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Cell Notation Practical Galvanic Cells -Batteries
Basic Redox Vocabulary • Write reactions for each of the following: • oxidation of metallic nickel by BiO+ • reduction of Zn2+ by hydroxide ion • reaction of Fe 2+ with Hg2+ 2+ • reaction of Cd with NO2 • AgI acting as an oxidizing agent toward Sn 2+ • What’s wrong with • The oxidation of Cr by Cl- • The reduction of Co 2+ by Ag+ Cell Notation • As was noted earlier, galvanic cells normally consist of two distinct regions, one housing the oxidation half and the other the reduction half. There is a simplified notation form that allows one to represent the cell easily( text p 798- 799). • The oxidation is written on the left and the reduction on the right. starting with the anode material and ending with the cathode material. • phase boundaries represented with single vertical lines “ |” • the physical separation between the two half cells is a double v ertical line “||” if it’s a salt bridge and with a single broken vertical line, “!”, if it’s a liquid junction • within each have cell, the species are written in a reactant-product order, separated by commas if they are in the same phase. Acid/base components should be included • The electrode material may be actively participating in the redox chemistry (active electrode) or merely providing surface for the electron transfer (passive or inert electrode, usually graphite or Pt) • Represent the following as galvanic cells(assume the reactions are spontaneous as written) • Tl(s) + Cd 2+ ó Tl + + Cd(s) - 2+ 2+ • Pb(s) + MnO4 ó Pb + Mn (acid) 2+ 4+ • O2(g) + Sn ó H2O + Sn Practical Galvanic Cells -batteries • Batteries represent the most common application of the electrochemical cell. -
Acid-Base Concentration Cell for Electric Power Generation
Europaisches Patentamt J European Patent Office 0 Publication number: 0613199 A1 Office europeen des brevets EUROPEAN PATENT APPLICATION 0 Application number: 94101725.3 0 int. CI A H01M 8/22, H01M 14/00, H01 M 6/24 0 Date of filing: 04.02.94 0 Priority: 22.02.93 US 21417 0 Applicant: Hughes Aircraft Company 7200 Hughes Terrace, 0 Date of publication of application: P.O. Box 80028 31.08.94 Bulletin 94/35 Los Angeles, California 90080-0028 (US) 0 Designated Contracting States: 0 Inventor: Ludwig, Frank A. DE FR GB 29443 Whitley Collins Rancho Palos Verdes, California (US) 0 Representative: KUHNEN, WACKER & PARTNER Alois-Steinecker-Strasse 22 D-85354 Freising (DE) 0 Acid-base concentration cell for electric power generation. 0 An electric power system particularly adapted for use in powering the electric motor or motors used in the drive train of an electric vehicle. The power system includes a power cell which is a continuous flow concentration cell which utilizes the electrochemical reaction between an acid electrolyte (11) and a base electrolyte (13) to produce electrical energy. Both the acid and base electrolyte utilized in the power cell are kept in external reservoirs (10,12). The use of external reservoirs for the electrolytes provides for increases in the energy of the system which is only limited by the size of the reservoirs. Recharging of the system is quickly and conveniently accomplished by recharging the reservoirs with fresh electrolyte, or by electrically recharging the system. Rank Xerox (UK) Business Services (3. 10/3.09/3.3.4) EP 0 613 199 A1 BACKGROUND OF THE INVENTION 1_. -
Voltaic Cells
