1.3.10 Electrochemistry Name Symbol Definition SI Unit Notes
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Nernst Equation in Electrochemistry the Nernst Equation Gives the Reduction Potential of a Half‐Cell in Equilibrium
Nernst equation In electrochemistry the Nernst equation gives the reduction potential of a half‐cell in equilibrium. In further cases, it can also be used to determine the emf (electromotive force) for a full electrochemical cell. (half‐cell reduction potential) (total cell potential) where Ered is the half‐cell reduction potential at a certain T o E red is the standard half‐cell reduction potential Ecell is the cell potential (electromotive force) o E cell is the standard cell potential at a certain T R is the universal gas constant: R = 8.314472(15) JK−1mol−1 T is the absolute temperature in Kelvin a is the chemical activity for the relevant species, where aRed is the reductant and aOx is the oxidant F is the Faraday constant; F = 9.64853399(24)×104 Cmol−1 z is the number of electrons transferred in the cell reaction or half‐reaction Q is the reaction quotient (e.g. molar concentrations, partial pressures …) As the system is considered not to have reached equilibrium, the reaction quotient Q is used instead of the equilibrium constant k. The electrochemical series is used to determine the electrochemical potential or the electrode potential of an electrochemical cell. These electrode potentials are measured relatively to the standard hydrogen electrode. A reduced member of a couple has a thermodynamic tendency to reduce the oxidized member of any couple that lies above it in the series. The standard hydrogen electrode is a redox electrode which forms the basis of the thermodynamic scale of these oxidation‐ reduction potentials. For a comparison with all other electrode reactions, standard electrode potential E0 of hydrogen is defined to be zero at all temperatures. -
Chapter 4 Calculation of Standard Thermodynamic Properties of Aqueous Electrolytes and Non-Electrolytes
Chapter 4 Calculation of Standard Thermodynamic Properties of Aqueous Electrolytes and Non-Electrolytes Vladimir Majer Laboratoire de Thermodynamique des Solutions et des Polymères Université Blaise Pascal Clermont II / CNRS 63177 Aubière, France Josef Sedlbauer Department of Chemistry Technical University Liberec 46117 Liberec, Czech Republic Robert H. Wood Department of Chemistry and Biochemistry University of Delaware Newark, DE 19716, USA 4.1 Introduction Thermodynamic modeling is important for understanding and predicting phase and chemical equilibria in industrial and natural aqueous systems at elevated temperatures and pressures. Such systems contain a variety of organic and inorganic solutes ranging from apolar nonelectrolytes to strong electrolytes; temperature and pressure strongly affect speciation of solutes that are encountered in molecular or ionic forms, or as ion pairs or complexes. Properties related to the Gibbs energy, such as thermodynamic equilibrium constants of hydrothermal reactions and activity coefficients of aqueous species, are required for practical use by geologists, power-cycle chemists and process engineers. Derivative properties (enthalpy, heat capacity and volume), which can be obtained from calorimetric and volumetric experiments, are useful in extrapolations when calculating the Gibbs energy at conditions remote from ambient. They also sensitively indicate evolution in molecular interactions with changing temperature and pressure. In this context, models with a sound theoretical basis are indispensable, describing with a limited number of adjustable parameters all thermodynamic functions of an aqueous system over a wide range of temperature and pressure. In thermodynamics of hydrothermal solutions, the unsymmetric standard-state convention is generally used; in this case, the standard thermodynamic properties (STP) of a solute reflect its interaction with the solvent (water), and the excess properties, related to activity coefficients, correspond to solute-solute interactions. -
Notation for States and Processes, Significance of the Word Standard in Chemical Thermodynamics, and Remarks on Commonly Tabulated Forms of Thermodynamic Functions
