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Carbon dioxide capture and acid gas injection / edited by Ying Wu, John J. Carroll, and Weiyao Zhu.
- Format:
- Book
- Series:
- Advances in natural gas engineering.
- Advances in Natural Gas Engineering
- Language:
- English
- Subjects (All):
- Carbon dioxide mitigation.
- Oil wells--Gas lift.
- Oil wells.
- Physical Description:
- 1 online resource (265 pages) : illustrations.
- Edition:
- 1st ed.
- Place of Publication:
- Hoboken, New Jersey : Scrivener Publishing : Wiley, 2017.
- Summary:
- This is the sixth volume in a series of books on natural gas engineering, focusing carbon dioxide (CO2) capture and acid gas injection. This volume includes information for both upstream and downstream operations, including chapters on well modeling, carbon capture, 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 and operations being used in the field. Not available anywhere else, this volume is a must-have for any chemical engineer, chemist, or process engineer working with natural gas. There are updates of new technologies in other related areas of natural gas, in addition to the CO2 capture and acid gas injection, including testing, reservoir simulations, and natural gas hydrate formations. Advances in Natural Gas Engineering is an ongoing series of books meant to form the basis for the working library of any engineer working in natural gas today. Every volume is a must-have for any engineer or library.
- Contents:
- Cover
- Title Page
- Copyright Page
- Contents
- Preface
- 1 Enthalpies of Carbon Dioxide-Methane and Carbon Dioxide-Nitrogen Mixtures: Comparison with Thermodynamic Models
- 1.1 Introduction
- 1.2 Enthalpy
- 1.3 Literature Review
- 1.3.1 Carbon Dioxide-Methane
- 1.3.2 Carbon Dioxide-Nitrogen
- 1.4 Calculations
- 1.4.1 Benedict-Webb-Rubin
- 1.4.2 Lee-Kesler
- 1.4.3 Soave-Redlich-Kwong
- 1.4.4 Peng-Robinson
- 1.4.5 AQUAlibrium
- 1.5 Discussion
- 1.6 Conclusion
- References
- 2 Enthalpies of Hydrogen Sulfide-Methane Mixture: Comparison with Thermodynamic Models
- 2.1 Introduction
- 2.2 Enthalpy
- 2.3 Literature Review
- 2.4 Calculations
- 2.4.1 Lee-Kesler
- 2.4.2 Benedict-Webb-Rubin
- 2.4.3 Soave-Redlich-Kwong
- 2.4.4 Redlich-Kwong
- 2.4.5 Peng-Robinson
- 2.4.6 AQUAlibrium
- 2.5 Discussion
- 2.6 Conclusion
- 3 Phase Behavior and Reaction Thermodynamics Involving Dense-Phase CO2 Impurities
- 3.1 Introduction
- 3.2 Experimental
- 3.3 Results and Discussion
- 3.3.1 Phase Behavior Studies of SO2 Dissolved in Dense CO2 Fluid
- 3.3.2 The Densimetric Properties of CS2 and CO2 Mixtures
- 4 Sulfur Recovery in High Density CO2 Fluid
- 4.1 Introduction
- 4.2 Literature Review
- 4.3 Methodology
- 4.4 Results and Discussion
- 4.5 Conclusion and Future Directions
- 5 Carbon Capture Performance of Seven Novel Immidazolium and Pyridinium Based Ionic Liquids
- 5.1 Introduction
- 5.2 Experimental Work
- 5.2.1 Materials
- 5.2.2 Density Measurement
- 5.2.3 Solubility Measurement
- 5.3 Modeling
- 5.3.1 Calculation of Henry's Law Constants
- 5.3.2 Critical Properties Calculations
- 5.3.3 Peng Robinson EoS
- 5.4 Results and Discussion
- 5.4.1 Density
- 5.4.2 Critical Properties
- 5.4.3 CO2 Solubility
- 5.4.4 The Effect of Changing the Cation.
- 5.4.5 The Effect of Changing the Anion
- 5.4.6 Henry's Law Constant, Enthalpy and Entropy Calculations
- 5.4.7 Thermodynamic Modeling of CO2 Solubility
- 5.5 Conclusion
- Acknowledgements
- 6 Vitrisol® a 100% Selective Process for H2S Removal in the Presence of CO2
- 6.1 Introduction
- 6.2 Case Definition
- 6.3 "Amine-Treated" Cases by PPS
- 6.3.1 Introduction to PPS
- 6.3.2 Process Description
- 6.3.3 PFD
- 6.3.4 Results
- 6.3.4.1 Case 1
- 6.3.4.2 Case 2
- 6.4 Vitrisol® Process Extended with Regeneration of Active Component
- 6.4.1 Technology Description
- 6.4.2 Parameters Determining the Process Boundary Conditions
- 6.4.3 Absorption Section
- 6.4.4 Regeneration Section
- 6.4.5 Sulphur Recovery Section
- 6.4.6 CO2-Absorber
- 6.4.7 PFD
- 6.5 Results
- 6.6 Discussion
- 6.6.1 Comparison of Amine Treating Solutions to Vitrisol®
- 6.6.2 Enhanced H2S Removal of Barnett Shale Gas (case 2)
- 6.7 Conclusions
- 6.8 Notation
- Appendix 6-A: H&
- M Balance of Case 1 (British Columbia shale) of the Amine Process
- Appendix 6-B H&
- M Balance of Case 2a (Barnett shale) of the Amine Process with Stripper Promoter
- Appendix 6-C H&
- M Balance of Case 3 (Barnett shale) of the Amine Process (MEA)
- Appendix 6-D: H&
- M Balance of Case 1 (British Columbia shale) of the Vitrisol® process
- Appendix 6-E H&
- M Balance of Case 2 (Barnett shale) of the Vitrisol® Process
- 7 New Amine Based Solvents for Acid Gas Removal
- 7.1 Introduction
- 7.2 Chemicals and Materials
- 7.3 Liquid-Liquid Equilibria
- 7.3.1 LLE in {methylpiperidines - H2O} and {methylpiperidines - H2O - CO2}
- 7.3.2 Liquid-Liquid Equilibria of Ternary Systems {Amine - H2O - Glycol}
- 7.3.3 Liquid-Liquid Equilibria of the Quaternary Systems {CO2 - NMPD - TEG - H2O}.
