
Electrochemical Power Sources
Beschreibung
Alles über E-Books | Antworten auf Fragen rund um E-Books, Kopierschutz und Dateiformate finden Sie in unserem Info- & Hilfebereich.
Rezensionen / Stimmen
"Electrochemical Power Sources: Batteries, Fuel Cells, and Supercapacitors" is an excellent introductory text to electrochemical energy devices which covers material considerations, historical developments of the technology and future prospects, spanning fundamental mechanisms to engineering challenges at a high level perspective. The supercapacitor section in particular goes into much more detail of the materials. This text would be most useful for students studying an introduction to electrochemistry course." (Johnson Matthey Technology Review, 1 October 2015)Weitere Details
Weitere Ausgaben
Andere Ausgaben


Personen
Inhalt
Foreword xv
Acknowledgements xvii
Preface xix
Symbols xxi
Abbrevations xxiii
Introduction xxv
Part I Batteries with Aqueous Electrolytes 1
1 General Aspects 3
1.1 Definition 3
1.2 Current-Producing Chemical Reaction 3
1.3 Classification 5
1.4 Thermodynamic Aspects 6
1.5 Historical Development 8
1.6 Nomenclature 9
Reviews and Monographs 10
2 Main Battery Types 11
2.1 Electrochemical Systems 11
2.2 Leclanché (Zinc-Carbon) Batteries 12
2.3 The Zinc Electrode in Alkaline Solutions 14
2.4 Alkaline Manganese-Zinc Batteries 14
2.5 Lead Acid Batteries 17
2.6 Alkaline Nickel Storage Batteries 20
2.7 Silver-Zinc Batteries 23
References 24
Monographs and Reviews 25
3 Performance 27
3.1 Electrical Characteristics of Batteries 27
3.2 Electrical Characteristics of Storage Batteries 30
3.3 Comparative Characteristics 30
3.4 Operational Characteristics 31
References 32
4 Miscellaneous Batteries 33
4.1 Mercury-Zinc Batteries 33
4.2 Compound Batteries 34
4.3 Batteries with Water as Reactant 37
4.4 Standard Cells 38
4.5 Reserve Batteries 39
Reference 41
Reviews and Monographs 41
5 Design and Technology 43
5.1 Balance in Batteries 43
5.2 Scale Factors 44
5.3 Separators 44
5.4 Sealing 46
5.5 Ohmic Losses 47
5.6 Thermal Processes in Batteries 48
6 Applications of Batteries 51
6.1 Automotive Equipment Starter and Auxiliary Batteries 51
6.2 Traction Batteries 52
6.3 Stationary Batteries 53
6.4 Domestic and Portable Systems 53
6.5 Special Applications 54
7 Operational Problems 55
7.1 Discharge and Maintenance of Primary Batteries 55
7.2 Maintenance of Storage Batteries 56
7.3 General Aspects of Battery Maintenance 60
8 Outlook for Batteries with Aqueous Electrolyte 63
References 64
Part II Batteries with Nonaqueous Electrolytes 65
9 Different Kinds of Electrolytes 67
9.1 Electrolytes Based on Aprotic Nonaqueous Solutions 68
9.2 Ionically Conducting Molten Salts 69
9.3 Ionically Conducting Solid Electrolytes 70
References 72
10 Insertion Compounds 73
Monographs and Reviews 76
11 Primary Lithium Batteries 77
11.1 General Information: Brief History 77
11.2 Current-Producing and Other Processes in Primary Power Sources 79
11.3 Design of Primary Lithium Cells 81
11.4 Fundamentals of the Technology of Manufacturing of Lithium Primary Cells 82
11.5 Electric Characteristics of Lithium Cells 82
11.6 Operational Characteristics of Lithium Cells 83
11.7 Features of Primary Lithium Cells of Different Electrochemical Systems 84
Monographs 89
12 Lithium Ion Batteries 91
12.1 General Information: Brief History 91
12.2 Current-Producing and Other Processes in Lithium Ion Batteries 93
12.3 Design and Technology of Lithium Ion Batteries 96
12.4 Electric Characteristics, Performance, and Other Characteristics of Lithium Ion Batteries 98
