A Review of Cathode and Anode Materials for Lithium-Ion Batteries
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Electrolyte Panel
Lab Dept: Chemistry Test Name: ELECTROLYTE PANEL General Information Lab Order Codes: LYTE Synonyms: Electrolytes; Lytes CPT Codes: 80051 – Electrolyte panel Test Includes: Carbon Dioxide, Chloride, Potassium, Sodium concentrations reported in mEq/L, and AGAP (Anion Gap). Logistics Test Indications: The maintenance of osmotic pressure and water distribution in the various body fluid compartments is primarily a function of the four major electrolytes, Na+, K+, Cl-, and HCO3-. In addition to water homeostasis, these electrolytes play an important part in the maintenance of pH, regulation of proper heart and muscle functions, involvement in electron transfer reactions, and participation in catalysis as cofactors for enzymes. Lab Testing Sections: Chemistry Phone Numbers: MIN Lab: 612-813-6280 STP Lab: 651-220-6550 Test Availability: Daily, 24 hours Turnaround Time: 30 minutes Special Instructions: N/A Specimen Specimen Type: Blood Container: Green top (Li Heparin) tube, preferred Alternate tube: Red, marble or gold top tube Draw Volume: 0.6 mL blood Processed Volume: 0.2 mL serum/plasma Collection: Routine blood collection. Mix tubes containing anticoagulant by gentle inversion. Note: Venipuncture samples are preferred, but capillary specimens will be accepted. Special Processing: Lab Staff: Sample must be run within one hour of collection for CO2 stability. Centrifuge specimen, remove serum/plasma aliquot into a plastic sample cup. Avoid prolonged contact with separated cells. Store at refrigerated temperatures. Patient Preparation: None Sample Rejection: Mislabeled or unlabeled specimens Interpretive Reference Range: See individual analyte procedures Critical Values: See individual analyte procedures Limitations: See individual analyte procedures Methodology: See individual analyte procedures References: See individual analyte procedures Updates: 2/8/2016: Update alt tube types . -
Next Generation Anodes for Lithium-Ion Batteries
NEXT GENE ATION ANODES Next Ge eratio A odes for Lithium-Io Batteries Seco d Quarter Progress Report 2018 De is Dees, Poi t-of-Co tact Argonne National Laboratory 9700 South Cass Avenue Argonne, IL 60439 Phone: (630) 252-7349 E-mail: [email protected] Bria Cu i gham, DOE-EERE-VTO Tech ology Ma ager U.S. Department of Energy, Battery R&D Phone: (202) 287-5686 E-mail: [email protected] Table of Co te ts Overview (page 2) 1. Research Facilities Support (page 5) CAMP Facility Support Activities (ANL) (page 5) Characterization and Optimization of Si Slurry by Zeta Potential (ORNL) (page 7) Thermodynamic Understanding and Abuse Performance (SNL) (page 9) Hydro/Solvothermal Synthesis and Scale-up of Silicon and Silicon-containing Nanoparticles (ANL) (page 10) 2. Characterization, Diagnostics, and Analysis (page 12) Spectroscopic Characterization of Cycled Si Electrodes: Understanding the Role of Binder (ORNL) (page 12) EQCM Studies of Silicon Anodes (ANL) (page 13) Effect of silicate thickness on the electrochemical performance of silicate-coated silicon nanoparticles (ANL) (page 15) Calendar-life versus Cycle-life aging of Lithium-ion Cells with Silicon-Graphite Composite Electrodes – Electrolyte Analysis (ANL) (page 17) 3. Materials Advancements (page 18) Continued Study of Lithiation Effect of the Poly(Acrylic Acid) Binders on the Silicon Anode of Lithium-Ion Batteries (ANL) (page 19) Probe the relationships between functional electrolytes structure and SEI property for Si materials (LBNL) (page 21) Silicon Surface Modification Using -
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. -
All-Carbon Electrodes for Flexible Solar Cells
