Fuel cell systems explained /
Since publication of the first edition of Fuel Cell Systems Explained, three compelling drivers have supported the continuing development of fuel cell technology. These are: the need to maintain energy security in an energy-hungry world, the desire to move towards zero-emission vehicles and power pl...
Clasificación: | Libro Electrónico |
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Autores principales: | , |
Formato: | Electrónico eBook |
Idioma: | Inglés |
Publicado: |
Hoboken, NJ, USA :
Wiley,
[2018]
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Edición: | Third edition. |
Temas: | |
Acceso en línea: | Texto completo |
Tabla de Contenidos:
- Intro
- Title Page
- Copyright Page
- Contents
- Brief Biographies
- Preface
- Acknowledgments
- Acronyms and Initialisms
- Symbols and Units
- Chapter 1 Introducing Fuel Cells
- 1.1 Historical Perspective
- 1.2 Fuel-Cell Basics
- 1.3 Electrode Reaction Rates
- 1.4 Stack Design
- 1.5 Gas Supply and Cooling
- 1.6 Principal Technologies
- 1.7 Mechanically Rechargeable Batteries and Other Fuel Cells
- 1.7.1 Metal-Air Cells
- 1.7.2 Redox Flow Cells
- 1.7.3 Biological Fuel Cells
- 1.8 Balance-of-Plant Components
- 1.9 Fuel-Cell Systems: Key Parameters
- 1.10 Advantages and Applications
- Further Reading
- Chapter 2 Efficiency and Open-Circuit Voltage
- 2.1 Open-Circuit Voltage: Hydrogen Fuel Cell
- 2.2 Open-Circuit Voltage: Other Fuel Cells and Batteries
- 2.3 Efficiency and Its Limits
- 2.4 Efficiency and Voltage
- 2.5 Influence of Pressure and Gas Concentration
- 2.5.1 Nernst Equation
- 2.5.2 Hydrogen Partial Pressure
- 2.5.3 Fuel and Oxidant Utilization
- 2.5.4 System Pressure
- 2.6 Summary
- Further Reading
- Chapter 3 Operational Fuel-Cell Voltages
- 3.1 Fundamental Voltage: Current Behaviour
- 3.2 Terminology
- 3.3 Fuel-Cell Irreversibilities
- 3.4 Activation Losses
- 3.4.1 The Tafel Equation
- 3.4.2 The Constants in the Tafel Equation
- 3.4.3 Reducing the Activation Overpotential
- 3.5 Internal Currents and Fuel Crossover
- 3.6 Ohmic Losses
- 3.7 Mass-Transport Losses
- 3.8 Combining the Irreversibilities
- 3.9 The Electrical Double-Layer
- 3.10 Techniques for Distinguishing Irreversibilities
- 3.10.1 Cyclic Voltammetry
- 3.10.2 AC Impedance Spectroscopy
- 3.10.3 Current Interruption
- Further Reading
- Chapter 4 Proton-Exchange Membrane Fuel Cells
- 4.1 Overview
- 4.2 Polymer Electrolyte: Principles of Operation
- 4.2.1 Perfluorinated Sulfonic Acid Membrane.
- 4.2.2 Modified Perfluorinated Sulfonic Acid Membranes
- 4.2.3 Alternative Sulfonated and Non-Sulfonated Membranes
- 4.2.4 Acid-Base Complexes and Ionic Liquids
- 4.2.5 High-Temperature Proton Conductors
- 4.3 Electrodes and Electrode Structure
- 4.3.1 Catalyst Layers: Platinum-Based Catalysts
- 4.3.2 Catalyst Layers: Alternative Catalysts for Oxygen Reduction
- 4.3.2.1 Macrocyclics
- 4.3.2.2 Chalcogenides
- 4.3.2.3 Conductive Polymers
- 4.3.2.4 Nitrides
- 4.3.2.5 Functionalized Carbons
- 4.3.2.6 Heteropolyacids
- 4.3.3 Catalyst Layer: Negative Electrode
- 4.3.4 Catalyst Durability
- 4.3.5 Gas-Diffusion Layer
- 4.4 Water Management
- 4.4.1 Hydration and Water Movement
- 4.4.2 Air Flow and Water Evaporation
- 4.4.3 Air Humidity
- 4.4.4 Self-Humidified Cells
- 4.4.5 External Humidification: Principles
- 4.4.6 External Humidification: Methods
- 4.5 Cooling and Air Supply
- 4.5.1 Cooling with Cathode Air Supply
- 4.5.2 Separate Reactant and Cooling Air
- 4.5.3 Water Cooling
- 4.6 Stack Construction Methods
- 4.6.1 Introduction
- 4.6.2 Carbon Bipolar Plates
- 4.6.3 Metal Bipolar Plates
- 4.6.4 Flow-Field Patterns
- 4.6.5 Other Topologies
- 4.6.6 Mixed Reactant Cells
- 4.7 Operating Pressure
- 4.7.1 Technical Issues
- 4.7.2 Benefits of High Operating Pressures
- 4.7.2.1 Current
- 4.7.3 Other Factors
- 4.8 Fuel Types
- 4.8.1 Reformed Hydrocarbons
- 4.8.2 Alcohols and Other Liquid Fuels
- 4.9 Practical and Commercial Systems
- 4.9.1 Small-Scale Systems
- 4.9.2 Medium-Scale for Stationary Applications
- 4.9.3 Transport System Applications
- 4.10 System Design, Stack Lifetime and Related Issues
- 4.10.1 Membrane Degradation
- 4.10.2 Catalyst Degradation
- 4.10.3 System Control
- 4.11 Unitized Regenerative Fuel Cells
- Further Reading
- Chapter 5 Alkaline Fuel Cells
- 5.1 Principles of Operation.
