Engineering Solutions for CO2 Conversion

Engineering Solutions for CO2 Conversion
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A comprehensive guide that offers a review of the current technologies that tackle CO2 emissions <br> <br> The race to reduce CO2 emissions continues to be an urgent global challenge. «Engineering Solutions for CO2 Conversion» offers a thorough guide to the most current technologies designed to mitigate CO2 emissions ranging from CO2 capture to CO2 utilization approaches. With contributions from an international panel representing a wide range of expertise, this book contains a multidisciplinary toolkit that covers the myriad aspects of CO2 conversion strategies. Comprehensive in scope, it explores the chemical, physical, engineering and economical facets of CO2 conversion. <br> «Engineering Solutions for CO2 Conversion» explores a broad range of topics including linking CFD and process simulations, membranes technologies for efficient CO2 capture-conversion, biogas sweetening technologies, plasma-assisted conversion of CO2, and much more. <br> <br> This important resource: <br> <br> * Addresses a pressing concern of global environmental damage, caused by the greenhouse gases emissions from fossil fuels<br> * Contains a review of the most current developments on the various aspects of CO2 capture and utilization strategies <br> * Incldues information on chemical, physical, engineering and economical facets of CO2 capture and utilization <br> * Offers in-depth insight into materials design, processing characterization, and computer modeling with respect to CO2 capture and conversion <br> <br> Written for catalytic chemists, electrochemists, process engineers, chemical engineers, chemists in industry, photochemists, environmental chemists, theoretical chemists, environmental officers, «Engineering Solutions for CO2 Conversion» provides the most current and expert information on the many aspects and challenges of CO2 conversion.

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Группа авторов. Engineering Solutions for CO2 Conversion

Table of Contents

List of Tables

List of Illustrations

Guide

Pages

Engineering Solutions for CO2 Conversion

1 CO2 Capture – A Brief Review of Technologies and Its Integration

1.1 Introduction: The Role of Carbon Capture

1.2 CO2 Capture Technologies. 1.2.1 Status of CO2 Capture Deployment

1.2.2 Pre‐combustion

1.2.3 Oxyfuel

1.2.4 Post‐combustion

1.2.4.1 Adsorption

1.2.4.2 High‐Temperature Solids Looping Technologies

1.2.4.3 Membranes

1.2.4.4 Chemical Absorption

1.2.4.4.1 Advances on Process Configurations

1.2.5 Others CO2 Capture/Separation Technologies

1.2.5.1 Fuel Cells

1.2.5.1.1 Solid Oxide Fuel Cells (SOFCs)

1.2.5.1.2 Molten Carbonate Fuel Cells (MCFCs)

1.3 Integration of Post‐combustion CO2 Capture in the Power Plant and Electricity Grid

1.3.1 Integration of the Capture Unit in the Thermal Power Plant

1.3.2 Flexible Operation of Thermal Power Plants in Future Energy Systems

1.4 CO2 Capture in the Industrial Sector

1.5 Conclusions

References

Notes

2 Advancing CCSU Technologies with Computational Fluid Dynamics (CFD): A Look at the Future by Linking CFD and Process Simulations

2.1 Sweep Across the General Simulation Techniques Available

2.2 Multi‐scale Approach for CFD Simulation of Amine Scrubbers

2.3 Eulerian, Eulerian–Lagrangian, and Discrete Element Methods for the Simulation of Calcium Looping, Mineral Carbonation, and Adsorption in Other Solid Particulate Materials

2.4 CFD for Oxy‐fuel Combustion Technologies: The Application of Single‐Phase Reactive Flows and Particle Tracking Algorithms

2.5 CFD for Carbon Storage and Enhanced Oil Recovery (EOR): The Link Between Advanced Imaging Techniques and CFD

2.6 CFD for Carbon Utilization with Chemical Conversion: The Importance of Numerical Techniques on the Study of New Catalysts

