8.2.1 Modeling Software; 8.2.2 Simulation Setup; 8.3 CASE I: 100 % CO2; 8.3.1 How Much to Dehydrate; 8.3.2 Dehydration using Air Coolers; 8.3.3 Methanol injection for hydrate suppression; 8.3.4 Methanol Injection for Achieving 2:1 Water Content; 8.3.5 DexProTM for Achieving 2:1 Water Content; 8.4 CASE II: 50 Percent CO2, 50 Percent H2S; 8.4.1- How Much to Dehydrate?
8.4.2 Dehydration using Air Coolers
Notes:
Description based upon print version of record.
Includes bibliographical references and index.
Description based on print version record.
ISBN:
9781118938577
1118938577
9781118938607
1118938607
9781118938584
1118938585
OCLC:
888351220

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