12.5 Prospects of Development of Lithium Ion Batteries 99
Monographs 101
13 Lithium Ion Batteries: What Next? 103
13.1 Lithium-Air Batteries 103
13.2 Lithium-Sulfur Batteries 106
13.3 Sodium Ion Batteries 108
Reviews 110
14 Solid-State Batteries 111
14.1 Low-Temperature Miniature Batteries with Solid Electrolytes 111
14.2 Sulfur-Sodium Storage Batteries 112
Monographs and Reviews 115
15 Batteries with Molten Salt Electrolytes 117
15.1 Storage Batteries 117
15.2 Reserve-Type Thermal Batteries 120
References 122
Part III Fuel Cells 123
16 General Aspects 125
16.1 Thermodynamic Aspects 125
16.2 Schematic Layout of Fuel-Cell Units 128
16.3 Types of Fuel Cells 131
16.4 Layout of a Real Fuel Cell: The Hydrogen-Oxygen Fuel Cell with Liquid Electrolyte 132
16.5 Basic Parameters of Fuel Cells 134
Reference 140
Monographs 140
17 The Development of Fuel Cells 141
17.1 The Period prior to 1894 141
17.2 The Period from 1894 to 1960 143
17.3 The Period from 1960 to the 1990s 144
17.4 The Period after the 1990s 148
References 149
Monographs and Reviews 150
18 Proton-Exchange Membrane Fuel Cells (PEMFC) 151
18.1 The History of PEMFC 151
18.2 Standard PEMFC Version of the 1990s 154
18.3 Operating Conditions of PEMFC 156
18.4 Special Features of PEMFC Operation 157
18.5 Platinum Catalyst Poisoning by Traces of Co in the Hydrogen 159
18.6 Commercial Activities in Relation to PEMFC 161
18.7 Future Development of PEMFCs 162
18.8 Elevated-Temperature PEMFCs (ET-PEMFCs) 167
References 170
Reviews 170
19 Direct Liquid Fuel Cells with Gaseous, Liquid, And/Or Solid Reagents 171
19.1 Current-Producing Reactions and Thermodynamic Parameters 172
19.2 Anodic Oxidation of Methanol 172
19.3 Use of Platinum-Ruthenium Catalysts for Methanol Oxidation 173
19.4 Milestones in DMFC Development 173
19.5 Membrane Penetration by Methanol (Methanol Crossover) 174
19.6 Varieties of DMFC 176
19.7 Special Operating Features of DMFC 178
19.8 Practical Prototypes of DMFC and Their Features 180
19.9 The Problems to be Solved in Future DMFC 181
19.10 Direct Liquid Fuel Cells (DLFC) 183
Reference 188
Reviews 188
20 Molten Carbonate Fuel Cells (MCFC) 191
20.1 Special Features of High-Temperature Fuel Cells 191
20.2 The Structure of Hydrogen-Oxygen MCFC 192
20.3 MCFC with Internal Fuel Reforming 194
20.4 The Development of MCFC Work 195
20.5 The Lifetime of MCFCs 196
References 198
Reviews and Monographs 198
21 Solid Oxide Fuel Cells (SOFCs) 199
21.1 Schematic Design of a Conventional SOFC 200
21.2 Tubular SOFCs 201
21.3 Planar SOFCs 202
21.4 Varieties of SOFCs 205
21.5 The Utilization of Natural Fuels in SOFCs 206
21.6 Interim-Temperature SOFCs (ITSOFCs) 208
21.7 Low-Temperature SOFCs (LT-SOFC) 211
21.8 Factors Influencing the Lifetime of SOFCs 211
References 212
Monographs and Reviews 212
22 Other Types of Fuel Cells 213
22.1 Phosphoric Acid Fuel Cells (PAFCs) 213
22.2 Redox Flow Fuel Cells 218
22.3 Biological Fuel Cells 221
22.4 Direct Carbon Fuel Cells (DCFCs) 224
References 227
Monographs 227
23 Alkaline Fuel Cells (AFCs) 229
23.1 Hydrogen-Oxygen AFCs 230
23.2 Problems in the AFC Field 233
23.3 The Present State and Future Prospects of AFC Work 235
23.4 Anion-Exchange (Hydroxyl Ion Conducting) Membranes 236
23.5 Methanol Fuel Cell with an Invariant Alkaline Electrolyte 237
References 237
Monograph 237
24 Applications of Fuel Cells 239
24.1 Large Stationary Power Plants 239
24.2 Small Stationary Power Units 242
24.3 Fuel Cells for Transport Applications 243
24.4 Portables 248
