Electronic Environments and Electrochemical Properties of Lithium Storage Materials
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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_. -
Quality Decision for Overcharged Li Ion Battery from Reliability and Safety Perspective
Quality Decision for Overcharged Li Ion Battery from reliability and safety perspective Feng Leng 1,2, Cher Ming Tan 1,2,*, Rachid Yazami 2,3, Kenza Maher 3, Robert Wang1 1 Nanyang Technological University, School of Electrical Electronics Engineering, Blk S2.1, 50 Nanyang Avenue, Singapore 639798, (Singapore) Email: [email protected] Email: [email protected] Email: [email protected] 2 TUM CREATE PTE LTD, 1 Create Way, #10-02 Create Tower, Singapore 138602, (Singapore) 3 Nanyang Technological University, School of Materials Science and Engineering and Research Institute at Nanyang (ERIAN), Research Techno Plaza, X-Frontier Blk, 50 Nanyang Drive, Singapore 637553, (Singapore) Email: YAZAMI [email protected] Email: Maher [email protected] Abstract During charging of Lithium-ion battery (LiB), the charging cut-off voltage (COV) may exceed the manufacturers’ specification because of incorrect monitoring of the charging control circuit, either due to the ageing of the control circuit or the design/manufacturing errors of the control circuit. In fact, it is found that overcharging LiB cell is a common abuse. This work shows the effect of excessive COV on cell’s discharging ability, and the use of a novel non-destructive method to evaluate if the damage made in the cell by the excessive COV is rendering the cell from further safe usage or it is still acceptable with minor degradation in reliability and safety, thus providing a basis for quality consideration of the cell. The method also enables battery manufacturers to identify the internal components for their cells that are most vulnerable to the excessive COV so that quality improvement of their batteries can be designed and produced. -
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. -
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. -
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. -
Electrochemistry Is the Branch of Chemistry Concerned with the Interrelation of Electrical and Chemical Changes That Are Caused by the Passage of Current.”
11/9/2020 Madan Mohan Malaviya University of Technology, Gorakhpur-273010 “Electrochemistry is the branch of chemistry concerned with the interrelation of electrical and chemical changes that are caused by the passage of current.” “Chemical reactions that involve the input or generation of electric currents are called electrochemical reactions.” “A device capable of either generating electrical energy from chemical reactions or using electrical energy to cause chemical reactions is called Electrochemical cell.” CESD, MMMUT, Gorakhpur-273010 1 11/9/2020 Madan Mohan Malaviya University of Technology, Gorakhpur-273010 “A Galvanic cell is an electrochemical cell that produces electricity as result of spontaneous reaction occurring in it.” “A Galvanic cell is a device in which the free energy of a physical or chemical process is converted in to electrical energy.” It is also called as Voltaic (voltage generated) cell. Daniell Cell: A Daniell cell is the best example of a galvanic cell which converts chemical energy into electrical energy. The Daniell cell consists of two electrodes of dissimilar metals, Zn and Cu; each electrode is in contact with a solution of its own ion; Zinc sulphate and copper sulphate respectively. Zn(s) + Cu2+(aq) Zn2+(aq) + Cu (s) 2 11/9/2020 Madan Mohan Malaviya University of Technology, Gorakhpur-273010 Electrode: An electrode is a small piece of metal or other substance that is used to take an electric current to or from a source of power. Electrolyte: Electrolyte is a substance that conducts electric current as a result of dissociation into cations and anions, in a polar solvent. The most familiar electrolytes are acids, bases, and salts, which ionize when dissolved in solvents such as water or alcohol. -
UCLA Electronic Theses and Dissertations
UCLA UCLA Electronic Theses and Dissertations Title SnO2/Graphene Nanocomposites as High-Capacity Anode Materials for Lithium-Ion Batteries: Synthesis and Electrochemical Performance Permalink https://escholarship.org/uc/item/41g3q26f Author Zhu, Xiuming Publication Date 2018 Peer reviewed|Thesis/dissertation eScholarship.org Powered by the California Digital Library University of California UNIVERSITY OF CALIFORNIA Los Angeles SnO2/Graphene Nanocomposites as High-Capacity AnoDe Materials For Lithium-Ion Batteries: Synthesis anD Electrochemical Performance A thesis submitteD in partial satisfaction oF the requirements For the Degree Master oF Science in Materials Science anD Engineering by Xiuming Zhu 2018 © Copyright by Xiuming Zhu 2018 ABSTRACT OF THE DISSERTATION SnO2/Graphene Nanocomposites as High-Capacity AnoDe Materials For Lithium-Ion