cl ELECTROCHEMICAL BEHAVIOUR OF PLATINUM-IRIDIUM ANODES BY DONALD ARTHUR WENSLEY B.A.Sc, University of British Columbia, 1970 A THESIS SUBMITTED IN PARTIAL FULFILMENT OF THE REQUIREMENTS FOR THE DEGREE OF MASTER OF APPLIED SCIENCE in the Department of METALLURGY . We accept this thesis as conforming to the required standard THE UNIVERSITY OF BRITISH COLUMBIA June, 1973 In presenting this thesis in partial fulfilment of the requirements for an advanced degree at the University of British Columbia, I agree that the Library shall make it freely available for reference and study. I further agree that permission for extensive copying of this thesis for scholarly purposes may be granted by the Head of my Department or by his representatives. It is understood that copying or publication of this thesis for financial gain shall not be allowed without my written permission. Department of Metallurgy The University of British Columbia Vancouver 8, Canada Date October 4, 1973 ii ABSTRACT This thesis considers the electrochemistry of platinum- iridium electrodes in both sulphate- and chloride-containing electro lytes at 20 - 25°C. Both wire electrodes of appropriate alloy composi tions and titanium-substrate electrodes were employed. Polarization curves were obtained, and a technique for measuring the surface area of the electrodes was employed in order to determine the effect of potentiostatic electrolysis on the electrochemically active area. The wire alloy electrodes showed polarization behaviour in 1M NaCl; pH 2 identical to that of platinum electrodes, indicating that iridium is not effective in reducing the passivation of these electrodes even with up to 25% alloy content. The coated electrodes showed irreversible surface area losses in both sulphate and chloride electrolytes, with the latter pro ducing significant reductions after very short polarization times. It is suggested that oxidation of the substrate leading to electrical iso lation of coating plates is responsible for the area decay. i ii TABLE OF CONTENTS Page 1. INTRODUCTION 1 2. LITERATURE SURVEY AND THEORETICAL CONSIDERATION 5 2.1 ELECTRODE PRETREATMENT AND ACTIVATION 6 2.1.1 Nature of the Problem 6 2.1.2 Methods of Pretreatment and Activation .... 9 2.1.3 Mechanisms of Activation of Noble Metal Electrodes 11 2.1.3.1 Surface Area Increases 11 2.1.3.2 Active Surface Structure 14 2.1.3.3 Active Oxidized Surface 18 2.1.3.4 Active Reduced Surface 20 2.1.3.5 Activity Induced by Dermasorption of Oxygen 24 2.1.3.6 Altered Electronic Properties .... 27 2.1.3.7 Impurity Removal 29 2.1.4 Summary 32 2.2 SURFACE AREA OF NOBLE METAL ELECTRODES 33 2.2.1 Bases for Electrochemical Surface Area Measurement 33 2.2.1.1 Complications due to Simultaneous Processes 34 2.2.1.2 Compensation for Double Layer Charging 36 2.2.1.3 Monolayer Formation 37 2.2.1.4 Absorption 38 iv Page 2.2.1.5 Surface Atom Density 40 2.2.2 Procedures for Surface Area Measurement ... 42 2.2.2.1 Potential Sweep Techniques 42 2.2.2.2 \Galvanostatic Charge Techniques .. 44 2.2.3 Summary 46 2.3 ELECTROLYSIS OF CHLORIDE SOLUTIONS 48 2.3.1 Polarization of Smooth Noble Metal Anodes . 50 2.3.2 Polarization of Titanium-Substrate Anodes . 58 2.3.2.1 Behaviour of Titanium 59 2.3.2.2 Coupling of Platinum Metals with Titanium 61 2.3.2.3 Polarization Characteristics 63 2.3.3 Summary 64 2.4 DISSOLUTION OF THE NOBLE METALS 65 2.4.1 The Active Dissolution of the Noble Metals 66 2.4.2 Dissolution with Oxygen Participation 72 2.4.3 Dissolution During Activation 78 2.4.4 Degradation of Noble Metal Coatings 83 2.4.4.1 Degradation as a Result of Coat ing Undermining 83 2.4.4.2 Other Causes of Coating Loss 86 2.4.5 Summary 87 2.5 RELATION TO AIMS OF PRESENT WORK 88 3. EXPERIMENTAL 93 3.1 ELECTRODES 93 V Page 3.2 ELECTROLYTES 95 3.3 CELLS 96 3.4 PROCEDURES 100 3.4.1 Anodic Galvanostatic Measurements 100 3.4.2 Anodic Potentiostatic Measurements 101 3.4.3 Surface Area Measurements 102 3.4.4 Observation of Electrode Surfaces 105 4. RESULTS 106 4.1 GALVANOSTATIC POLARIZATION CURVES 106 4.2 POTENTIOSTATIC POLARIZATION CURVES 119 4.3 CHANGE OF SURFACE AREA WITH POTENTIOSTATIC ANODIZATION 122 4.4 OBSERVATIONS OF ELECTRODE