Pure &Appl.Chem.., Vol.54, No.6, pp.1239—1250,1982. 0033—4545/82/061239—12$03.00/0 Printed in Great Britain. Pergamon Press Ltd. ©1982IUPAC INTERNATIONAL UNION OF PURE AND APPLIED CHEMISTRY PHYSICAL CHEMISTRY DIVISION COMMISSION ON THERMODYNAMICS* NOTATION FOR STATES AND PROCESSES, SIGNIFICANCE OF THE WORD STANDARD IN CHEMICAL THERMODYNAMICS, AND REMARKS ON COMMONLY TABULATED FORMS OF THERMODYNAMIC FUNCTIONS (Recommendations 1981) (Appendix No. IV to Manual of Symbols and Terminology for Physicochemical Quantities and Units) Prepared for publication by J. D. COX, National Physical Laboratory, Teddington, UK with the assistance of a Task Group consisting of S. ANGUS, London; G. T. ARMSTRONG, Washington, DC; R. D. FREEMAN, Stiliwater, OK; M. LAFFITTE, Marseille; G. M. SCHNEIDER (Chairman), Bochum; G. SOMSEN, Amsterdam, (from Commission 1.2); and C. B. ALCOCK, Toronto; and P. W. GILLES, Lawrence, KS, (from Commission 11.3) *Membership of the Commission for 1979-81 was as follows: Chairman: M. LAFFITTE (France); Secretary: G. M. SCHNEIDER (FRG); Titular Members: S. ANGUS (UK); G. T. ARMSTRONG (USA); V. A. MEDVEDEV (USSR); Y. TAKAHASHI (Japan); I. WADSO (Sweden); W. ZIELENKIEWICZ (Poland); Associate Members: H. CHIHARA (Japan); J. F. COUNSELL (UK); M. DIAZ-PENA (Spain); P. FRANZOSINI (Italy); R. D. FREEMAN (USA); V. A. LEVITSKII (USSR); 0.SOMSEN (Netherlands); C. E. VANDERZEE (USA); National Representatives: J. PICK (Czechoslovakia); M. T. RATZSCH (GDR). NOTATION FOR STATES AND PROCESSES, SIGNIFICANCE OF THE WORD STANDARD IN CHEMICAL THERMODYNAMICS, AND REMARKS ON COMMONLY TABULATED FORMS OF THERMODYNAMIC FUNCTIONS SECTION 1. INTRODUCTION The main IUPAC Manual of symbols and terminology for physicochemical quantities and units (Ref. -
Electrode Reactions and Kinetics
CHEM465/865, 2004-3, Lecture 14-16, 20 th Oct., 2004 Electrode Reactions and Kinetics From equilibrium to non-equilibrium : We have a cell, two individual electrode compartments, given composition, molar reaction Gibbs free ∆∆∆ energy as the driving force, rG , determining EMF Ecell (open circuit potential) between anode and cathode! In other words: everything is ready to let the current flow! – Make the external connection through wires. Current is NOT determined by equilibrium thermodynamics (i.e. by the composition of the reactant mixture, i.e. the reaction quotient Q), but it is controlled by resistances, activation barriers, etc Equilibrium is a limiting case – any kinetic model must give the correct equilibrium expressions). All the involved phenomena are generically termed ELECTROCHEMICAL KINETICS ! This involves: Bulk diffusion Ion migration (Ohmic resistance) Adsorption Charge transfer Desorption Let’s focus on charge transfer ! Also called: Faradaic process . The only reaction directly affected by potential! An electrode reaction differs from ordinary chemical reactions in that at least one partial reaction must be a charge transfer reaction – against potential-controlled activation energy, from one phase to another, across the electrical double layer. The reaction rate depends on the distributions of species (concentrations and pressures), temperature and electrode potential E. Assumption used in the following: the electrode material itself (metal) is inert, i.e. a catalyst. It is not undergoing any chemical transformation. It is only a container of electrons. The general question on which we will focus in the following is: How does reaction rate depend on potential? The electrode potential E of an electrode through which a current flows differs from the equilibrium potential Eeq established when no current flows. -
Integrated Chemical Microsensor Systems in CMOS Technology by A
microtechnology and mems microtechnology and mems Series Editor: H. Baltes H. Fujita D. Liepmann The series Microtechnology and MEMS comprises text books, monographs, and state-of-the-art reports in the very active field of microsystems and microtech- nology. Written by leading physicists and engineers, the books describe the basic science, device design, and applications. They will appeal to researchers, engineers, and advanced students. Mechanical Microsensors By M. Elwenspoek and R. Wiegerink CMOS Cantilever Sensor Systems Atomic Force Microscopy and Gas Sensing Applications By D. Lange, O. Brand, and H. Baltes Micromachines as Tools for Nanotechnology Editor: H. Fujita Modelling of Microfabrication Systems By R. Nassar and W. Dai Laser Diode Microsystems By H. Zappe Silicon Microchannel Heat Sinks Theories and Phenomena By L. Zhang, K.E. Goodson, and T.W. Kenny Shape Memory Microactuators By M. Kohl Force Sensors for Microelectronic Packaging Applications By J. Schwizer, M. Mayer and O. Brand