2.7 CFD for Biological Utilization: Microalgae Cultivation

2.8 What Does the Future Hold?

References

3 Membranes Technologies for Efficient CO2 Capture–Conversion

3.1 Introduction

3.2 Polymer Membranes

3.3 Oxygen Transport Membranes for CO2 Valorization

3.3.1 Oxygen Transport Membrane Fundamentals

3.3.2 Application Concepts of OTMs for Carbon Capture and Storage (CCS)

3.3.3 Existing Developments

3.4 Protonic Membranes

3.4.1 Proton Defects in Oxide Ceramics

3.4.2 Proton Transport Membrane Fundamentals

3.4.3 Application Concepts of Proton Conducting Membranes

3.5 Membranes for Electrochemical Applications

3.5.1 Electrolysis and Co‐electrolysis Processes

3.5.1.1 Water Electrolysis

3.5.1.2 CO2 Co‐electrolysis

3.5.2 Synthesis Gas Chemistry

Power to methane

Power to methanol

3.5.3 Other Applications. 3.5.3.1 Methane Steam Reforming

3.5.3.2 Methane Dehydroaromatization

3.6 Conclusions and Final Remarks

References

4 Computational Modeling of Carbon Dioxide Catalytic Conversion

4.1 Introduction

4.2 General Methods for Theoretical Catalysis Research

4.3 Characterizing the Catalyst and Its Interaction with CO2 Using DFT Calculations

4.4 Microkinetic Modeling in Heterogeneous Catalysis

4.5 New Trends: High‐Throughput Screening, Volcano Plots, and Machine Learning. 4.5.1 High‐Throughput Screening

4.5.2 Volcano Plots and Scaling Relations

4.5.3 DFT and Machine Learning

4.5.3.1 Machine‐Learned Potentials

4.5.3.2 Descriptors to Predict Catalytic Properties

4.5.3.3 Future Challenges in HT‐DFT Applied to Catalysis

References

5 An Overview of the Transition to a Carbon‐Neutral Steel Industry

5.1 Introduction

5.2 Global Relevance of the Steel Industry

5.2.1 Features that Make Steel a Special Material

5.3 Current Trends in Emission Policies in the World's Leading Countries in Steel Industry

5.4 Transition to a Carbon‐Neutral Production. A Big Challenge for the Steel Industry

5.4.1 Urea

5.4.2 Methanol and Formic Acid

5.4.3 Carbon Monoxide

5.4.4 Methane

5.5 CO2 Methanation: An Interesting Opportunity for the Valorization of the Steel Industry Emissions

5.6 Relevant Projects Already Launched for the Valorization of the CO2 Emitted by the Steel Industry

5.7 Concluding Remarks

References

6 Potential Processes for Simultaneous Biogas Upgrading and Carbon Dioxide Utilization

6.1 Introduction

6.2 Overview of Biogas General Characteristics and Upgrading Technologies to Bio‐methane Production. 6.2.1 Biogas Composition and Applications