Voltaic Cells Tro Chapter 19 – Electrochemistry 19.3 Voltaic(or Galvanic) Cells: Generating Electricity from Spontaneous Chemical Reactions Electric Current Flowing Directly Between Atoms Tro, Chemistry: A Molecular Approach 2 Electrochemical Cells Voltaic (Galvanic) ΔG < 0 to Electrolytic Δ G > 0 uses electrical generate electrical energy. energy to drive non-spontaneous process. Electrochemical Cells • Oxidation and reduction half-reactions are kept separate in half-cells. • Electron flow through a wire along with ion flow through a solution constitutes an electric circuit. • It requires a conductive solid electrode to allow the transfer of electrons. – Through external circuit – Metal or graphite • Requires ion exchange between the Daniell Cell two half-cells of the system. – Electrolyte Definitions Anode Salt Bridge • Electrode where oxidation always occurs • An inverted, U-shaped tube containing a • More negatively charged electrode in strong electrolyte and connecting the two voltaic cell half-cells. • Typically made of metal that is oxidized Cathode • Electrode where reduction always occurs Potential Difference • More positively charged electrode in • The difference in potential energy voltaic cell between the reactants and products. • Typically metal that is produced by reduction (Caused by an electric field resulting from the charge difference on the two If the redox reaction involves the oxidation or electrodes.) reduction of an ion to a different oxidation state, or the oxidation or reduction of a gas, we Cell Potential (Ecell or emf) may use an inert electrode. • The potential difference between the anode and the cathode in a voltaic cell. • An inert electrode is one that not does participate in the reaction but just provides a surface on which the transfer of electrons can take place. -
Liquid Junction Potentials at Mixed Electrolyte Salt
LIQUID JUNCTION POTENTIALS AT MIXED ELECTROLYTE SALT BRIDGES. A Thesis 2ubmitted in Part-Fulfilment of the Requirements for the Degree of Master of Science of Rhodes University. BY NOEL PHILLIP FINKELSTEIN. RHODES UNIVERSITY, GRAHAli-1STmVN. September, 1956. ( i) ACKNOJLEDGJ:!Ji.fuNTS. It is with sincere gratitude that the following acknowledgements are made: DR . E.T. VE~DISR , M.Sc., (S.A.); Docteur es Sciences Physiques (France), for his able dir$ction, guidance, and constant encoura~ement. PROFESSOR W.F. BA~KER, B.Sc., Ph.D., F.R.I.C. F.n.s.s. Af., for his encouragement and interest. PHOFESSOR J.A. GLEDHILL , Ph.D., (S.A.), Ph.D., (Yale), for long hours of in valuable discussion. Mr. F. van der VI/A Tim, for his skilful and patient assistance with the technical aspects of the work. Mr. D.A. CLUR, B.Sc., (Hons.) for much in valuable discusssion, and many useful suggestions. Mrs. J. FINKELSTbiN, for her assistance with the clerical side of the pre paration of the thesis. Mr. H.T. DREYER, who was responsible for the diagrams. THE SOUTH AFRICAN COUNCIL FOH SCI~NTI?IC AND INDUSTRIAL RESJ:;AllCH for a grant held during this research. ( ii) CONTENTS . £ (( 'i j . AC KNO':-.ILED£}]-1ENTS (1) 1. GLOSSARY OF ABBREVIATIONS AND SYMBOLS. 1. 2. INTRODUCTimT. 3 . 3. CRITICAL SURVEY ON PREVIOUS WORK ON LIQUID JUNCTION POTEN~IALS. 5· 3.1. The Theory of Liquid Junction Pot- entials . 5· 3. 2. The ~l i m ination of the Error due to Liquid Junction Potentials . g. 3~3. The Measurement of Liquid Junction Potentials . -
A Novel Iron Chloride Red-Ox Concentration Flow Cell Battery (ICFB) Concept; Power and Electrode Optimization
energies Article A Novel Iron Chloride Red-Ox Concentration Flow Cell Battery (ICFB) Concept; Power and Electrode Optimization Robert Bock 1 , Björn Kleinsteinberg 2,3, Bjørn Selnes-Volseth 1 and Odne Stokke Burheim 1,* 1 Department of Energy and Process Engineering, Norwegian University of Science and Technology, NO-7491 Trondheim, Norway; [email protected] (R.B.); [email protected] (B.S.