Hydrogen production technologies /
Clasificación: | Libro Electrónico |
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Otros Autores: | , |
Formato: | Electrónico eBook |
Idioma: | Inglés |
Publicado: |
Beverly, MA : Hoboken, NJ :
Scrivener Publishing ; John Wiley & Sons,
2017.
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Colección: | Advances in hydrogen production and storage
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Temas: | |
Acceso en línea: | Texto completo |
Tabla de Contenidos:
- Cover
- Title Page
- Copyright
- Contents
- Preface
- Part I Catalytic and Electrochemical Hydrogen Production
- 1 Hydrogen Production from Oxygenated Hydrocarbons: Review of Catalyst Development, Reaction Mechanism and Reactor Modeling
- 1.1 Introduction
- 1.2 Catalyst Development for the Steam Reforming Process
- 1.2.1 Catalyst Development for the Steam Reforming of Methanol (SRM)
- 1.2.2 Catalyst Development for the Steam Reforming of Ethanol (SRE)
- 1.2.2.1 Co-Based Catalysts for SRE
- 1.2.2.2 Ni-Based Catalysts for SRE
- 1.2.2.3 Bimetallic-Based Catalysts for SRE
- 1.2.3 Catalyst Development for the Steam Reforming of Glycerol (SRG)
- 1.3 Kinetics and Reaction Mechanism for Steam Reforming of Oxygenated Hydrocarbons
- 1.3.1 Surface Reaction Mechanism for SRM
- 1.3.2 Surface Reaction Mechanism for SRE
- 1.3.3 Surface Reaction Mechanism for SRG
- 1.4 Reactor Modeling and Simulation in Steam Reforming of Oxygenated Hydrocarbons
- References
- 2 Ammonia Decomposition for Decentralized Hydrogen Production in Microchannel Reactors: Experiments and CFD Simulations
- 2.1 Introduction
- 2.2 Ammonia Decomposition for Hydrogen Production
- 2.2.1 Ammonia as a Hydrogen Carrier
- 2.2.2 Thermodynamics of Ammonia Decomposition
- 2.2.3 Reaction Mechanism and Kinetics for Ammonia Decomposition
- 2.2.3.1 Effect of Ammonia Concentration
- 2.2.3.2 Effect of Hydrogen Concentration
- 2.2.4 Current Status for Hydrogen Production Using Ammonia Decomposition
- 2.2.4.1 Microreactors for Ammonia Decomposition
- 2.3 Ammonia-Fueled Microchannel Reactors for Hydrogen Production: Experiments
- 2.3.1 Microchannel Reactor Design
- 2.3.2 Reactor Operation and Performance
- 2.3.2.1 Microchannel Reactor Operation
- 2.3.2.2 Performance and Operational Considerations
- 2.3.2.3 Performance Comparison with Other Ammonia Microreactors.
- 2.4 CFD Simulation of Hydrogen Production in Ammonia-Fueled Microchannel Reactors
- 2.4.1 Model Validation
- 2.4.2 Velocity, Temperature and Concentration Distributions
- 2.4.3 Evaluation of Mass Transport Limitations
- 2.4.4 Model Limitations: Towards Multiscale Simulations
- 2.5 Summary
- Acknowledgments
- References
- 3 Hydrogen Production with Membrane Systems
- 3.1 Introduction
- 3.2 Pd-Based Membranes
- 3.2.1 Long-Term Stability of Ceramic Supported Thin Pd-Based Membranes
- 3.2.2 Long-Term Stability of Metallic Supported Thin Pd-Based Membranes
- 3.3 Fuel Reforming in Membrane Reactors for Hydrogen Production
- 3.3.1 Ceramic Supported Pd-Based Membrane Reactor and Comparison with Commercial Membrane
- 3.3.2 Metallic Supported Pd-Based Membrane Reactor
- 3.4 Thermodynamic and Economic Analysis of Fluidized Bed Membrane Reactors for Methane Reforming
- 3.4.1 Comparison of Membrane Reactors to Emergent Technologies
- 3.4.1.1 Methods and Assumptions
- 3.4.1.2 Comparison
- 3.4.2 Techno-Economical Comparison of Membrane Reactors to Benchmark Reforming Plant
- 3.5 Conclusions
- Acknowledgments
- References
- 4 Catalytic Hydrogen Production from Bioethanol
- 4.1 Introduction
- 4.2 Production Technology Overview
- 4.2.1 Fermentative Hydrogen Production
- 4.2.2 Photocatalytic Hydrogen Production
- 4.2.3 Aqueous Phase Reforming
- 4.2.4 CO2 Dry Reforming
- 4.2.5 Plasma Reforming
- 4.2.6 Partial Oxidation
- 4.2.7 Steam Reforming
- 4.3 Catalyst Overview
- 4.4 Catalyst Optimization Strategies
- 4.5 Reaction Mechanism and Kinetic Studies
- 4.6 Computational Approaches
- 4.7 Economic Considerations
- 4.8 Future Development Directions
- Acknowledgment
- References
- 5 Hydrogen Generation from the Hydrolysis of Ammonia Borane Using Transition Metal Nanoparticles as Catalyst
- 5.1 Introduction.