Integrated Chemical Microsensor Systems in CMOS Technology By A. Hierlemann A. Hierlemann Integrated Chemical Microsensor Systems in CMOS Technology With 125 Figures 123 Professor Dr. Andreas Hierlemann Physical Electronics Laboratory ETH Hoenggerberg, HPT-H 4.2, IQE 8093 Zurich Switzerland Email: [email protected] Series Editors: Professor Dr. H. Baltes ETH Zürich, Physical Electronics Laboratory ETH Hoenggerberg, HPT-H6, 8093 Zürich, Switzerland Professor Dr. Hiroyuki Fujita University of Tokyo, Institute of Industrial Science 4-6-1 Komaba, Meguro-ku, Tokyo 153-8505, Japan Professor Dr. Dorian Liepmann University of California, Department of Bioengineering 466 Evans Hall, #1762, Berkeley, CA 94720-1762, USA ISSN 1439-6599 ISBN 3-540-23782-8 Springer Berlin Heidelberg New York LibraryofCongressControlNumber:2004114045 This work is subject to copyright. -
Quantum Mechanics Electromotive Force
Quantum Mechanics_Electromotive force . Electromotive force, also called emf[1] (denoted and measured in volts), is the voltage developed by any source of electrical energy such as a batteryor dynamo.[2] The word "force" in this case is not used to mean mechanical force, measured in newtons, but a potential, or energy per unit of charge, measured involts. In electromagnetic induction, emf can be defined around a closed loop as the electromagnetic workthat would be transferred to a unit of charge if it travels once around that loop.[3] (While the charge travels around the loop, it can simultaneously lose the energy via resistance into thermal energy.) For a time-varying magnetic flux impinging a loop, theElectric potential scalar field is not defined due to circulating electric vector field, but nevertheless an emf does work that can be measured as a virtual electric potential around that loop.[4] In a two-terminal device (such as an electrochemical cell or electromagnetic generator), the emf can be measured as the open-circuit potential difference across the two terminals. The potential difference thus created drives current flow if an external circuit is attached to the source of emf. When current flows, however, the potential difference across the terminals is no longer equal to the emf, but will be smaller because of the voltage drop within the device due to its internal resistance. Devices that can provide emf includeelectrochemical cells, thermoelectric devices, solar cells and photodiodes, electrical generators,transformers, and even Van de Graaff generators.[4][5] In nature, emf is generated whenever magnetic field fluctuations occur through a surface. -
Fundamentals of Electrochemistry
ffirs.qxd 10/29/2005 11:56 AM Page iii FUNDAMENTALS OF ELECTROCHEMISTRY Second Edition V. S. BAGOTSKY A. N. Frumkin Institute of Physical Chemistry and Electrochemistry Russian Academy of Sciences Moscow, Russia Sponsored by THE ELECTROCHEMICAL SOCIETY, INC. Pennington, New Jersey A JOHN WILEY & SONS, INC., PUBLICATION ftoc.qxd 10/29/2005 12:01 PM Page xiv ffirs.qxd 10/29/2005 11:55 AM Page i FUNDAMENTALS OF ELECTROCHEMISTRY ffirs.qxd 10/29/2005 11:55 AM Page ii THE ELECTROCHEMICAL SOCIETY SERIES The Electrochemical Society 65 South Main Street Pennington, NJ 08534-2839 http://www.electrochem.org A complete list of the titles in this series appears at the end of this volume. ffirs.qxd 10/29/2005 11:56 AM Page iii FUNDAMENTALS OF ELECTROCHEMISTRY Second Edition V. S. BAGOTSKY A. N. Frumkin Institute of Physical Chemistry and Electrochemistry Russian Academy of Sciences Moscow, Russia Sponsored by THE ELECTROCHEMICAL SOCIETY, INC. Pennington, New Jersey A JOHN WILEY & SONS, INC., PUBLICATION ffirs.qxd 10/29/2005 11:56 AM Page iv Copyright © 2006 by John Wiley & Sons, Inc. All rights reserved Published by John Wiley & Sons, Inc., Hoboken, New Jersey Published simultaneously in Canada No part of this publication may be reproduced, stored in a retrieval system, or transmitted in any form or by any means, electronic, mechanical, photocopying, recording, scanning, or otherwise, except as permitted under Section 107 or 108 of the 1976 United States Copyright Act, without either the prior written permission of the Publisher, or authorization through payment of the appropriate per-copy fee to the Copyright Clearance Center, Inc., 222 Rosewood Drive, Danvers, MA 01923, (978) 750-8400, fax (978) 750-4470, or on the web at www.copyright.com. -
Elements of Electrochemistry
