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Cutting-edge technology for carbon capture, utilization, and storage / Karine Ballerat-Busserolles, Ying (Alice) Wu and John J. Carroll.

Ebook Central Academic Complete Available online

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Format:
Book
Conference/Event
Author/Creator:
Ballerat-Busserolles, Karine, author.
Wu, Ying (Petroleum engineer), author.
Carroll, John J., author.
Conference Name:
Cutting-Edge Technology for Carbon Capture, Utilization, and Storage (Conference) (2017 : Clermont-Ferrand, France)
Language:
English
Subjects (All):
Carbon sequestration--Technological innovations.
Carbon sequestration.
Physical Description:
1 online resource (366 pages)
Edition:
1st ed.
Place of Publication:
Beverly, MA : Scrivener Publishing ; Hoboken, NJ : Wiley, [2018]
Summary:
Compiled from a conference on this important subject by three of the most well-known and respected editors in the industry, this volume provides some of the latest technologies related to carbon capture, utilization and, storage (CCUS). Of the 36 billon tons of carbon dioxide (CO2) being emitted into Earth's atmosphere every year, only 40 million tons are able to be captured and stored. This is just a fraction of what needs to be captured, if this technology is going to make any headway in the global march toward reversing, or at least reducing, climate change. CO2 capture and storage has long been touted as one of the leading technologies for reducing global carbon emissions, and, even though it is being used effectively now, it is still an emerging technology that is constantly changing. This volume, a collection of papers presented during the Cutting-Edge Technology for Carbon Capture, Utilization, and Storage (CETCCUS), held in Clermont-Ferrand, France in the fall of 2017, is dedicated to these technologies that surround CO2 capture. Written by some of the most well-known engineers and scientists in the world on this topic, the editors, also globally known, have chosen the most important and cutting-edge papers that address these issues to present in this groundbreaking new volume, which follows their industry-leading series, Advances in Natural Gas Engineering, a seven-volume series also available from Wiley-Scrivener. With the ratification of the Paris Agreement, many countries are now committing to making real progress toward reducing carbon emissions, and this technology is, as has been discussed for years, one of the most important technologies for doing that. This volume is a must-have for any engineer or scientist working in this field.
Contents:
Cover
Title Page
Copyright Page
Contents
Preface
Introduction
Part I: Carbon Capture and Storage
1 Carbon Capture Storage Monitoring ("CCSM")
1.1 Introduction
1.2 State of the Art Practice
1.3 Marmot's CCSM Technology
1.4 Principles of Information Analysis
1.5 Operating Method
1.6 Instrumentation and Set up
Abbreviations
References
2 Key Technologies of Carbon Dioxide Flooding and Storage in China
2.1 Background
2.2 Key Technologies of Carbon dioxide Flooding and Storage
2.2.1 CO2 Miscible Flooding Theory in Continental Sedimentary Reservoirs
2.2.2 The Storage Mechanism of CO2 in Reservoirs and Salt Water Layers
2.2.3 Reservoir Engineering Technology of CO2 Flooding and Storage
2.2.4 High Efficiency Technology of Injection and Production for CO2 Flooding
2.2.5 CO2 Long-Distance Pipeline Transportation and Supercritical Injection Technology
2.2.6 Fluid Treatment and Circulating Gas Injection Technology of CO2 Flooding
2.2.7 Reservoir Monitoring and Dynamic Analysis and Evaluation Technology of CO2 Flooding
2.3 Existing Problems and Technical Development Direction
2.3.1 The Vital Communal Troubles &amp
Challenges
2.3.2 Further Orientation of Technology Development
3 Mapping CCUS Technological Trajectories and Business Models: The Case of CO2-Dissolved
3.1 Introduction
3.2 CCS and Roadmaps: From Expectations to Reality ...
3.3 CCS Project Portfolio: Between Diversity and Replication
3.3.1 Demonstration Process: Between Diversity and Replication
3.3.2 Diversity of the Current Project Portfolio
3.4 Going Beyond EOR: Other Business Models for Storage?
3.4.1 The EOR Legacy
3.4.2 From EOR to a CCS Wide-Scale Deployment
3.5 Coupling CCS and Geothermal Energy: Lessons from the CO2-DISSOLVED Project Study
3.5.1 CO2-DISSOLVED Concept.
3.5.2 Techno-Economic Analysis of CO2-DISSOLVED
3.5.3 Business Models and the Replication/Diversity Dilemma
3.6 Conclusion
Acknowledgements
4 Feasibility of Ex-Situ Dissolution for Carbon Dioxide Sequestration
4.1 Introduction
4.2 Methods to Accelerate Dissolution
4.2.1 In-situ
4.2.2 Ex-situ
4.3 Discussion and Conclusions
Acknowledgments
Part II: EOR
5 CO2 Gas Injection as an EOR Technique - Phase Behavior Considerations
5.1 Introduction
5.2 Features of CO2
5.3 Miscible CO2 Drive
5.4 Immiscible CO2 Drives and Density Effects
5.5 Asphaltene Precipitation Caused by Gas Injection
5.6 Gas Revaporization as EOR Technique
5.7 Conclusions
List of Symbols
Appendix A Reservoir Fluid Compositions and Key Property Data
6 Study on Storage Mechanisms in CO2 Flooding for Water-Flooded Abandoned Reservoirs
6.1 Introduction
6.2 CO2 Solubility in Coexistence of Crude Oil and Brine
6.3 Mineral Dissolution Effect
6.4 Relative Permeability Hysteresis
6.5 Effect of CO2 Storage Mechanisms on CO2 Flooding
6.6 Conclusions
7 The Investigation on the Key Hydrocarbons of Crude Oil Swelling via Supercritical CO2
7.1 Introduction
7.2 Hydrocarbon Selection
7.3 Experiment Section
7.3.1 Principle
7.3.2 Apparatus and Samples
7.3.3 Experimental Scheme Design
7.3.4 Procedures
7.4 Results and Discussion
7.4.1 Results and Data Processing
7.4.2 Volume Swelling Influenced by the Hydrocarbon Property
7.4.3 A New Parameter of Molar Density for Evaluating Hydrocarbon Volume Swelling
7.4.4 Advantageous Hydrocarbons
7.5 Conclusions
Nomenclature
8 Pore-Scale Mechanisms of Enhanced Oil Recovery by CO2 Injection in Low-Permeability Heterogeneous Reservoir
8.1 Introduction.
8.2 Experimental Device and Samples
8.3 Experimental Procedure
8.3.1 Experimental Results
8.4 Quantitative Analysis of Oil Recovery in Different Scale Pores
8.5 Conclusions
Part III: Data - Experimental and Correlation
9 Experimental Measurement of CO2 Solubility in a 1 mol/kgw CaCl2 Solution at Temperature from 323.15 to 423.15 K and Pressure up to 20 MPa