24.5 Military Applications 250
References 250
25 Outlook for Fuel Cells 251
25.1 Alternating Periods of Hope and Disappointment-Forever? 252
25.2 Development of Electrocatalysis 252
25.3 "Ideal Fuel Cells" Do Exist 253
25.4 Expected Future Situation with Fuel Cells 255
Reference 256
Monographs 256
Part IV Supercapacitors 257
26 General Aspects 259
26.1 Electrolytic Capacitors 259
References 261
27 Electrochemical Supercapacitors with Carbon Electrodes 263
27.1 Introduction 263
27.2 Main Properties of Electric Double-Layer Capacitors (EDLC) 264
27.3 EDLC Energy Density and Power Density 267
27.4 Fundamentals of EDLC Macrokinetics 271
27.5 Porous Structure and Hydrophilic-Hydrophobic Properties of Highly Dispersed Carbon Electrodes 272
27.6 Effect of Ratio of Ion and Molecule Sizes and Pore Sizes 275
27.7 Effect of Functional Groups on EDLC Characteristics 277
27.8 Electrolytes Used in EDLC 279
27.9 Impedance of Highly Dispersed Carbon Electrodes 283
27.10 Nanoporous Carbons Obtained Using Various Techniques 286
27.11 High-Frequency Carbon Supercapacitors 303
27.12 Self-Discharge of Carbon Electrodes and Supercapacitors 306
27.13 Processes of EDLC Degradation (AGING) 311
References 313
Monograph and Reviews 313
28 Pseudocapacitor Electrodes and Supercapacitors 315
28.1 Electrodes Based on Inorganic Salts of Transition Metals 315
28.2 Electrodes Based on Electron-Conducting Polymers (ECPs) 322
28.3 Redox Capacitors Based on Organic Monomers 333
28.4 Lithium-Cation-Exchange Capacitors 335
References 337
Monograph and Reviews 337
29 Hybrid (Asymmetric) Supercapacitors (HSCs) 339
29.1 HSCs of MeOx/C Types 339
29.2 HSCs of ECP/C Type 343
References 344
Review 344
30 Comparison of Characteristics of Supercapacitors and Other Electrochemical Devices. Characteristics of Commercial Supercapacitors 345
Reference 350
Reviews 350
31 Prospects of Electrochemical Supercapacitors 351
32 Electrochemical Aspects of Solar Energy Conversion 355
32.1 Photoelectrochemical Phenomena 355
32.2 Photoelectrochemical Devices 356
32.3 Photoexcitation of Metals (Electron Photoemission into Solutions) 356
32.4 Behavior of Illuminated Semiconductors 357
32.5 Semiconductor Solar Batteries (SC-SB) 358
32.6 Dye-Sensitized Solar Cells (DSSC) 360
References 363
Reviews and Monographs 363
Author Index 365
Subject Index 369
Chapter 1
General Aspects
1.1 Definition
Batteries are a variety of galvanic cells, that is, devices containing two (identical or different) electron-conducting electrodes, which contact an ion-conducting electrolyte. Batteries are destined to convert the energy of a chemical reaction between solid electrode components into electrical energy providing an electric current (when the circuit is closed) between two not-identical electrodes having different values of the electrode potential (positive and negative terminals). A battery comprises one or several single galvanic cells. In each such cell a comparatively low voltage is generated, typically 0.5-4 V for different classes of cells. Where higher voltages are required, the necessary number of cells is connected in series to form a galvanic battery. Colloquially, the term "battery" is often used to denote single galvanic cells acting as electrochemical power sources as well as groups of single cells. This is retained in this book. Some battery types retain the term "cell" even for groups of single cells (e.g., fuel cell, not fuel battery). The term "cell" is also used when it is necessary to compare different aspects of single-cell and multicell batteries.
