Carbon dioxide capture and acid gas injection

✍ Scribed by Carroll, John J.; Wu, Ying; Zhu, Weiyao

• Publisher: Wiley
• Year: 2017
• Tongue: English
• Leaves: 256
• Series: Advances in natural gas engineering
• Category: Library

✦ Table of Contents

Content: 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 Review2.4 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
References
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
References
4 Sulfur Recovery in High Density CO2 Fluid
4.1 Introduction
4.2 Literature Review 4.3 Methodology4.4 Results and Discussion
4.5 Conclusion and Future Directions
References
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 Calculations5.4.7 Thermodynamic Modeling of CO2 Solubility
5.5 Conclusion
Acknowledgements
References
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 Section6.4.4 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
References
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)

✦ Subjects

Carbon dioxide mitigation;Greenhouse gas mitigation;Oil wells -- Gas lift;TECHNOLOGY & ENGINEERING / Power Resources / General