9.1 Introduction
9.2 Literature Review
9.3 Experimental Section
9.3.1 Chemicals
9.3.2 Apparatus
9.3.3 Operating Procedure
9.3.4 Analysis
9.4 Results and Discussion
9.5 Conclusion
10 Determination of Dry-Ice Formation during the Depressurization of a CO2 Re-Injection System
10.1 Introduction
10.2 Thermodynamics
10.3 Case Study
10.3.1 System Description
10.3.2 Objectives
10.3.3 Scenarios
10.3.4 Simulation Runs Conclusions
10.4 Conclusions
11 Phase Equilibrium Properties Aspects of CO2 and Acid Gases Transportation
11.1 Introduction
11.1.1 State of the Art and Phase Diagrams
11.2 Experimental Work and Description of Experimental Setup
11.3 Models and Correlation Useful for the Determination of Equilibrium Properties
11.4 Presentation of Some Results
11.5 Conclusion
12 Thermodynamic Aspects for Acid Gas Removal from Natural Gas
12.1 Introduction
12.2 Thermodynamic Models
12.3 Results and Discussion
12.3.1 Hydrocarbons and Mercaptans Solubilities in Aqueous Alkanolamine Solution
12.3.2 Acid Gases (CO2/H2S) Solubilities in Aqueous Alkanolamine Solution
12.3.3 Multi-component Systems Containing CO2-H2SAlkanolamine-Water-Methane-Mercaptan
12.4 Conclusion and Perspectives
13 Speed of Sound Measurements for a CO2 Rich Mixture
13.1 Experimental Section.
13.1.1 Material
13.1.2 Experimental Setup
13.2 Results and Discussion
13.3 Conclusion
14 Mutual Solubility of Water and Natural Gas with Different CO2 Content
14.1 Introduction
14.2 Experimental
14.2.1 Materials
14.2.2 Experimental Apparatus
14.2.3 Experimental Procedures
14.3 Thermodynamic Model
14.3.1 The Cubic-Plus-Association Equation of State
14.3.2 Parameterization of the Model
14.4 Results and Discussion
14.4.1 Phase Behavior of CO2-Water
14.4.2 The Mutual Solubility of Water-Natural Gas
14.5 Conclusion
Acknowledgement
15 Effect of SO2 Traces on Metal Mobilization in CCS
15.1 Introduction
15.2 Experimental
15.2.1 Sample Preparation
15.2.1.1 Sandstone
15.2.1.2 Brine
15.2.2 Experimental Set-up
15.2.3 Experimental Methodology
15.3 Results and Discussion
15.3.1 Major Components
15.3.2 Trace Metals
15.3.2.1 Strontium
15.3.2.2 Manganese
15.3.2.3 Copper
15.3.2.4 Zinc
15.3.2.5 Vanadium
15.3.2.6 Lead
15.3.3 Metal Mobilization
15.4 Conclusions
16 Experiments and Modeling for CO2 Capture Processes Understanding
16.1 Introduction
16.2 Chemicals and Materials
16.3 Vapor-Liquid Equilibria
16.3.1 Experimental VLE of Pure Amine
16.3.2 Experimental VLE of {Amine - H2O} System
16.3.3 Modeling VLE
16.4 Speciation at Equilibrium
16.4.1 Equilibrium Measurements 1H and 13C NMR
16.4.2 Modeling of Species Concentration
Acknowledgment
Part IV: Molecular Simulation
17 Kinetic Monte Carlo Molecular Simulation of Chemical Reaction Equilibria
18 Molecular Simulation Study on the Diffusion Mechanism of Fluid in Nanopores of Illite in Shale Gas Reservoir
18.1 Introduction
18.2 Models and Simulation Details.
18.2.1 Models and Simulation Parameters
18.2.2 Data Processing and Computing Methods
18.3 Results and Discussion
18.3.1 Variation Law of Self Diffusion Coefficient
18.3.2 Density Distribution
18.3.3 Radial Distribution Function
18.4 Conclusions
19 Molecular Simulation of Reactive Absorption of CO2 in Aqueous Alkanolamine Solutions
Part V: Processes
20 CO2 Capture from Natural Gas in LNG Production. Comparison of Low-Temperature Purification Processes and Conventional Amine Scrubbing
20.1 Introduction
20.2 Description of Process Solutions
20.2.1 The Ryan-Holmes Process
20.2.2 The Dual Pressure Low-Temperature Distillation Process
20.2.3 The Chemical Absorption Process
20.3 Methods
20.4 Results and Discussion
20.5 Conclusions
Symbols
Subscripts
Superscripts
Greek Symbols
21 CO2 Capture Using Deep Eutectic Solvent and Amine (MEA) Solution
21.1 Experimental Section
21.2 Results and Discussion
21.2.1 Validation of the Experimental Method
21.2.2 Solubility of CO2 in the Solvent DES/MEA
21.2.3 Solubility of CO2 - Comparison Between DES + MEA and DES Solvent
21.2.4 Solubility of CO2 - Comparison Between (DES + MEA) and (H2O + MEA) Solvent
21.5 Conclusion
22 The Impact of Thermodynamic Model Accuracy on Sizing and Operating CCS Purification and Compression Units
22.1 Introduction
22.2 Thermodynamic Systems in CCUS Technologies
22.2.1 Compositional Characteristics of CO2 Captured Flows
22.2.2 Post-Combustion
22.2.3 Oxy-Fuel Combustion
22.2.4 Pre-Combustion
22.3 Operating Conditions of Purification and Compression Units
22.4 Quality Specifications of CO2 Capture Flows
22.5 Cubic Equations of State for CCUS Fluids.
22.6 Influence of EoS Accuracy on Purification and Compression Processes.
Notes:
Includes index.
Description based on print version record.
ISBN:
9781119363729
1119363721
9781119363804
1119363802
9781119363767
1119363764
OCLC:
1031998836

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