1.2 Current-Producing Chemical Reaction
Reactions in batteries are chemical reactions between an oxidizer and a reducer. In reactions of this type, the reducer being oxidized releases electrons while the oxidizer being reduced accepts electrons. An example of such a redox reaction is the reaction between silver oxide (the oxidizer) and metallic zinc (the reducer):
1.1in which electrons are transferred from zinc atoms of metallic zinc to silver ions in the crystal lattice of silver oxide. When reaction (1.1) is allowed to proceed in a jar in which silver oxide is thoroughly mixed with fine zinc powder, no electrical energy is produced in spite of all the electron transfers at grain boundaries. This is because these transfers occur randomly in space and the reaction energy is liberated as heat that can raise the temperature of the reaction mixture to dangerous levels. The same reaction does occur in batteries, but in an ordered manner in two partial reactions separated in space and accompanied by electric current flow (Fig. 1.1).
Figure 1.1 Schematic of a silver-zinc battery.
In the simple case a battery (cell) consists of two electrodes made of different materials immersed in an electrolyte. The electrodes are conducting metal plates or grids covered by reactants (active mass); the oxidizer is present on one electrode, the reducer on the other. In silver-zinc cells the electrodes are metal grids, one covered with silver oxide and the other with zinc. An aqueous solution of KOH serves as electrolyte. Schematically, this system can be written as
1.2When these electrodes are placed into the common electrolyte enabling electrolytic contact between them, an open circuit voltage (OCV) e develops between them (here e = 1.6 V), zinc being the negative electrode. When they are additionally connected by an electronically conducting external circuit, the OCV causes electrons to flow through it from the negative to the positive electrode. This is equivalent to an electric current I in the opposite direction. This current is the result of reactions occurring at the surfaces of the electrodes immersed into the electrolyte: zinc being oxidized at the negative electrode (anode)1
1.3and silver oxide being reduced at the positive electrode (cathode)
1.4These electrode reactions sustain a continuous flow of electrons in the external circuit. The OH- ions produced by reaction (1.4) in the vicinity of the positive electrode are transported through the electrolyte toward the negative electrode to replace OH- ions consumed in reaction (1.3). Thus, the electric circuit as a whole is closed. Apart from the OCV, the current depends on the cell's internal resistance and the ohmic resistance present in the external circuit. Current flow will stop as soon as at least one of the reactants is consumed.
In contrast to what occurred in the jar, in the batteries, the overall chemical reaction occurs in the form of two spatially separated partial electrochemical reactions. Electric current is generated because the random transfer of electrons is replaced by a spatially ordered overall process (current-producing reaction).
1.3 Classification
By their principles of functioning, batteries can be classified as follows:
- Primary (single-discharge) batteries. A primary battery contains a finite quantity of the reactants participating in the reaction; once this quantity is consumed (on completion of discharge), a primary battery cannot be used again ("throw-away batteries").
- Storage (multiple-cycle) batteries (also called secondary or rechargeable batteries). On the completion of discharge, a storage battery can be recharged by forcing an electric current through it in the opposite direction; this will regenerate the original reactants from the reaction (or discharge) products. Therefore, electric energy supplied by an external power source (such as the grid) is stored in the battery in the form of chemical energy. During the discharge phase this energy is delivered to a consumer independent of the grid. During the charging phase the electrode reactions and the overall current-producing reaction occur in the direction opposite to that during discharge. Thus, these reactions must be chemically reversible (the notion of chemical reversibility must not be confused with that of thermodynamic reversibility). Good rechargeable batteries will sustain a large number of such charge-discharge cycles (hundreds or even thousands). The classification into primary and storage batteries is not rigorous because under certain conditions some primary battery may be recharged and storage batteries after a single use are sometimes discarded.