6.2.2 Biogas Upgrading Processes

6.2.2.1 Water Scrubbing

6.2.2.2 Pressure Swing Adsorption

6.2.2.3 Chemical Scrubbing

6.2.2.4 Organic Physical Scrubbing

6.2.2.5 Membrane Separation

6.2.2.6 Cryogenic Separation

6.3 CCU Main Technologies

6.3.1 Supercritical CO2 as a Solvent

6.3.2 Chemicals from CO2

6.3.3 Mineral Carbonation

6.3.4 Fuels from CO2

6.3.5 Algae Production

6.3.6 Enhanced Oil Recovery (EOR)

6.4 Potential Processes for Biogas Upgrading and Carbon Utilization

6.4.1 Chemical Scrubbing Coupled with CCU

6.4.2 Membrane Separation Coupled with CCU

6.4.3 Cryogenic Separation Coupled with CCU

6.5 Conclusions

References

7 Biogas Sweetening Technologies

7.1 Introduction

7.2 Biogas Purification Technologies

7.2.1 Removal of Water Vapor (H2O(g))

7.2.2 Removal of Hydrogen Sulfide (H2S) and Other Sulfur‐Containing Compounds

7.2.2.1 In Situ Precipitation of H2S Through Air/Oxygen Injection

7.2.2.2 In Situ Precipitation of H2S Through Iron Chloride/Oxide Injection

7.2.2.3 Adsorption by Activated Carbon

7.2.2.4 Zeolite‐Based Sieve (Molecular Sieve)

7.2.2.5 Water Scrubbing

7.2.2.6 Organic Solvent Scrubbing

7.2.2.7 Sodium Hydroxide Scrubbing

7.2.2.8 Chemical Adsorption via Iron Oxide or Hydroxide (Iron Sponge)

7.2.2.9 Biological Filters

7.2.3 Removal of Siloxanes

7.2.3.1 Organic Solvent Scrubbing

7.2.3.2 Adsorption on Activated Carbon, Molecular Sieves, and Silica Gel

7.2.3.3 Membrane Separation

7.2.3.4 Biological Filters

7.2.3.5 Cryogenic Condensation

7.2.4 Removal of Volatile Organic Compound (VOCs)

7.2.5 Removal of Ammonia (NH3)

7.2.6 Removal of Oxygen (O2) and Nitrogen (N2)

7.3 Biogas Upgrading Technologies

7.3.1 Water Scrubbing

7.3.2 Organic Solvent Scrubbing

7.3.3 Chemical Scrubbing

7.3.4 Pressure Swing Adsorption

7.3.5 Polymeric Membranes

7.3.6 Cryogenic Treatment

7.4 Conclusions

References

8 CO2 Conversion to Value‐Added Gas‐Phase Products: Technology Overview and Catalysts Selection

8.1 Chapter Overview

8.2 CO2 Methanation. 8.2.1 Background

8.2.2 Fundamentals

8.2.3 Catalysts

8.2.3.1 Ruthenium‐Based Catalysts

8.2.3.2 Nickel‐Based Catalysts

8.2.3.3 Rhodium and Palladium‐Based Catalysts

8.3 RWGS Reaction. 8.3.1 Background

8.3.2 Fundamentals

8.3.3 Catalysts

8.3.3.1 Noble Metal‐Based Catalysts

8.3.3.2 Copper‐Based Catalysts

8.3.3.3 Ceria‐Based Support Catalysts

8.3.3.4 Carbide Support Catalysts

8.4 CO2 Reforming Reactions. 8.4.1 Background

8.4.2 Fundamentals

8.4.3 Catalysts

8.4.3.1 Noble Metal‐Based Catalysts

8.4.3.2 Ni‐Based Catalysts

8.4.3.3 Catalytic Supports

8.5 Conclusions and Final Remarks

References

9 CO2 Utilization Enabled by Microchannel Reactors

9.1 Introduction

9.2 Transport Phenomena and Heat Exchange in Microchannel Reactors

9.2.1 Microfluidics and Mixing Flow

9.2.2 Heat Exchange and Temperature Control

9.3 Application of Microreactors in CO2 Capture, Storage, and Utilization Processes

9.3.1 CO2 Capture and Storage (CCS)

9.3.2 CO2 as a Feedstock for Producing Valuable Commodity Chemicals

9.3.2.1 Methanation of Carbon Dioxide (Sabatier Reaction)

9.3.2.2 CO2‐to‐Methanol and Dimethyl Ether (DME) Transformation

9.3.2.3 CO2‐to‐Higher Hydrocarbons and Fuels

9.3.2.4 Production of Cyclic Organic Carbonates

9.4 Concluding Remarks and Future Perspectives

References

10 Analysis of High‐Pressure Conditions in CO2 Hydrogenation Processes

10.1 Introduction

10.2 Thermodynamic Aspects

10.2.1 Le Chatelier Principle as a Simple Way to Understand the Effect of Pressure in Chemical Reactions

10.2.2 Equilibrium Composition Calculations of High‐Pressure Gas Reactions Based on the Computerized Gibbs Energy Minimization