- 5.2 Transition Metal Nanoparticles in Catalysis
- 5.3 Preparation, Stabilization and Characterization of Metal Nanoparticles
- 5.4 Transition Metal Nanoparticles in Hydrogen Generation from the Hydrolysis of Ammonia Borane
- 5.5 Durability of Catalysts in Hydrolysis of Ammonia Borane
- 5.6 Conclusion
- References
- 6 Hydrogen Production by Water Electrolysis
- 6.1 Historical Aspects of Water Electrolysis
- 6.2 Fundamentals of Electrolysis
- 6.2.1 Thermodynamics
- 6.2.2 Kinetics and Efficiencies
- 6.3 Modern Status of Electrolysis
- 6.3.1 Water Electrolysis Technologies
- 6.3.2 Alkaline Water Electrolysis
- 6.3.3 PEM Water Electrolysis
- 6.3.4 High Temperature Water Electrolysis
- 6.4 Perspectives of Hydrogen Production by Electrolysis
- Acknowledgment
- References
- 7 Electrochemical Hydrogen Production from SO2 and Water in a SDE Electrolyzer
- 7.1 Introduction
- 7.2 Membrane Characterization
- 7.2.1 Weight Change
- 7.2.2 Ion Exchange Capacity (IEC)
- 7.2.3 TGA-MS
- 7.3 MEA Characterization
- 7.3.1 MEA Manufacture
- 7.3.2 MEA Characterization
- 7.4 Effect of Anode Impurities
- 7.5 High Temperature SO2 Electrolysis
- 7.6 Conclusion
- References
- Part II Bio Hydrogen Production
- 8 Biomass Fast Pyrolysis for Hydrogen Production from Bio-Oil
- 8.1 Introduction
- 8.2 Biomass Pyrolysis to Produce Bio-Oils
- 8.2.1 Fast Pyrolysis for Bio-Oil Production
- 8.2.2 Pyrolysis Reactions
- 8.2.2.1 Hemicellulose Pyrolysis
- 8.2.2.2 Cellulose Pyrolysis
- 8.2.2.3 Lignin Pyrolysis
- 8.2.2.4 Char Formation Process
- 8.2.3 Influence of the Pretreatment of Raw Biomass and Pyrolysis Paramenters on Bio-Oil Production
- 8.2.4 Pyrolysis Reactors
- 8.2.4.1 Drop Tube Reactor
- 8.2.4.2 Bubbling Fluid Beds
- 8.2.4.3 Circulating Fluid Beds and Transported Beds
- 8.2.4.4 Rotating Cone
- 8.2.4.5 Ablative Pyrolysis.