SURFACES 132 5. DISCUSSION 140 5.1 ANODIC GALVANOSTATIC MEASUREMENTS 140 5.2 ANODIC POTENTIOSTATIC MEASUREMENTS 142 5.3 SURFACE AREA CHANGES 143 6. PROPOSALS FOR FUTURE WORK 148 BIBLIOGRAPHY 153 APPENDIXES 163 APPENDIX I Electrode Surface Conditions 163 APPENDIX II Surface Area Measurement 167 APPENDIX III X-ray Diffraction Results 170 vi LIST OF TABLES TABLE Page 1. Hydrogen and oxygen monolayer charges for platinum and iridium electrodes 41 2. Electrode areas measured after determination of the polarization curves 109 3. Tafel parameters for Pt and Pt/Ir wire electrodes for the lower Tafel region of the polarization curves in 1M NaCl; pH 2 I ll 4. Tafel parameters for Pt and Pt/Ir wire electrodes for the ascending and descending upper Tafel regions of the polarization curve in 1M NaCl; pH 2 I ll 5. Passivation data for Pt and Pt/Ir wire electrodes from polarization curves in 1M NaCl; pH 2 113 6. Surface area changes as a result of potentiostatic polarization in chloride electrolytes with Pt/30 Ir- Ti electrodes 118 7. Effect of potentiostatic polarization in 1M ^SO^ on the surface area of Pt/30 Ir-Ti electrodes 119 8. Effect of treatment in aqua regia on the surface area of Pt/30 Ir-Ti electrodes 120 9. Effects of "activation" procedures on the surface area of Pt/30 Ir-Ti electrodes 126 10. Surface conditions of wire electrodes used in galvano- static polarization experiments 163 11. Surface conditions of coated electrodes used in potent iostatic polarization and surface area determinations .. 165 12. Identification of X-ray diffraction peaks for a new titanium substrate electrode 170 13. Identification of X-ray diffraction peaks for a used titanium substrate electrode (3 weeks in 1M H„S0, at .2 A/ft.2 and 40°C) 171 vii LIST OF FIGURES FIGURE Page 1. Galvanostatic cell 98 2. Cell for surface area measurement 99 3. Galvanostatic polarization curve for platinum wire electrode in helium-saturated 1M NaCl; pH 2 109 4. Galvanostatic polarization curve for platinum/5% iridium wire electrode in helium-saturated 1M NaCl; pH 2 110 5. Galvanostatic polarization curve for platinum/10% iridium wire electrode in helium-saturated 1M NaCl; pH 2 I ll 6. Galvanostatic polarization curve for platinum/20% iridium wire electrode in helium-saturated 1M NaCl; pH 2 112 7. Galvanostatic polarization curve for platinum/25% iridium wire electrode in helium-saturated 1M NaCl; pH 2 113 8. Potentiostatic polarization curve for Pt/30 Ir-Ti in unstirred 1M l^SO^ 120 9. Potentiostatic polarization curve for Pt/30 Ir-Ti in unstirred 1M NaCl; pH 2 121 10. Current/time relations for potentiostatic polarization with Pt/30 Ir-Ti electrodes at 1800 mV (S.C.E.) in various electrolytes 127 11. Current/time relations for a Pt/30 Ir-Ti electrode for potentiostatic electrolysis of IM H^SO^ at 1800 mV and 25°C, after various pretreatment times in aqua regia .. 128 12. Current/time relations for a Pt/30 Ir-Ti electrode for potentiostatic electrolysis of 1M H^SO^ at 2000 mV and 25°C, before and after potentiostatxc electrolysis of 1M NaCl; pH 2 129 13. S.E.M. Observation of Pt/30 Ir-Ti surfaces 134 14. S.E.M. Observation of used Pt/30 Ir-Ti electrodes 135 viii FIGURE Page 15. S.E.M. Observation of platinum sheet 136 16. S.E.M. Observation of platinum wire electrodes 137 17. S.E.M. Observation of Pt/25 Ir wire electrodes 138 18. E.P. Observation of new Pt/30 Ir-Ti electrode 139 19. Schematic representation of the potential history of a wire electrode used in galvanostatic polarization experiments ; 164 20. Schematic representation of the potential hostory of a coated electrode used in potentiostatic polarization experiments 166 21. Representation of a typical anodic charge curve in de- aerated 1M I^SO^ at 20°C, showing constructions for determining oxygen deposition charge 169 I wish to thank Dr. I.H. Warren for his guidance throughout the course of this research, the staff of the Science Division, Main Library, "U.B.C. for their invaluable aid, and my wife, Darlene, for her enduring patience. Financial support from the National Research Council and International Nickel Company is also acknowledged.
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