- 7.4 Densities and Heat Capacities of Ternary Systems {NMPD - H2O - Glycol}
- 7.4.1 Densities
- 7.4.2 Specific Heat Capacities
- 7.5 Vapor-Liquid Equilibria of Ternary Systems {NMPD - TEG - H2O - CO2}
- 7.6 Enthalpies of Solution
- 7.7 Discussion and Conclusion
- Acknowledgments
- 8 Improved Solvents for CO2 Capture by Molecular Simulation Methodology
- 8.1 Introduction
- 8.2 Physical and Chemical Models
- 8.3 Molecular-Level Models and Algorithms for Thermodynamic Property Predictions
- 8.4 Molecular-Level Models and Methodology for MEA-H2O-CO2
- 8.4.1 Extensions to Other Alkanolamine Solvents and Their Mixtures
- 9 Strategies for Minimizing Hydrocarbon Contamination in Amine Acid Gas for Reinjection
- 9.1 Introduction
- 9.2 Amine Sweetening Process
- 9.3 Hydrocarbons in Amine
- 9.4 Effect of Hydrocarbons on the Acid Gas Reinjection System
- 9.5 Effect of Hydrocarbons on the Amine Plant
- 9.6 Minimizing Hydrocarbon Content in Amine Acid Gas
- 9.6.1 Option 1. Optimization of the Amine Plant Operation
- 9.6.2 Option 2. Amine Flash Tanks
- 9.6.3 Option 3. Rich Amine Liquid Coalescers
- 9.6.4 Option 4. Use of Skimming Devices
- 9.6.5 Option 5. Technological Solutions
- 10 Modeling of Transient Pressure Response for CO2 Flooding Process by Incorporating Convection and Diffusion Driven Mass Transfer
- 10.1 Introduction
- 10.2 Model Development
- 10.2.1 Pressure Diffusion
- 10.2.2 Mass Transfer
- 10.2.3 Solutions
- 10.3 Results and Discussion
- 10.3.1 Flow Regimes
- 10.3.2 Effect of Mass Transfer
- 10.3.3 Sensitivity Analysis
- 10.3.3.1 CO2 Bank
- 10.3.3.2 Reservoir Outer Boundary
- 10.4 Conclusions
- 11 Well Modeling Aspects of CO2 Sequestration
- 11.1 Introduction
- 11.2 Delivery Conditions.
- 11.3 Reservoir and Completion Data
- 11.4 Inflow Performance Relationship (IPR) and Injectivity Index
- 11.5 Equation of State (EOS)
- 11.6 Vertical Flow Performance (VFP) Curves
- 11.7 Impact of the Well Deviation on CO2 Injection
- 11.8 Implication of Bottom Hole Temperature (BHT) on Reservoir
- 11.9 Impact of CO2 Phase Change
- 11.10 Injection Rates, Facility Design Constraints and Number of Wells Required
- 11.11 Wellhead Temperature Effect on VFP Curves
- 11.12 Effect of Impurities in CO2 on VFP Curves
- 11.13 Concluding Remarks
- Conversion Factors
- 12 Effects of Acid Gas Reinjection on Enhanced Natural Gas Recovery and Carbon Dioxide Geological Storage: Investigation of the Right Bank of the Amu Darya River
- 12.1 Introduction
- 12.2 The Amu Darya Right Bank Gas Reservoirs in Turkmenistan
- 12.3 Model Development
- 12.3.1 State equation
- 12.3.1.1 Introduction of Traditional PR State Equation
- 12.3.1.2 Modifications for the Vapor-Aqueous System
- 12.3.2 Salinity
- 12.3.3 Diffusion
- 12.3.3.1 Diffusion Coefficients
- 12.3.3.2 The Cross-Phase Diffusion Coefficients
- 12.4 Simulation Model
- 12.4.1 Model Parameters
- 12.4.2 Grid-Sensitive Research of the Model
- 12.4.3 The Development and Exploitation Mode
- 12.5 Results and Discussion
- 12.5.1 Reservoir Pressure
- 12.5.2 Gas Sequestration
- 12.5.3 Production
- 12.5.4 Recovery Ratio and Recovery Percentage
- 12.6 Conclusions
- 12.7 Acknowledgments
- Index
- EULA.
- Notes:
- Includes bibliographical references at the end of each chapters and index.
- Description based on print version record.
- ISBN:
- 9781118938676
- 1118938674
- 9781118938683
- 1118938682
- 9781118938706
- 1118938704
- OCLC:
- 983797061
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