Lithium Ion Battery
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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 . -
A Review of Cathode and Anode Materials for Lithium-Ion Batteries
A Review of Cathode and Anode Materials for Lithium-Ion Batteries Yemeserach Mekonnen Aditya Sundararajan Arif I. Sarwat IEEE Student Member IEEE Student Member IEEE Member Department of Electrical & Department of Electrical & Department of Electrical & Computer Engineering Computer Engineering Computer Engineering Florida International University Florida International University Florida International University Email: [email protected] Email: [email protected] Email: [email protected] Abstract—Lithium ion batteries are one of the most technologies such as plug-in HEVs. For greater application use, commercially sought after energy storages today. Their batteries are usually expensive and heavy. Li-ion and Li- based application widely spans from Electric Vehicle (EV) to portable batteries show promising advantages in creating smaller, devices. Their lightness and high energy density makes them lighter and cheaper battery storage for such high-end commercially viable. More research is being conducted to better applications [18]. As a result, these batteries are widely used in select the materials for the anode and cathode parts of Lithium (Li) ion cell. This paper presents a comprehensive review of the common consumer electronics and account for higher sale existing and potential developments in the materials used for the worldwide [2]. Lithium, as the most electropositive element making of the best cathodes, anodes and electrolytes for the Li- and the lightest metal, is a unique element for the design of ion batteries such that maximum efficiency can be tapped. higher density energy storage systems. The discovery of Observed challenges in selecting the right set of materials is also different inorganic compounds that react with alkali metals in a described in detail. -
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. -
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. -
Questions and Answers Related to Lithium-Ion Rechargeable Battery Care
FAQ Questions and answers related to lithium-ion rechargeable battery care 1. How should I store my batteries? Lithium-ion batteries (Li-ion) should not be stored over a longer period of time either uncharged or fully charged. The optimum storage as determined by extensive experiments is with 40% to 50% capacity and at low temperatures, which should not drop below 0°C. Storage at 5°C to 10°C is optimal. As a result of self-discharge, a recharge is necessary every 12 months, at the latest. 2. Should the battery be taken from the device in case of a long period of non-use? Yes. A small current can also flow in the switched-off device, which leads to a complete discharge which, after a longer period of time, can damage the battery and at the very worst destroy it. 3. What is understood by self-discharge? In the case of lithium-ion batteries, 3% to 5% loss of charge monthly is possible the self- discharge is temperature-dependent and higher with increased temperatures. 4. What is understood by complete discharge? By complete discharge is understood the "squeezing-out" of a battery until it does not yield this any more current at all. The voltage drops to 0 volt in this case. If this status is retained, chemically reactions progress at the electrodes in the battery, which make it partially to completely unusable. The result is that the battery loses capacity massively and possibly cannot be charged up any longer. For this reason batteries should not be discharged to below a type-dependent final cut-off voltage and should be charged up again as quickly as possible. -
The Rechargeable Battery Market and Main Trends 2018-2030
The Rechargeable Battery Market and Main Trends 2018-2030 Christophe PILLOT th September 18 , 2019 Director, AVICENNE ENERGY Lyon, France Presentation Outline • The rechargeable battery market in 2018 • The Li-ion battery value chain • Li-ion battery material market Christophe PILLOT • Focus on xEV batteries + 33 1 44 55 19 90 [email protected] • Forecasts & conclusions AGENDA The market in 2018 by technology, applications & battery suppliers The Rechargeable Battery Market and Main Trends 2018 – 2030 Li-ion components market & value chain xEV market in 2018 xEV forecasts up to 2030 Lyon, France Rechargeable battery market forecasts up to 2030 September 18th, 2019 Christophe PILLOT + 33 1 44 55 19 90 [email protected] 2 OEM INVESTMENT IN VEHICLE ELECTRIFICATION Carmakers to invest more than $90 Billion in EV Ford will invest $11 billion by 2022 to launch 40 new electric cars and hybrids worldwide The Rechargeable Battery Volkswagen plan to spend $40 Billion by 2030 to build electrified versions of its 300-plus Market and Main Trends 2018 – 2030 global models Daimler will spend at least $11,7 billion to introduce 10 pure electric 40 hybrid models Nissan pledged to launch 8 new electric vehicles and hit annual sales of 1 million electrified vehicles by 2022 Toyota will launch 10 Evs by the early 2020s and sell 5,5 million electrified vehicles, including Lyon, France hybrids and hydrogen fuel cell vehicles, by 2030 September 18th, 2019 BMW will offer 25 electrified (12 fully electric) vehicles by 2025 GM pledging to sell 20 all-electric -