- 8.2.4.6 Vacuum Pyrolysis
- 8.2.4.7 Screw or Auger Reactors
- 8.3 Bio-oil Reforming Processes
- 8.3.1 Bio-oil Reforming Reactions
- 8.3.2 Reforming Catalysts
- 8.3.2.1 Non-Noble Metal-Based Catalysts
- 8.3.2.2 Noble Metal-Based Catalysts
- 8.3.2.3 Conventional Supports
- 8.3.2.4 Non-Conventional Supports
- 8.3.3 Reaction Systems
- 8.3.4 Reforming Process Intensifications
- 8.3.4.1 Sorption Enhanced Steam Reforming
- 8.3.4.2 Chemical Looping
- 8.3.4.3 Sorption Enhanced Chemical Looping
- 8.4 Future Prospects
- References
- 9 Production of a Clean Hydrogen-Rich Gas by the Staged Gasification of Biomass and Plastic Waste
- 9.1 Introduction
- 9.2 Chemistry of Gasification
- 9.3 Tar Cracking and H2 Production
- 9.4 Staged Gasification
- 9.4.1 Two-Stage UOS Gasification Process
- 9.4.2 Three-Stage UOS Gasification Process
- 9.5 Experimental Results and Discussion
- 9.5.1 Effects of Type of Feed Material on H2 Production
- 9.5.2 Effect of Activated Carbon on H2 Production
- 9.5.3 Effects of Other Reaction Parameters on H2 Production
- 9.5.3.1 Temperature
- 9.5.3.2 ER
- 9.5.3.3 Gasifying Agent
- 9.5.4 Comparison of Two-Stage and Three-Stage Gasifiers
- 9.5.5 Tar Removal Mechanism over Activated Carbon
- 9.5.6 Deactivation of Activated Carbon and Long-Term Gasification Experiments
- 9.5.7 Removal of Other Impurities (NH3, H2S, and HCl)
- 9.6 Conclusions
- References
- 10 Enhancement of Bio-Hydrogen Production Technologies by Sulphate-Reducing Bacteria
- 10.1 Introduction
- 10.2 Sulphate-Reducing Bacteria for H2 Production
- 10.3 Mathematical Modeling of the SR Fermentation
- 10.4 Bifurcation Analysis
- 10.5 Process Control Strategies
- 10.6 Conclusions
- Acknowledgment
- Nomenclature
- References.
- 11 Microbial Electrolysis Cells (MECs) as Innovative Technology for Sustainable Hydrogen Production: Fundamentals and Perspective Applications
- 11.1 Introduction
- 11.2 Principles of MEC for Hydrogen Production
- 11.3 Thermodynamics of MEC
- 11.4 Factors Influencing the Performance of MECs
- 11.4.1 Biological Factors
- 11.4.1.1 Electrochemically Active Bacteria (EAB) in MECs
- 11.4.1.2 Extracellular Electron Transfer in MECs
- 11.4.1.3 Inoculation and Source of Inoculum
- 11.4.2 Electrode Materials Used in MECs
- 11.4.2.1 Anode Electrode Materials
- 11.4.2.2 Cathode Electrode Materials or Catalysts
- 11.4.3 Membrane or Separator
- 11.4.4 Physical Factors
- 11.4.5 Substrates Used in MECs
- 11.4.6 MEC Operational Factors
- 11.4.6.1 Applied Voltage
- 11.4.6.2 Other Key Operational Factors
- 11.5 Current Application of MECs
- 11.5.1 Hydrogen Production and Wastewater Treatment
- 11.5.1.1 Treatment of DWW Using MECs
- 11.5.1.2 Use of MECs for Treatment of IWW and Other Types of WW
- 11.5.2 Application of MECs in Removal of Ammonium or Nitrogen from Urine
- 11.5.3 MECs for Valuable Products Synthesis
- 11.5.3.1 Methane (CH4)
- 11.5.3.2 Acetate
- 11.5.3.3 Hydrogen Peroxide (H2O2)
- 11.5.3.4 Ethanol (C2H5OH)
- 11.5.3.5 Formic Acid (HCOOH)
- 11.6 Conclusions and Prospective Application of MECs
- Acknowledgments
- References
- 12 Algae to Hydrogen: Novel Energy-Efficient Co-Production of Hydrogen and Power
- 12.1 Introduction
- 12.2 Algae Potential and Characteristics
- 12.2.1 Algae Potential
- 12.2.2 Types of Algae
- 12.2.3 Compositions of Algae
- 12.3 Energy-Efficient Energy Harvesting Technologies
- 12.4 Pretreatment (Drying)
- 12.5 Conversion of Algae to Hydrogen-Rich Gases
- 12.5.1 SCWG for Algae
- 12.5.1.1 Integrated System with SCWG
- 12.5.1.2 Analysis of the Integrated System.