The silver-zinc battery is a storage battery: after discharge, it can be recharged by forcing through it an electric current in the reverse direction. In this process the two electrode reactions (1.3) and (1.4) as well as the overall reaction (1.2) go from right to left.
- cells. In the fuel-cell mode of operation, reactants are continuously fed into the cell (or battery) while reaction products are continuously removed. Hence, fuel cells (the more appropriate term of fuel battery is not commonly used) can deliver current continuously for a considerable length of time, which largely depends on external reactant storage.
Batteries are also classified according to their chemistry (their system), that is, the chemical nature of reactants. The above-mentioned battery with silver oxide as an oxidant at the positive electrode and metallic zinc as negative electrode is called "silver-zinc battery."
Sometimes other methods of classification are also used, for example, on the basis of the application (stationary or mobile batteries), shape (cylindrical, prismatic, disk-shape batteries), size (miniature, small-sized, medium-sized, or large-sized batteries), electrolyte type (alkaline, acidic, or neutral electrolyte, with liquid or solid (solidified), or molten salt electrolyte), voltage (low voltage or high voltage batteries), electric power generation (low power or high power batteries), and so on.
1.4 Thermodynamic Aspects
Each electrode j of a battery brought into contact with the electrolyte develops a certain electrode potential Ej. The concept of "potential" is an experimental, undefined parameter, that is, it has a real physical meaning and reflects a real physical phenomenon, but cannot be determined from experimental data (even from thought experiments). Only potential differences between the given electrode and another electrode (reference electrode) are measurable. (Similarly, the height of a certain geographic point is defined and can be measured only when referred to the height of another point, e.g., sea level). Values of electrode potentials are commonly referred to as the potential of the standard hydrogen electrode (SHE). Potentials of different electrodes can be either negative (i.e., more negative than the potential of the SHE) or positive. The OCV of a battery U is the potential difference between the positive electrode and the negative electrode:
1.5According to this definition, the OCV is always positive (provided the potentials of both electrodes are referred to the same reference electrode).
Thermodynamically, electrode reactions can be either reversible or irreversible. In case of a reversible reaction, the electrode potential is called reversible (thermodynamic electrode potential). The corresponding OCV is traditionally called "electromotive force" (EMF) and is denoted as e.
The EMF of a battery with reversible electrodes can be defined by the thermodynamic relation
1.6where ?G is the difference of the Gibbs energy G during the current-producing reaction-the difference of the Gibbs energies of all reactants and...
Systemvoraussetzungen
Dateiformat: ePUB
Kopierschutz: Adobe-DRM (Digital Rights Management)
Systemvoraussetzungen:
- Computer (Windows; MacOS X; Linux): Installieren Sie bereits vor dem Download die kostenlose Software Adobe Digital Editions (siehe E-Book Hilfe).
- Tablet/Smartphone (Android; iOS): Installieren Sie bereits vor dem Download die kostenlose App Adobe Digital Editions oder die App PocketBook (siehe E-Book Hilfe).
- E-Book-Reader: Bookeen, Kobo, Pocketbook, Sony, Tolino u.v.a.m. (nicht Kindle)
Das Dateiformat ePUB ist sehr gut für Romane und Sachbücher geeignet – also für „fließenden” Text ohne komplexes Layout. Bei E-Readern oder Smartphones passt sich der Zeilen- und Seitenumbruch automatisch den kleinen Displays an.
Mit Adobe-DRM wird hier ein „harter” Kopierschutz verwendet. Wenn die notwendigen Voraussetzungen nicht vorliegen, können Sie das E-Book leider nicht öffnen. Daher müssen Sie bereits vor dem Download Ihre Lese-Hardware vorbereiten.
Bitte beachten Sie: Wir empfehlen Ihnen unbedingt nach Installation der Lese-Software diese mit Ihrer persönlichen Adobe-ID zu autorisieren!
Weitere Informationen finden Sie in unserer E-Book Hilfe.