applied sciences Article All-Carbon Electrodes for Flexible Solar Cells Zexia Zhang 1,2,3 ID , Ruitao Lv 1,2,*, Yi Jia 4, Xin Gan 1,5 ID , Hongwei Zhu 1,2 and Feiyu Kang 1,5,* 1 State Key Laboratory of New Ceramics and Fine Processing, School of Materials Science and Engineering, Tsinghua University, Beijing 100084, China; [email protected] (Z.Z.); [email protected] (X.G.); [email protected] (H.Z.) 2 Key Laboratory of Advanced Materials (MOE), School of Materials Science and Engineering, Tsinghua University, Beijing 100084, China 3 School of Physics and Electronic Engineering, Xinjiang Normal University, Urumqi 830046, Xinjiang Province, China 4 Qian Xuesen Laboratory of Space Technology, China Academy of Space Technology, Beijing 100094, China; [email protected] 5 Graduate School at Shenzhen, Tsinghua University, Shenzhen 518055, Guangdong Province, China * Correspondences: [email protected] (R.L.); [email protected] (F.K.) Received: 16 December 2017; Accepted: 20 January 2018; Published: 23 January 2018 Abstract: Transparent electrodes based on carbon nanomaterials have recently emerged as new alternatives to indium tin oxide (ITO) or noble metal in organic photovoltaics (OPVs) due to their attractive advantages, such as long-term stability, environmental friendliness, high conductivity, and low cost. However, it is still a challenge to apply all-carbon electrodes in OPVs. Here, we report our efforts to develop all-carbon electrodes in organic solar cells fabricated with different carbon-based materials, including carbon nanotubes (CNTs) and graphene films synthesized by chemical vapor deposition (CVD). Flexible and semitransparent solar cells with all-carbon electrodes are successfully fabricated. -
Coal As Value-Added for Lithium Battery Anodes
Coal as Value-Added for Lithium Battery Anodes Project Review Award No. DE-FE0031879 November 6th 2020 1 Project Summary • Semplastics has begun development of a novel material based on our X-MAT® polymer-derived ceramic (PDC) technology for use as an anode material in lithium-ion batteries • The X-MAT anode material is a composite of chemically tailored silicon oxycarbide (SiOC) and domestically sourced coal powder, designed to be a drop- in replacement for graphite within lithium-ion batteries • Preliminary tests of this material have shown more than twice the reversible capacity of graphite anodes • Through this project, Semplastics proposes to complete development and begin commercialization of this material 2 Project Description and Objectives 3 What are X-MAT Coal-Core Composite Powders? • Raw coal powder mixed with our proprietary polymer derived ceramic (PDC)-forming resin to produce coal-core composite powder materials – Electrically conductive – Low cost – Coal is 1-5¢/lb – The raw coal will not be burned during materials processing, and the resulting powder composite will not burn – Easily manufactured compared to typical ceramics – no sintering needed – Capable of using a variety of coals including lignite, bituminous, and anthracite particles in an “as-is” state with our proprietary PDC technology 4 How is this different from other approaches? • Our PDCs can be tuned at the Atomic Level to contain varying amounts of silicon, oxygen and carbon • Uses a “green” low-energy method – does not involve high-energy processes including -
A Highly-Active, Stable and Low-Cost Platinum-Free Anode Catalyst Based on Runi for Hydroxide Exchange Membrane Fuel Cells
ARTICLE https://doi.org/10.1038/s41467-020-19413-5 OPEN A highly-active, stable and low-cost platinum-free anode catalyst based on RuNi for hydroxide exchange membrane fuel cells Yanrong Xue1,2,5, Lin Shi3,5, Xuerui Liu1,2, Jinjie Fang1,2, Xingdong Wang2, Brian P. Setzler3, Wei Zhu 2, ✉ ✉ Yushan Yan 1,3 & Zhongbin Zhuang 1,2,4 1234567890():,; The development of cost-effective hydroxide exchange membrane fuel cells is limited by the lack of high-performance and low-cost anode hydrogen oxidation reaction catalysts. Here we report a Pt-free catalyst Ru7Ni3/C, which exhibits excellent