10.3 Overview of Some Industrial Approaches Focused on the Production of Valuable Compounds form CO2 Using a Carbon Capture and Utilization (CCU) Approach

10.3.1 Industrial Production of Methanol

10.3.2 Production of Methane

10.4 Techno‐Economic Considerations for the Methanol Production from a CCU Approach with the Use of High Pressure

10.5 Concluding Remarks

References

Notes

11 Sabatier‐Based Direct Synthesis of Methane and Methanol Using CO2 from Industrial Gas Mixtures

11.1 Overview

11.2 Methane Synthesis of Gas Mixtures

11.2.1 Thermodynamics of Methane Conversion

11.2.2 Experimental Setup, General Definitions, and Catalysts

11.2.3 Industrial Gas Mixtures

11.3 Applications

11.3.1 APP‐01: Combustion Plant Flue Gas

11.3.2 APP‐02: Coke Oven Gas (COG)

11.3.3 APP‐03: Saline Aquifer Back‐Produced CO2

11.3.4 APP‐04: Biogenic CO2 Sources

11.3.5 APP‐05: Oxyfuel Operation in Gas Engines

11.3.6 APP‐06: Reusage of CH4 Product Gas Mixtures

11.4 Methanol Synthesis

Acknowledgments

References

12 Survey of Heterogeneous Catalysts for the CO2 Reduction to CO via Reverse Water Gas Shift

12.1 Introduction

12.2 RWGS Catalysts

12.2.1 Supported Metal Catalysts

12.2.1.1 Au‐Based Catalysts

12.2.1.2 Pt‐Based Catalysts

12.2.1.3 Rh‐Based Catalysts

12.2.1.4 Ru‐Based Catalysts

12.2.1.5 Pd‐ and Ir‐Based Catalysts

12.2.1.6 Cu‐Based Catalysts

12.2.1.7 Ni‐Based Catalysts

12.2.2 Oxide Systems

12.2.3 Transition Metal Carbides

12.3 Mechanism of RWGS Reaction

References

13 Electrocatalytic Conversion of CO2 to Syngas

13.1 Introduction

13.2 Production of Syngas

13.3 Electroreduction of CO2/Water Mixtures to Syngas

13.3.1 Effect of Cell Configuration and Chemical Environment

13.3.2 Effect of the Cathode Composition and Structure

13.3.3 Effect of the Reaction Parameters

13.3.4 Electrochemical Promotion of Catalyst (EPOC) for CO2 Hydrogenation

13.4 Conclusions

Acknowledgments

References

14 Recent Progress on Catalyst Development for CO2 Conversion into Value‐Added Chemicals by Photo‐ and Electroreduction

14.1 Introduction

14.2 CO2 Catalytic Conversion by Photoreduction

14.2.1 Principle of CO2 Photothermal Reduction

14.2.2 Catalyst Development for CO2 Photothermal Reduction

14.3 CO2 Catalytic Conversion by Electroreduction

14.3.1 Principle of CO2 Electrocatalytic Reduction

14.3.2 Catalysts Development for CO2 Electroreduction

References

15 Yolk@Shell Materials for CO2 Conversion: Chemical and Photochemical Applications

15.1 Overview

15.2 Key Benefits of Hierarchical Morphology

15.2.1 Confinement Effects

15.3 Materials for Chemical CO2 Recycling Reactions

15.3.1 CO2 Utilization Reactions

15.3.2 Photochemical Reactions with CO2

15.3.2.1 Principles of Photocatalysis

15.3.2.2 Prominent Materials

15.3.2.3 Benefits of YS in Photocatalysis

15.4 Synthesis Techniques for CS/YS: A Brief Overview

15.4.1 Soft Templating Techniques

15.4.2 Hard Templating Techniques

15.4.2.1 Metal Oxide/Carbide Shells

15.5 Future Advancement

References

16 Aliphatic Polycarbonates Derived from Epoxides and CO2

Abbreviations

16.1 Introduction