Battery Technologies for Small Scale Embeded Generation
Battery Technologies for Small Scale Embedded Generation. by Norman Jackson, South African Energy Storage Association (SAESA) Content Provider – Wikipedia et al Small Scale Embedded Generation - SSEG • SSEG is very much a local South African term for Distributed Generation under 10 Mega Watt. Internationally they refer to: Distributed generation, also distributed energy, on-site generation (OSG) or district/decentralized energy It is electrical generation and storage performed by a variety of small, grid- connected devices referred to as distributed energy resources (DER) Types of Energy storage: • Fossil fuel storage • Thermal • Electrochemical • Mechanical • Brick storage heater • Compressed air energy storage • Cryogenic energy storage (Battery Energy • Fireless locomotive • Liquid nitrogen engine Storage System, • Flywheel energy storage • Eutectic system BESS) • Gravitational potential energy • Ice storage air conditioning • Hydraulic accumulator • Molten salt storage • Flow battery • Pumped-storage • Phase-change material • Rechargeable hydroelectricity • Seasonal thermal energy battery • Electrical, electromagnetic storage • Capacitor • Solar pond • UltraBattery • Supercapacitor • Steam accumulator • Superconducting magnetic • Thermal energy energy storage (SMES, also storage (general) superconducting storage coil) • Chemical • Biological • Biofuels • Glycogen • Hydrated salts • Starch • Hydrogen storage • Hydrogen peroxide • Power to gas • Vanadium pentoxide History of the battery This was a stack of copper and zinc Italian plates, -
2020 Grid Energy Storage Technology Cost and Performance Assessment
Energy Storage Grand Challenge Cost and Performance Assessment 2020 December 2020 2020 Grid Energy Storage Technology Cost and Performance Assessment Kendall Mongird, Vilayanur Viswanathan, Jan Alam, Charlie Vartanian, Vincent Sprenkle*, Pacific Northwest National LaBoratory. Richard Baxter, Mustang Prairie Energy * [email protected] Technical Report Publication No. DOE/PA-0204 December 2020 Energy Storage Grand Challenge Cost and Performance Assessment 2020 December 2020 Disclaimer 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. ii Energy Storage Grand Challenge Cost and Performance Assessment 2020 December 2020 Acronyms AC alternating current Ah ampere-hour BESS battery energy storage system BLS U.S. Bureau of Labor Statistics BMS battery management system BOP balance of plant BOS balance of system C&C controls & communication C&I civil and infrastructure CAES compressed-air energy -
Development and Demonstration of Redox Flow Battery System
FEATURED TOPIC Development and Demonstration of Redox Flow Battery System Keiji YANO*, Shuji HAYASHI, Takahiro KUMAMOTO, Toshikazu SHIBATA, Katsuya YAMANISHI and Kazuhiro FUJIKAWA ---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------- High expectations have been placed on rechargeable batteries as a key technology to power system reliability associated with introduction of an increasing volume of renewable energy, as well as efficient power supply and successful business continuity planning. We have developed a redox flow battery system that is safe with a long service life. A demonstration proved its applicability to multiple requirements from electric power companies and other businesses. This paper describes the system, demonstration results, and our effort to reduce the price. ---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------- Keywords: redox flow battery, energy storage, renewable energy, demand response, BCP 1. Introduction 2. Operating Principle and Features of Redox Flow Battery In recent years, an increasing volume of renewable energy sources, such as solar and wind power, has been Figure 1 illustrates the configuration of an RF battery. -
All-Solid-State Lithium Batteries with Wide Operating Temperature Range