hydrogen oxidation reaction activity in both rotating disk electrode and membrane electrode assembly measurements. The hydrogen oxidation reaction mass activity and specific activity of Ru7Ni3/C, as measured in rotating disk experiments, is about 21 and 25 times that of Pt/C, and 3 and 5 times that of PtRu/C, respectively. The hydroxide exchange membrane fuel cell with Ru7Ni3/C anode can −2 −2 deliver a high peak power density of 2.03 W cm in H2/O2 and 1.23 W cm in H2/air (CO2-free) at 95 °C, surpassing that using PtRu/C anode catalyst, and good durability with less than 5% voltage loss over 100 h of operation. The weakened hydrogen binding of Ru by alloying with Ni and enhanced water adsorption by the presence of surface Ni oxides lead to the high hydrogen oxidation reaction activity of Ru7Ni3/C. By using the Ru7Ni3/C catalyst, the anode cost can be reduced by 85% of the current state-of-the-art PtRu/C, making it highly promising in economical hydroxide exchange membrane fuel cells. -
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 . -
Demonstrating Solar Conversion Using Natural Dye Sensitizers
Demonstrating Solar Conversion Using Natural Dye Sensitizers Subject Area(s) Science & Technology, Physical Science, Environmental Science, Physics, Biology, and Chemistry Associated Unit Renewable Energy Lesson Title Dye Sensitized Solar Cell (DSSC) Grade Level (11th-12th) Time Required 3 hours / 3 day lab Summary Students will analyze the use of solar energy, explore future trends in solar, and demonstrate electron transfer by constructing a dye-sensitized solar cell using vegetable and fruit products. Students will analyze how energy is measured and test power output from their solar cells. Engineering Connection and Tennessee Careers An important aspect of building solar technology is the study of the type of materials that conduct electricity and understanding the reason why they conduct electricity. Within the TN-SCORE program Chemical Engineers, Biologist, Physicist, and Chemists are working together to provide innovative ways for sustainable improvements in solar energy technologies. The lab for this lesson is designed so that students apply their scientific discoveries in solar design. Students will explore how designing efficient and cost effective solar panels and fuel cells will respond to the social, political, and economic needs of society today. Teachers can use the Metropolitan Policy Program Guide “Sizing The Clean Economy: State of Tennessee” for information on Clean Economy Job Growth, TN Clean Economy Profile, and Clean Economy Employers. www.brookings.edu/metro/clean_economy.aspx Keywords Photosynthesis, power, electricity, renewable energy, solar cells, photovoltaic (PV), chlorophyll, dye sensitized solar cells (DSSC) Page 1 of 10 Next Generation Science Standards HS.ESS-Climate Change and Human Sustainability HS.PS-Chemical Reactions, Energy, Forces and Energy, and Nuclear Processes HS.ETS-Engineering Design HS.ETS-ETSS- Links Among Engineering, Technology, Science, and Society Pre-Requisite Knowledge Vocabulary: Catalyst- A substance that increases the rate of reaction without being consumed in the reaction. -
Solid Electrolyte Batteries
SOLID ELECTROLYTE BATTERIES John B. Goodenough and Yuhao Lu Texas Materials Institute The University of Texas at Austin Project ID: ES060 DOE Vehicle Technologies Annual Merit Review Meeting May 9-13, 2011 This presentation does not contain any proprietary or confidential information. 