16.2 Aliphatic Polycarbonates. 16.2.1 Synthesis of the Monomers

16.2.2 Mechanistic Aspects of the Copolymerization of Epoxides and CO2

16.2.3 Thermal Stability and Possible Degradation Pathways

16.2.4 Mechanical Properties

16.3 Catalyst Systems for the CO2/Epoxide Copolymerization

16.3.1 Heterogeneous Catalysts

16.3.2 Overview of the Homogeneous Catalytic Systems

16.3.3 Terpolymerization Pathways

16.3.4 Limonene Oxide: Recent Advances in Catalysis and Mechanism Elucidation

16.4 Conclusion

References

17 Metal–Organic Frameworks (MOFs) for CO2 Cycloaddition Reactions

17.1 Introduction to MOF

17.2 MOFs as Catalysts

17.2.1 Active Sites in MOFs: Lewis Acid Sites. 17.2.1.1 Historical Overview

17.2.1.2 Tunability of the Lewis Acid Sites. 17.2.1.2.1 Nature of the Metal Cluster

17.2.1.2.2 Defect Generation

17.2.1.3 Active Sites in MOFs: Lewis Basic Sites

17.3 CO2 Cycloadditions

17.3.1 Reaction Mechanism

17.3.2 CO2 Cycloadditions Reactions Catalyzed by Lewis Acid MOFs

17.3.3 CO2 Cycloaddition Reactions Catalyzed by Lewis Acid and Basic MOFs

17.3.4 Defective MOFs for CO2 Cycloaddition Reactions

17.3.5 MOFs Having Functional Linkers for CO2 Cycloaddition Reactions

17.4 Oxidative Carboxylation

References

18 Plasma‐Assisted Conversion of CO2

18.1 Introduction

18.1.1 What Is a Plasma?

18.1.2 History

18.1.3 Electrification

18.1.4 Thermodynamics

18.1.5 Homogeneous Plasma Activation of CO2

18.1.6 Mechanisms

18.1.7 Plasma Reactors

18.1.8 Performance in Various Plasma Reactors

18.2 Plasma‐catalytic CO2 Conversion

18.2.1 Introduction

18.2.2 Mutual Influence of Plasma and Catalyst

18.2.3 Catalyst Development

18.2.4 Experimental Performance

18.2.4.1 CO2 Dissociation

18.2.4.2 Dry Reforming of Methane

18.2.4.3 CO2 Hydrogenation

18.2.4.4 Artificial Photosynthesis

18.3 Perspective

18.3.1 Models Describing Plasma Catalysis

18.3.2 Scale‐Up and Process Considerations

18.4 Conclusion

References

Index

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Edited by

Tomas R. Reina José A. Odriozola Harvey Arellano‐Garcia

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For large bandgap oxide materials (e.g. Ce, Ti, and Zr), the formation of proton defects at moderate temperatures takes places through the dissociative absorption of water [80]. Water dissociates into a hydroxide ion and a proton, the hydrogen ion then occupies an oxide ion vacancy, and the proton forms a covalent bond with a lattice oxygen. The formation of proton defects implies a significant weight gain; hence, the concentration of such defects can be measured by thermogravimetric analysis (TGA) as a function of temperature and water partial pressure.

Understanding the mechanism of proton conduction is of utmost importance for the development of novel materials. It is generally accepted that proton diffusion in protonic conductors occur via the Grotthuss‐type mechanism assisted by water molecules [81–83]. Moreover, hydrogen separation is driven by the hydrogen partial pressure difference across the membrane.

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