Batteries: Synthesis anD Electrochemical Performance by Xiuming Zhu Master oF Science in Materials Science anD Engineering University oF CaliFornia, Los Angeles, 2018 ProFessor Bruce S. Dunn, Chair Lithium ion batteries as a poWer source are the most commonly useD in the electronic Devices anD electric vehicles (EV) For griD-energy storage. AnoDe materials With high speciFic capacity For lithium ion batteries have been DevelopeD in recent years. SnO2 has also been consiDereD as a promising canDiDate to serve as the anoDe material For lithium ion batteries Due to its high theoretical capacity. But the volume expansion eFFect results in the DegraDation oF active material anD limits the complete realization oF theoretical capacity. Graphene has recently become one oF the most promising matrices For high-capacity anode materials, due to gooD electrical conDuctivity, outstanDing mechanical Flexibility and high theoretical capacity. In this paper, the nanocomposites of SnO2 and graphene as anoDe materials For lithium ion batteries Were Facilely synthesizeD through hydrothermal methoD. -
The Influence of Internal Parameters on the Electrochemical and Thermal Behaviors of Lithium-Ion Batteries
The Influence of Internal Parameters on the Electrochemical and Thermal Behaviors of Lithium-Ion Batteries by Rui Zhao A thesis submitted to the Faculty of Graduate and Postdoctoral Affairs in partial fulfillment of the requirements for the degree of Master of Applied Science in Materials Engineering Carleton University Ottawa, Ontario © 2014 Rui Zhao Abstract Lithium ion (Li-ion) batteries, consisting of multiple electrochemical cells, are complex system whose high electrochemical and thermal stability is often critical to the well-being and functional capabilities of the electric device. Considering any change in the specifications may significantly affect the overall performance and life of a battery, an investigation of the impacts of the electrode thickness and initial electrolyte salt concentration on the electrochemical and thermal properties of lithium-ion cells based on experiments and a coupling model composed of a 1D electrochemical model and a 3D thermal model is conducted in this work. Pertinent results have demonstrated that the electrode thickness as well as the electrolyte salt concentration can significantly influence the battery from many key aspects such as the energy density, voltage, temperature, distribution and proportion of different heat sources and ability to prevent lithium plating. ii Acknowledgements First and foremost, I would like to express my great gratitude to my supervisors, Dr. LIU Jie and GU Junjie, for their enthusiastic supervision and patient guidance. They guided me throughout my entire master program. Without their perspectiveness, knowledge, constant support and encouragement, it is impossible for me to have the current thesis. In addition, I wish to acknowledge of Dr. ZHANG Zhonghua in the technical suggestion. -
Corrosion Basics
CORROSION BASICS (from Swain (1996) and Schultz (1997)) What is corrosion? • Webster’s Dictionary - corrode (v.) To eat away or be eaten away gradually, especially by chemical action. • NACE Corrosion Basics - corrosion may be defined as the deterioration of a material (usually a metal) because of a reaction with the environment. Why do metals corrode? Most metals are found in nature as ores. The manufacturing process of converting these ores into metals involves the input of energy. During the corrosion reaction the energy added in manufacturing is released, and the metal is returned to its oxide state. Metal Ore reduction (add electrons)→ Metal oxidation (strip electrons)→ Corrosion Products In the marine environment, the corrosion process generally takes place in aqueous solutions and is therefore electrochemical in nature. Corrosion consequences Economic - corrosion results in the loss of $8 - $126 billion annually in the U.S. alone. This impact is primarily the result of: 1. Downtime 2. Product Loss 3. Efficiency Loss 4. Contamination 5. Overdesign Safety / Loss of Life Corrosion can lead to catastrophic system failures which endanger human life and health. Examples include a 1967 bridge collapse in West Virginia which killed 46. The collapse was attributed to stress corrosion cracking (SCC). In another example, the fuselage of an airliner in Hawaii ripped open due to the combined action of stress and atmospheric corrosion. Corrosion cell Corrosion occurs due to the formation of electrochemical cells. In order for the corrosion reaction to occur five things are necessary. If any of these factors are eliminated, galvanic corrosion will not occur. THIS IS THE KEY TO CORROSION CONTROL! The necessary factors for corrosion to proceed are: 1. -
A Continuous Electrochemical Process to Convert Lignin to Low Molecular Weight