Page 1 of 8 Chem 201 Winter 2006 ELEM ENTS OF ELEC TROCHEMIS TRY I. Introduction A. A number of analytical techniques are based upon oxidation-reduction reactions. B. Examples of these techniques would include: 1. Determinations of Keq and oxidation-reduction midpoint potentials. 2. Determination of analytes by oxidation-reductions titrations. 3. Ion-specific electrodes (e.g., pH electrodes, etc.) 4. Gas-sensing probes. 5. Electrogravimetric analysis: oxidizing or reducing analytes to a known product and weighing the amount produced 6. Coulometric analysis: measuring the quantity of electrons required to reduce/oxidize an analyte II. Terminology A. Reduction: the gaining of electrons B. Oxidation: the loss of electrons C. Reducing agent (reductant): species that donates electrons to reduce another reagent. (The reducing agent get oxidized.) D. Oxidizing agent (oxidant): species that accepts electrons to oxidize another species. (The oxidizing agent gets reduced.) E. Oxidation-reduction reaction (redox reaction): a reaction in which electrons are transferred from one reactant to another. 1. For example, the reduction of cerium(IV) by iron(II): Ce4+ + Fe2+ ! Ce3+ + Fe3+ a. The reduction half-reaction is given by: Ce4+ + e- ! Ce3+ b. The oxidation half-reaction is given by: Fe2+ ! e- + Fe3+ 2. The half-reactions are the overall reaction broken down into oxidation and reduction steps. 3. Half-reactions cannot occur independently, but are used conceptually to simplify understanding and balancing the equations. III. Rules for Balancing Oxidation-Reduction Reactions A. Write out half-reaction "skeletons." Page 2 of 8 Chem 201 Winter 2006 + - B. Balance the half-reactions by adding H , OH or H2O as needed, maintaining electrical neutrality. -
Galvanic Cell Notation • Half-Cell Notation • Types of Electrodes • Cell
Galvanic Cell Notation ¾Inactive (inert) electrodes – not involved in the electrode half-reaction (inert solid conductors; • Half-cell notation serve as a contact between the – Different phases are separated by vertical lines solution and the external el. circuit) 3+ 2+ – Species in the same phase are separated by Example: Pt electrode in Fe /Fe soln. commas Fe3+ + e- → Fe2+ (as reduction) • Types of electrodes Notation: Fe3+, Fe2+Pt(s) ¾Active electrodes – involved in the electrode ¾Electrodes involving metals and their half-reaction (most metal electrodes) slightly soluble salts Example: Zn2+/Zn metal electrode Example: Ag/AgCl electrode Zn(s) → Zn2+ + 2e- (as oxidation) AgCl(s) + e- → Ag(s) + Cl- (as reduction) Notation: Zn(s)Zn2+ Notation: Cl-AgCl(s)Ag(s) ¾Electrodes involving gases – a gas is bubbled Example: A combination of the Zn(s)Zn2+ and over an inert electrode Fe3+, Fe2+Pt(s) half-cells leads to: Example: H2 gas over Pt electrode + - H2(g) → 2H + 2e (as oxidation) + Notation: Pt(s)H2(g)H • Cell notation – The anode half-cell is written on the left of the cathode half-cell Zn(s) → Zn2+ + 2e- (anode, oxidation) + – The electrodes appear on the far left (anode) and Fe3+ + e- → Fe2+ (×2) (cathode, reduction) far right (cathode) of the notation Zn(s) + 2Fe3+ → Zn2+ + 2Fe2+ – Salt bridges are represented by double vertical lines ⇒ Zn(s)Zn2+ || Fe3+, Fe2+Pt(s) 1 + Example: A combination of the Pt(s)H2(g)H Example: Write the cell reaction and the cell and Cl-AgCl(s)Ag(s) half-cells leads to: notation for a cell consisting of a graphite cathode - 2+ Note: The immersed in an acidic solution of MnO4 and Mn 4+ reactants in the and a graphite anode immersed in a solution of Sn 2+ overall reaction are and Sn . -
Redox Potentials As Reactivity Descriptors in Electrochemistry José H
Chapter Redox Potentials as Reactivity Descriptors in Electrochemistry José H. Zagal, Ingrid Ponce and Ruben Oñate Abstract A redox catalyst can be present in the solution phase or immobilized on the electrode surface. When the catalyst is present in the solution phase the process can proceed via inner- (with bond formation, chemical catalysis) or outer-sphere mechanisms (without bond formation, redox catalysis). For the latter, log k is linearly proportional to the redox potential of the catalysts, E°. In contrast, for inner-sphere catalyst, the values of k are much higher than those predicted by the redox potential of the catalyst. The behaviour of these catalysts when they are confined on the electrode surface is completely different. They all seem to work as inner-sphere catalysts where a crucial step is the formation of a bond between the active site and the target molecule. Plots