- 5.2 System Designs
- 5.2.1 Circulating Electrolyte Solution
- 5.2.2 Static Electrolyte Solution
- 5.2.3 Dissolved Fuel
- 5.2.4 Anion-Exchange Membrane Fuel Cells
- 5.3 Electrodes
- 5.3.1 Sintered Nickel Powder
- 5.3.2 Raney Metals
- 5.3.3 Rolled Carbon
- 5.3.4 Catalysts
- 5.4 Stack Designs
- 5.4.1 Monopolar and Bipolar
- 5.4.2 Other Stack Designs
- 5.5 Operating Pressure and Temperature
- 5.6 Opportunities and Challenges
- Further Reading
- Chapter 6 Direct Liquid Fuel Cells
- 6.1 Direct Methanol Fuel Cells
- 6.1.1 Principles of Operation
- 6.1.2 Electrode Reactions with a Proton-Exchange Membrane Electrolyte
- 6.1.3 Electrode Reactions with an Alkaline Electrolyte
- 6.1.4 Anode Catalysts
- 6.1.5 Cathode Catalysts
- 6.1.6 System Designs
- 6.1.7 Fuel Crossover
- 6.1.8 Mitigating Fuel Crossover: Standard Techniques
- 6.1.9 Mitigating Fuel Crossover: Prospective Techniques
- 6.1.10 Methanol Production
- 6.1.11 Methanol Safety and Storage
- 6.2 Direct Ethanol Fuel Cells
- 6.2.1 Principles of Operation
- 6.2.2 Ethanol Oxidation, Catalyst and Reaction Mechanism
- 6.2.3 Low-Temperature Operation: Performance and Challenges
- 6.2.4 High-Temperature Direct Ethanol Fuel Cells
- 6.3 Direct Propanol Fuel Cells
- 6.4 Direct Ethylene Glycol Fuel Cells
- 6.4.1 Principles of Operation
- 6.4.2 Ethylene Glycol: Anodic Oxidation
- 6.4.3 Cell Performance
- 6.5 Formic Acid Fuel Cells
- 6.5.1 Formic Acid: Anodic Oxidation
- 6.5.2 Cell Performance
- 6.6 Borohydride Fuel Cells
- 6.6.1 Anode Catalysts
- 6.6.2 Challenges
- 6.7 Application of Direct Liquid Fuel Cells
- Further Reading
- Chapter 7 Phosphoric Acid Fuel Cells
- 7.1 High-Temperature Fuel-Cell Systems
- 7.2 System Design
- 7.2.1 Fuel Processing
- 7.2.2 Fuel Utilization
- 7.2.3 Heat-Exchangers
- 7.2.3.1 Designs
- 7.2.3.2 Exergy Analysis
- 7.2.3.3 Pinch Analysis.