-V.) 2 Electrochemical Energy Conversion and Storage Systems Group, Institute for Power Electronics and Electrical Drives (ISEA), RWTH Aachen University, 52062 Aachen, Germany; [email protected] 3 Helmholtz Institute Münster (HI MS), IEK-12, Forschungszentrum Juelich, Corrensstrasse 46, 48149 Münster, Germany * Correspondence: [email protected] Abstract: For renewable energies to succeed in replacing fossil fuels, large-scale and affordable solutions are needed for short and long-term energy storage. A potentially inexpensive approach of storing large amounts of energy is through the use of a concentration flow cell that is based on cheap and abundant materials. Here, we propose to use aqueous iron chloride as a reacting solvent on carbon electrodes. We suggest to use it in a red-ox concentration flow cell with two compartments separated by a hydrocarbon-based membrane. In both compartments the red-ox couple of iron II and III reacts, oxidation at the anode and reduction at the cathode. When charging, a concentration difference between the two species grows. When discharging, this concentration difference between iron II and iron III is used to drive the reaction. In this respect it is a concentration driven flow cell Citation: Bock, R.; Kleinsteinberg, B.; redox battery using iron chloride in both solutions. -
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 . -
Chapter 13: Electrochemical Cells
March 19, 2015 Chapter 13: Electrochemical Cells electrochemical cell: any device that converts chemical energy into electrical energy, or vice versa March 19, 2015 March 19, 2015 Voltaic Cell -any device that uses a redox reaction to transform chemical potential energy into electrical energy (moving electrons) -the oxidizing agent and reducing agent are separated -each is contained in a half cell There are two half cells in a voltaic cell Cathode Anode -contains the SOA -contains the SRA -reduction reaction -oxidation takes place takes place - (-) electrode -+ electrode -anions migrate -cations migrate towards the anode towards cathode March 19, 2015 Electrons move through an external circuit from the anode to cathode Electricity is produced by the cell until one of the reactants is used up Example: A simple voltaic cell March 19, 2015 When designing half cells it is important to note the following: -each half cell needs an electrolyte and a solid conductor -the electrode and electrolyte cannot react spontaneously with each other (sometimes carbon and platinum are used as inert electrodes) March 19, 2015 There are two kinds of porous boundaries 1. Salt Bridge 2. Porous Cup · an unglazed ceramic cup · tube filled with an inert · separates solutions but electrolyte such as NaNO allows ions to pass 3 through or Na2SO4 · the ends are plugged so the solutions are separated, but ions can pass through Porous boundaries allow for ions to move between two half cells so that charge can be equalized between two half cells 2+ 2– electrolyte: Cu (aq), SO4 (aq) 2+ 2– electrolyte: Zn (aq), SO4 (aq) electrode: zinc electrode: copper March 19, 2015 Example: Metal/Ion Voltaic Cell V Co(s) Zn(s) Co2+ SO 2- 4 2+ SO 2- Zn 4 Example: A voltaic cell with an inert electrode March 19, 2015 Example Label the cathode, anode, electron movement, ion movement, and write the half reactions taking place at each half cell. -
Electrochemical Cells - Redox Reactions Can Be Used in a Controlled Manner to Make a Battery
Chapter 17 Worksheet #2 Name __________________________ Electrochemical Cells - Redox reactions can be used in a controlled manner to make a battery. A galvanic cell (voltaic cell or battery) converts the chemical energy of the reactants into electrical energy. BATTERY: Anode - AN OX, RED CAT Cathode - Salt Bridge - A tube containing a salt (such as KCl or NaNO3) solution that is used to connect two half-cells in an electrochemical cell; allows the passage of ions (maintains charge neutrality), but prevents the mixing of half-cell electrolytes. Shorthand notation for a galvanic cell: Zn(s)│Zn2+(aq)║Cu2+(aq)│Cu(s) where the anode is on the left, the cathode on the right, │ indicates the interface between the metal and solution, and ║ indicates the salt bridge. In many cells, the electrode itself does not react but serves only as a channel to direct electrons to or from the solution where a reaction involving other species takes place. The electrode itself is unaffected. Platinum and graphite are inert in most (but not all) electrochemical reactions. The Cu electrode could be replaced by a platinum or graphite electrode in the Zn/Cu battery: Zn(s)│Zn2+(aq)║Cu2+(aq)│Pt(s) Construct a battery from the reaction: Cr(s) + Pb2+(aq) Cr3+(aq) + Pb(s) Construct a galvanic cell using platinum electrodes and the reaction: - - + 2+ 10 Br (aq) + 2 MnO4 (aq) + 16 H (aq) 5 Br2(ℓ) + 2 Mn (aq) + 8 H2O(ℓ) A salt bridge is not required in a battery in which the reactants are physically separated from each other. -