ENVIRONMENT, ENERGY & RESOURCES All-Solid-State Lithium Batteries with Wide Operating Temperature Range Mitsuyasu OGAWA*, Kentaro YOSHIDA and Keizo HARADA All-solid-state batteries do not use a flammable organic liquid electrolyte which has a risk of boiling, freezing or burning, and are therefore expected to operate in a wide temperature range. This paper reports on the development of a solid- state thin film lithium battery using a high conductive sulfide solid electrolyte and its charge-discharge characteristics at high and low temperatures. The high ionic conductivity of the sulfide solid electrolyte can reduce internal resistance, which greatly affects the charge-discharge characteristics of a battery. Test results show that, at room temperature, the capacity of this battery at a high discharge rate (24C) reaches 89% of the capacity at a low discharge rate (0.5 C). Cycle characteristics also confirmed that there was no degradation up to 100 cycles at both 170˚C and -40˚C. Keywords: solid-state battery, lithium battery, solid electrolyte, operating temperature range 1. Introduction the battery’s energy density. Because of these issues, all-solid-state lithium batteries Lithium ion secondary batteries have a high voltage have been proposed as a fundamental solution (Fig. 2)(2)-(4). and a high energy density, as shown in Fig. 1, and are All-solid-state batteries never use any liquid cell compo- widely used in mobile devices such as cell phones, note- nents. Instead of using organic electrolyte, a lithium ion book PCs and PDAs. However, since lithium ion secondary conductive ceramic, known as a solid electrolyte, is used. -
Fluid and Electrolyte Therapy Lyon Lee DVM Phd DACVA Purposes of Fluid Administration During the Perianesthetic Period
Fluid and Electrolyte Therapy Lyon Lee DVM PhD DACVA Purposes of fluid administration during the perianesthetic period • Replace insensible fluid losses (evaporation, diffusion) during the anesthetic period • Replace sensible fluid losses (blood loss, sweating) during the anesthetic period • Maintain an adequate and effective blood volume • Maintain cardiac output and tissue perfusion • Maintain patency of an intravenous route of drug administration Review normal body water distribution • 1 gm = 1 ml; 1 kg = 1 liter; 1 kg = 2.2 lbs • Total body water: 60% of body weight • Intracellular water: 40% of body weight • Extracellular water (plasma water + interstitial water): 20% of body weight • Interstitial water: 20 % of body weight • Plasma water: 5 % of body weight • Blood volume: 9 % of body weight (blood volume = plasma water + red blood cell volume) • Inter-compartmental distribution of water is maintained by hydrostatic, oncotic, and osmotic forces • Daily water requirement: 1-3 ml/kg/hr (24-72 ml/kg/day) o 50 ml x body weight (kg) provides rough estimate for daily requirement • Requirements vary with age, environment, disease, etc… 1 Figure 1. Normal body water distribution Body 100% Water Tissue 60 % (100) 40 % Intracellular space Extracellular space 40 % (60) 20 % (40) Interstitial space Intravascular space 15 % (30) 5 % (10) Fluid movement across capillary membranes • Filtration is governed by Starling’s equation as below • Net driving pressure into the capillary = [(Pc – Pi) – (πp – πi)] o Pc = capillary hydrostatic pressure (varies from artery to vein) o Pi = interstitial hydrostatic pressure (0) o πp = plasma oncotic pressure (28 mmHg) o πi = interstitial oncotic pressure (3 mmHg) • If colloid osmotic pressure (COP) in the capillaries decreases lower than the COP in the interstitium, fluid will move out of the vessels and edema will develop. -
Zinc Anode-Compatible In-Situ Solid Electrolyte Interphase Via Cation Solvation Modulation
ARTICLE https://doi.org/10.1038/s41467-019-13436-3 OPEN Zinc anode-compatible in-situ solid electrolyte interphase via cation solvation modulation Huayu Qiu1,2,4, Xiaofan Du1,4, Jingwen Zhao1*, Yantao Wang1, Jiangwei Ju1, Zheng Chen1, Zhenglin Hu1, Dongpeng Yan 3, Xinhong Zhou2* & Guanglei Cui1* The surface chemistry of solid electrolyte interphase is one of the critical factors that govern the cycling life of rechargeable batteries. However, this chemistry is less explored for zinc 1234567890():,; anodes, owing to their relatively high redox potential and limited choices in electrolyte. Here, we report the observation of a zinc fluoride-rich organic/inorganic hybrid solid electrolyte interphase on zinc anode, based on an acetamide-Zn(TFSI)2 eutectic electrolyte. A combi- nation of experimental and modeling investigations reveals that the presence of anion- complexing zinc species with markedly lowered decomposition energies contributes to the in situ formation of an interphase. The as-protected anode enables reversible (~100% Coulombic efficiency) and dendrite-free zinc plating/stripping even at high areal capacities (>2.5 mAh cm‒2), endowed by the fast ion migration coupled with high mechanical strength of the protective interphase. With this interphasial design the assembled zinc batteries exhibit excellent cycling stability with negligible capacity loss at both low and high rates. 1 Qingdao Industrial Energy Storage Research Institute, Qingdao Institute of Bioenergy and Bioprocess Technology, Chinese Academy of Sciences, Qingdao 266101, P. R. China. 2 College of Chemistry and Molecular Engineering, Qingdao University of Science and Technology, Qingdao 266042, P. R. China. 3 College of Chemistry, Beijing Normal University, Beijing Key Laboratory of Energy Conversion and Storage Materials, Beijing 100875, P.