- 7.3 Principles of Operation
- 7.3.1 Electrolyte
- 7.3.2 Electrodes and Catalysts
- 7.3.3 Stack Construction
- 7.3.4 Stack Cooling and Manifolding
- 7.4 Performance
- 7.4.1 Operating Pressure
- 7.4.2 Operating Temperature
- 7.4.3 Effects of Fuel and Oxidant Composition
- 7.4.4 Effects of Carbon Monoxide and Sulfur
- 7.5 Technological Developments
- Further Reading
- Chapter 8 Molten Carbonate Fuel Cells
- 8.1 Principles of Operation
- 8.2 Cell Components
- 8.2.1 Electrolyte
- 8.2.2 Anode
- 8.2.3 Cathode
- 8.2.4 Non-Porous Components
- 8.3 Stack Configuration and Sealing
- 8.3.1 Manifolding
- 8.3.2 Internal and External Reforming
- 8.4 Performance
- 8.4.1 Influence of Pressure
- 8.4.2 Influence of Temperature
- 8.5 Practical Systems
- 8.5.1 Fuel Cell Energy (USA)
- 8.5.2 Fuel Cell Energy Solutions (Europe)
- 8.5.3 Facilities in Japan
- 8.5.4 Facilities in South Korea
- 8.6 Future Research and Development
- 8.7 Hydrogen Production and Carbon Dioxide Separation
- 8.8 Direct Carbon Fuel Cell
- Further Reading
- Chapter 9 Solid Oxide Fuel Cells
- 9.1 Principles of Operation
- 9.1.1 High-Temperature (HT) Cells
- 9.1.2 Low-Temperature (IT) Cells
- 9.2 Components
- 9.2.1 Zirconia Electrolyte for HT-Cells
- 9.2.2 Electrolytes for IT-Cells
- 9.2.2.1 Ceria
- 9.2.2.2 Perovskites
- 9.2.2.3 Other Materials
- 9.2.3 Anodes
- 9.2.3.1 Nickel-YSZ
- 9.2.3.2 Cathode
- 9.2.3.3 Mixed Ionic-Electronic Conductor Anode
- 9.2.4 Cathode
- 9.2.5 Interconnect Material
- 9.2.6 Sealing Materials
- 9.3 Practical Design and Stacking Arrangements
- 9.3.1 Tubular Design
- 9.3.2 Planar Design
- 9.4 Performance
- 9.5 Developmental and Commercial Systems
- 9.5.1 Tubular SOFCs
- 9.5.2 Planar SOFCs
- 9.6 Combined-Cycle and Other Systems
- Further Reading
- Chapter 10 Fuels for Fuel Cells
- 10.1 Introduction
- 10.2 Fossil Fuels.
- 10.2.1 Petroleum
- 10.2.2 Petroleum from Tar Sands, Oil Shales and Gas Hydrates
- 10.2.3 Coal and Coal Gases
- 10.2.4 Natural Gas and Coal-Bed Methane (Coal-Seam Gas)
- 10.3 Biofuels
- 10.4 Basics of Fuel Processing
- 10.4.1 Fuel-Cell Requirements
- 10.4.2 Desulfurization
- 10.4.3 Steam Reforming
- 10.4.4 Carbon Formation and Pre-Reforming
- 10.4.5 Internal Reforming
- 10.4.5.1 Indirect Internal Reforming (IIR)
- 10.4.5.2 Direct Internal Reforming (DIR)
- 10.4.6 Direct Hydrocarbon Oxidation
- 10.4.7 Partial Oxidation and Autothermal Reforming
- 10.4.8 Solar-Thermal Reforming
- 10.4.9 Sorbent-Enhanced Reforming
- 10.4.10 Hydrogen Generation by Pyrolysis or Thermal Cracking of Hydrocarbons
- 10.4.11 Further Fuel Processing: Removal of Carbon Monoxide
- 10.5 Membrane Developments for Gas Separation
- 10.5.1 Non-Porous Metal Membranes
- 10.5.2 Non-Porous Ceramic Membranes
- 10.5.3 Porous Membranes
- 10.5.4 Oxygen Separation
- 10.6 Practical Fuel Processing: Stationary Applications
- 10.6.1 Industrial Steam Reforming
- 10.6.2 Fuel-Cell Plants Operating with Steam Reforming of Natural Gas
- 10.6.3 Reformer and Partial Oxidation Designs
- 10.6.3.1 Conventional Packed-Bed Catalytic Reactors
- 10.6.3.2 Compact Reformers
- 10.6.3.3 Plate Reformers and Microchannel Reformers
- 10.6.3.4 Membrane Reactors
- 10.6.3.5 Non-Catalytic Partial Oxidation Reactors
- 10.6.3.6 Catalytic Partial Oxidation Reactors
- 10.7 Practical Fuel Processing: Mobile Applications
- 10.8 Electrolysers
- 10.8.1 Operation of Electrolysers
- 10.8.2 Applications
- 10.8.3 Electrolyser Efficiency
- 10.8.4 Photoelectrochemical Cells
- 10.9 Thermochemical Hydrogen Production and Chemical Looping
- 10.9.1 Thermochemical Cycles
- 10.9.2 Chemical Looping
- 10.10 Biological Production of Hydrogen
- 10.10.1 Introduction.