of (log i)E versus E° give linear or volcano correlations. What is interesting in these volcano correlations is that the falling region corresponding to strong adsorption of intermediates to the active sites is not necessarily attributed to a gradual surface occupation of active sites by intermedi- ates (Langmuir isotherm) but rather to a gradual decrease in the amount of M(II) active sites which are transformed into M(III)OH inactive sites due to the applied potential. Keywords: redox potential, reactivity descriptors, redox catalysis, chemical catalysis, linear free-energy correlations, volcano correlations 1. Introduction Predicting the rate of chemical processes on the basis of thermodynamic infor- mation is of fundamental importance in all areas of chemistry including biochemis- try, coordination chemistry and especially electrochemistry [1]. -
Lecture 03 Electrochemical Kinetics
EMA4303/5305 Electrochemical Engineering Lecture 03 Electrochemical Kinetics Dr. Junheng Xing, Prof. Zhe Cheng Mechanical & Materials Engineering Florida International University Electrochemical Kinetics Electrochemical kinetics “Electrochemical kinetics is a field of electrochemistry studying the rate of electrochemical processes. Due to electrochemical phenomena unfolding at the interface between an electrode and an electrolyte, there are accompanying phenomena to electrochemical reactions which contribute to the overall reaction rate.” (Wikipedia) “The main goal of the electrochemical kinetics is to find a relationship between the electrode overpotential and current density due to an applied potential.” (S. N. Lvov) Main contents of this lecture . Overpotential (η) . Charge transfer overpotential − Butler-Volmer equation − Tafel equation . Mass transfer overpotential EMA 5305 Electrochemical Engineering Zhe Cheng (2017) 3 Electrochemical Kinetics 2 Cell Potential in Different Modes Electrolytic cell (EC) Galvanic cell (GC) 푬푬푸 = 푰 (푹풆풙풕 + 푹풊풏풕) 푬푨풑풑풍풊풆풅 = 푬푬푸 + 푰푹풊풏풕 푬풆풙풕 = 푬푬푸 − 푰푹풊풏풕= IRext EMA 5305 Electrochemical Engineering Zhe Cheng (2017) 3 Electrochemical Kinetics 3 Cell Potential-Current Dependence . 푹풊풏풕 represents the total internal resistance of the cell, which is usually not zero, in most cases. Therefore, the difference between cell equilibrium potential and apparent potential is proportional to the current passing through the cell. Cell potential-current dependences EMA 5305 Electrochemical Engineering Zhe Cheng (2017) 3 Electrochemical Kinetics 4 Overpotential (η) Overpotential for a single electrode . The difference between the actual potential (measured) for an electrode, E, and the equilibrium potential for that electrode, 푬푬푸, is called the overpotential of that electrode, 휼 = 푬 −푬푬푸, which could be either positive or negative, depending on the direction of the half (cell) reaction. -
Thermodynamics the Study of the Transformations of Energy from One Form Into Another
Thermodynamics the study of the transformations of energy from one form into another First Law: Heat and Work are both forms of Energy. in any process, Energy can be changed from one form to another (including heat and work), but it is never created or distroyed: Conservation of Energy Second Law: Entropy is a measure of disorder; Entropy of an isolated system Increases in any spontaneous process. OR This law also predicts that the entropy of an isolated system always increases with time. Third Law: The entropy of a perfect crystal approaches zero as temperature approaches absolute zero. ©2010, 2008, 2005, 2002 by P. W. Atkins and L. L. Jones ©2010, 2008, 2005, 2002 by P. W. Atkins and L. L. Jones A Molecular Interlude: Internal Energy, U, from translation, rotation, vibration •Utranslation = 3/2 × nRT •Urotation = nRT (for linear molecules) or •Urotation = 3/2 × nRT (for nonlinear molecules) •At room temperature, the vibrational contribution is small (it is of course zero for monatomic gas at any temperature). At some high temperature, it is (3N-5)nR for linear and (3N-6)nR for nolinear molecules (N = number of atoms in the molecule. Enthalpy H = U + PV Enthalpy is a state function and at constant pressure: ∆H = ∆U + P∆V and ∆H = q At constant pressure, the change in enthalpy is equal to the heat released or absorbed by the system. Exothermic: ∆H < 0 Endothermic: ∆H > 0 Thermoneutral: ∆H = 0 Enthalpy of Physical Changes For phase transfers at constant pressure Vaporization: ∆Hvap = Hvapor – Hliquid Melting (fusion): ∆Hfus = Hliquid –