A Continuous Electrochemical Process to Convert Lignin to Low Molecular Weight Aromatic Compounds and Cogeneration of Hydrogen A dissertation presented to the faculty of the Russ College of Engineering and Technology of Ohio University In partial fulfillment of the requirements for the degree Doctor of philosophy Mahtab Naderinasrabadi May 2020 © 2020 Mahtab Naderinasrabadi. All Rights Reserved. 2 This dissertation titled A Continuous Electrochemical Process to Convert Lignin to Low Molecular Weight Aromatic Compounds and Cogeneration of Hydrogen by MAHTAB NADERINASRABADI has been approved for the Department of Chemical and Biomolecular Engineering and the Russ College of Engineering and Technology by John Staser Associate Professor of Chemical and Biomolecular Engineering Mei Wei Dean, Russ College of Engineering and Technology 3 ABSTRACT NADERINASRABADI, MAHTAB, Ph.D., May 2020, Chemical Engineering A Continuous Electrochemical Process to Convert Lignin to Low Molecular Weight Aromatic Compounds and Cogeneration of Hydrogen Director of Dissertation: John Staser Lignin is one of the main byproducts of pulp and paper industry and biorefineries. Depolymerization of lignin can lead to producing valuable low molecular weight compounds with different functional groups, which are mainly achieved from crude oil sources. Lignin electrolysis could address issues of other lignin depolymerization methods such as complexity, lignin combustion, and low selectivity. On the other hand, lignin electrolysis can occur at significantly lower overpotentials than those required for water electrolysis, which leads to lower-voltage electrolyzer operation and as a result lower energy consumption for hydrogen production. This study includes research and experimental works on developing a continuous electrochemical process for both lignin electrolysis and hydrogen production in an electrolyzer. -
Electrochemistry a Chem1 Supplement Text Stephen K
Electrochemistry a Chem1 Supplement Text Stephen K. Lower Simon Fraser University Contents 1 Chemistry and electricity 2 Electroneutrality .............................. 3 Potential dierences at interfaces ..................... 4 2 Electrochemical cells 5 Transport of charge within the cell .................... 7 Cell description conventions ........................ 8 Electrodes and electrode reactions .................... 8 3 Standard half-cell potentials 10 Reference electrodes ............................ 12 Prediction of cell potentials ........................ 13 Cell potentials and the electromotive series ............... 14 Cell potentials and free energy ...................... 15 The fall of the electron ........................... 17 Latimer diagrams .............................. 20 4 The Nernst equation 21 Concentration cells ............................. 23 Analytical applications of the Nernst equation .............. 23 Determination of solubility products ................ 23 Potentiometric titrations ....................... 24 Measurement of pH .......................... 24 Membrane potentials ............................ 26 5 Batteries and fuel cells 29 The fuel cell ................................. 29 1 CHEMISTRY AND ELECTRICITY 2 6 Electrochemical Corrosion 31 Control of corrosion ............................ 34 7 Electrolytic cells 34 Electrolysis involving water ........................ 35 Faraday’s laws of electrolysis ....................... 36 Industrial electrolytic processes ...................... 37 The chloralkali -
Annual Report
2014 Annual Report NATIONAL ACADEMY OF ENGINEERING ENGINEERING THE FUTURE 1 Letter from the President 3 In Service to the Nation 3 Mission Statement 4 NAE 50th Anniversary Initiatives 5 Program Reports 5 Engineering Education Frontiers of Engineering Education (FOEE) 2- and 4-Year Engineering and Engineering Technology Transfer Student Pilot Barriers and Opportunities in Completing Two- and Four-Year STEM Degrees Engagement of Professional Engineering Societies in Undergraduate Engineering Education Understanding the Engineering Education–Workforce Continuum Engineering Technology Education 8 Technological Literacy LinkEngineering Website 8 Public Understanding of Engineering Media Relations Public Relations Grand Challenges for Engineering 10 Center for Engineering, Ethics, and Society (CEES) Online Ethics Center Expansion Ethics and Sustainability in Engineering Educational Partnership on Climate Change, Engineered Systems, and Society 11 Diversity of the Engineering Workforce EngineerGirl Website 11 Frontiers of Engineering Armstrong Endowment for Young Engineers—Gilbreth Lectures 14 Manufacturing, Design, and Innovation NAE Conference on Value Creation and Opportunity in the United States Making Value for America: Embracing the Future of Manufacturing, Technology, and Work 15 Technology, Science, and Peacebuilding 16 2014 NAE Awards Recipients 18 2014 New Members and Foreign Members 20 NAE Anniversary Members 25 2014 Private Contributions 28 Catalyst Society 28 Rosette Society 29 Challenge Society 29 Charter Society 31 Other Individual