Thin Films of Lithium Ion Conducting Garnets and Their Properties
Thin films of lithium ion conducting garnets and their properties dem Fachbereich Biologie und Chemie der Justus-Liebig-Universität Gießen vorgelegte Dissertation zur Erlangung des Grades Doktor der Naturwissenschaften – Dr. rer. nat. – von Jochen Reinacher geboren am 07.09.1984 Gießen 2014 II Dekan / Dean Prof. Dr. Holger Zorn 1. Gutachter / Reviewer Prof. Dr. Jürgen Janek 2. Gutachter / Reviewer Prof. Dr. Bruno K. Meyer Arbeit eingereicht: 10.06.2014 Tag der mündlichen Prüfung: 11.07.2014 III IV Abstract Different lithium ion conducting garnet-type thin films were prepared by pulsed laser deposition. Of these garnet-type thin films Li6BaLa2Ta2O12, cubic Li6.5La3Zr1.5Ta0.5O12 (additionally stabilized by Al2O3) and cubic Li7La3Zr2O12 stabilized by Ga2O3 were investigated in more detail. Conductivity measurements of these thin films performed in lateral geometry showed total conductivities of σ = 1.7∙10–6 S∙cm–1, σ = 2.9∙10–6 S∙cm–1 and σ = 1.2∙10–6 S∙cm–1, respectively. Electrochemical impedance spectroscopy was performed in axial geometry (orthogonal to the substrate), revealing conductivities of –5 –1 σ = 3.3∙10 S∙cm for Li6BaLa2Ta2O12 which is comparable to the bulk conductivity of –5 –1 Li6BaLa2Ta2O12 (σ = 4∙10 S∙cm ). The comparatively low lateral conductivity of the garnet-type material could be increased to a maximum of σ = 2.8∙10–5 S∙cm–1 for multilayer structures of two different alternating garnet-type materials (Li6.5La3Zr1.5Ta0.5O12:Al2O3, Li7La3Zr2O12:Ga2O3). These investigations revealed a strong influence of the thin film microstructure on the total conductivity. Additionally the electronic partial conductivity of Li6BaLa2Ta2O12 as bulk and thin film material was determined. -
Electrochemistry –An Oxidizing Agent Is a Species That Oxidizes Another Species; It Is Itself Reduced
Oxidation-Reduction Reactions Chapter 17 • Describing Oxidation-Reduction Reactions Electrochemistry –An oxidizing agent is a species that oxidizes another species; it is itself reduced. –A reducing agent is a species that reduces another species; it is itself oxidized. Loss of 2 e-1 oxidation reducing agent +2 +2 Fe( s) + Cu (aq) → Fe (aq) + Cu( s) oxidizing agent Gain of 2 e-1 reduction Skeleton Oxidation-Reduction Equations Electrochemistry ! Identify what species is being oxidized (this will be the “reducing agent”) ! Identify what species is being •The study of the interchange of reduced (this will be the “oxidizing agent”) chemical and electrical energy. ! What species result from the oxidation and reduction? ! Does the reaction occur in acidic or basic solution? 2+ - 3+ 2+ Fe (aq) + MnO4 (aq) 6 Fe (aq) + Mn (aq) Steps in Balancing Oxidation-Reduction Review of Terms Equations in Acidic solutions 1. Assign oxidation numbers to • oxidation-reduction (redox) each atom so that you know reaction: involves a transfer of what is oxidized and what is electrons from the reducing agent to reduced 2. Split the skeleton equation into the oxidizing agent. two half-reactions-one for the oxidation reaction (element • oxidation: loss of electrons increases in oxidation number) and one for the reduction (element decreases in oxidation • reduction: gain of electrons number) 2+ 3+ - 2+ Fe (aq) º Fe (aq) MnO4 (aq) º Mn (aq) 1 3. Complete and balance each half reaction Galvanic Cell a. Balance all atoms except O and H 2+ 3+ - 2+ (Voltaic Cell) Fe (aq) º Fe (aq) MnO4 (aq) º Mn (aq) b. -