1 The University of Texas at Austin Overview Timeline Barriers • Project Start Date-Oct. 2009 • Lithium-ion solid electrolyte. • Project End Date- Sept. 2010 • Choice of redox couples. • Percent complete: 100% complete • Flow-through- cathode cell design Budget Partners • Funding received in FY09-FY10 – $315K • Karim Zaghib of Hydro Quebec • Funding received in FY10-FY11 – $315K 2 The University of Texas at Austin Milestones Develop and test a suitable test cell. (Jan. 10) Completed Optimize components of the cell. (Apr. 10) Completed Develop a lithium/Fe(NO3)3 cell. (July. 10) Completed Design of a new cell (Sept. 10) Completed Test flow-through cell (Jan. 11) Completed 3 The University of Texas at Austin Typical Lithium Ion Battery (LIB) Cell e- e- - Separator + Li+ Anode Li+ Cathode (Reducing Agent) (Oxidizing Agent) Li+ SEI layer Electrolyte Capacity limited by Li solid solution in cathode and loss in SEI layer Voltage limited by Eg of carbonate electrolyte. 4 The University of Texas at Austin Why Oxides? E E Co: 4s0 Co: 4s0 Co(II): t4e2 µLi 4.0 eV Co(IV): t5e0 EFC EFC (pinned) Co(III): t6e0 Co(III): t6e0 O: 2p6 O: 2p6 N(E) N(E) Li CoO (0<x<0.55) LiCoO2 1-x 2 2- + Holes form peroxide (O2) for x> 0.55 or H inserted from electrolyte. -
Nickel-Metal Hydride Batteries: a New Generation of Secondary Storage
8 Nickel-Metal Hydride Batteries: A New Generation of Secondary Storage Brian Niece Literature Seminar September 23, 1993 Interest in secondary batteries suitable for use in electric vehicles has increased rapidly in the last decade, as restrictions on vehicle emissions in urban areas have become more stringent. Combustion of fossil fuels in large power plants and storage of the energy electrochemically is more efficient than direct combustion in internal combustion engines [1]. In addition, storage batteries can be charged from alternative sources of electricity, such as solar and hydroelectric plants. In order to be acceptable for use in an electric vehicle, a battery must meet a number of important criteria. It must have a high energy density to make the travel distance between recharges as long as possible. It must be capable of high power output throughout its dis charge cycle to provide the high current necessary to operate a vehicle, and it must be capa ble of especially high peak power for acceleration. The battery must also have a long cycle life as well as a long physical lifetime. It must not undergo rapid self discharge on standing. Finally, it must not be prohibitively expensive. Theoretical energy densities of secondary battery systems in common use are listed in Table 1. Most of these systems are not practical for electric vehicle use for a variety of rea sons. The lead-sulfuric acid battery cannot be sealed, and cannot be produced with a suffi ciently high energy density. The sodium-sulfur cell is undesirable because it contains metal lic sodium and operates at 300°C. -
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. -
Operation, Manufacturing, and Supply Chain of Lithium-Ion Batteries for Electric Vehicles
ORNL/TM-2020/1729 Operation, Manufacturing, and Supply Chain of Lithium-ion Batteries for Electric Vehicles Ilias Belharouak Jagjit Nanda Ethan Self W. Blake Hawley David Wood Zhijia Du Jianlin Li Approved for public release. Ronald L. Graves Distribution is unlimited. August 2020 DOCUMENT AVAILABILITY Reports produced after January 1, 1996, are generally available free via US Department of Energy (DOE) SciTech Connect. Website www.osti.gov Reports produced before January 1, 1996, may be purchased by members of the public from the following source: National Technical Information Service 5285 Port Royal Road Springfield, VA 22161 Telephone 703-605-6000 (1-800-553-6847) TDD 703-487-4639 Fax 703-605-6900 E-mail [email protected] Website http://classic.ntis.gov/ Reports are available to DOE employees, DOE contractors, Energy Technology Data Exchange representatives, and International Nuclear Information System representatives from the following source: Office of Scientific and Technical Information PO Box 62 Oak Ridge, TN 37831 Telephone 865-576-8401 Fax 865-576-5728 E-mail [email protected] Website http://www.osti.gov/contact.html This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or any agency thereof.