Teaching Undergraduate Chemistry Students Electrochemistry Fundamentals with Galvanic and Concentration Cells
Teaching Undergraduate Chemistry Students Electrochemistry Fundamentals with Galvanic and Concentration Cells Victoria Kong*, Isabelle Gray, and Dr. John Rowley Department of Chemistry and Physics, Carroll College, Helena, Montana *[email protected] W.E.L. Wiegand Foundaon Abstract Introduction/ Background In this lab, two things were achieved: a galvanic cell was made from different mixed metal components, allowing students to determine the identity of an unknown metal, and the value of the Nernst constant was Ecell=E°- (RT/nF)lnQ calculated through experimental data from a concentration cell. A galvanic cell with 1.5M Copper Nitrate solution at the cathode and a 1.5M Zinc Equation 1. The Nernst Equation. RT/F = 0.0592. Nitrate solution at the anode was made. A copper wire was used for both electrodes. A measured electrochemical cell potential for this system was ∆G°=nFE° (a) found to be -0.61V, giving a -19.7% error when compared against the ∆G= ∆G°+RTlnQ (b) theoretical Ecell value of -0.76V. The theoretical Ecell value was calculated Equation 2. Gibbs Free Energy Equation for (a) using the equation Ecell= Eanode- Ecathode. Using this technique, a galvanic standard and (b) non- standard conditions cell using 1.5M Copper Nitrate aqueous solution and 1.5M Lead Nitrate aqueous was also made, resulting in a -7.69% error when compared against Ecell°=E°cathode-E°anode the theoretical. A concentration cell with a Copper Nitrate solution at the Equation 3. E°cell equation. Values typically Figure 1. Representation of a anode and cathode yielded a calculated Nernst constant value of 0.0211, measured experimentally, or referenced from the Figure 2. -
Stability of Positive Electrolyte Containing Trishydroxymethyl Aminomethane Additive for Vanadium Redox Flow Battery
Int. J. Electrochem. Sci., 7 (2012) 4388 - 4396 International Journal of ELECTROCHEMICAL SCIENCE www.electrochemsci.org Stability of Positive Electrolyte Containing Trishydroxymethyl Aminomethane Additive for Vanadium Redox Flow Battery Sui Peng1, Nangfang Wang1,2, Chao Gao1, Ying Lei1, Xingxing Liang1, Suqin Liu1,* , Younian Liu1 1 Key Laboratory of Resources Chemistry of Nonferrous Metals, Ministry of Education, College of Chemistry and Chemical Engineering, Central South University, Changsha 410083, China 2 School of Chemistry and Chemical Engineering, Hunan Institute of Engineering, xiangtan 411104, China *E-mail: [email protected] Received: 10 March 2012 / Accepted: 24 March 2012 / Published: 1 May 2012 Trishydroxymethyl aminomethane (Tris) was used as an additive of the positive electrolyte for all vanadium redox battery (VRB) and cycling and electrochemical stabilities of the positive electrolyte were investigated. The 50 cyclic voltammetry (CV) cycles suggested that the positive electrolyte with the Tri additive after charge-discharge cycles has good cycle stability compared to that before the charge-discharge cycles. The VRB employing the vanadium electrolyte with the Tris additive as positive electrolyte exhibited better charge-discharge behavior and less discharge capacity fade rate with cycles compared with the blank electrolyte system. The UV/visible spectroscopy showed that the vanadium concentration in the positive electrolyte containing Tri additive during 40 charge-discharge cycles remains unchanged. The X-ray photoelectron spectroscopy (XPS) verified that the positive electrolyte with the Tri additive has no etching and oxidation effect on the carbon felt electrode. Keywords: Vanadium redox flow battery; additive; stability; electrochemical stability 1. INTRODUCTION All vanadium redox flow battery (VRB) is a promising energy conversion device that employs V(V)/ V(II)/V(III) and V(IV)/V(V) couples in the negative and positive half-cells respectively to store chemical potential energy [1-3].