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An Overview of Battery Simulation Robert Spotnitz, Battery Design LLC Overview A. Battery History B. Battery Market and Technology C. Battery Modeling 2 What is a battery? A battery or galvanic cell converts chemical energy to


  1. An Overview of Battery Simulation Robert Spotnitz, Battery Design LLC

  2. Overview A. Battery History B. Battery Market and Technology C. Battery Modeling 2

  3. What is a battery? • A battery or “galvanic cell” converts chemical energy to electrochemical energy using at least one of reactant stored in a cell . • A fuel cell converts chemical energy to electrochemical energy using reactants stored externally. • A capacitor stores and releases electrical energy using double-layer charge separation or a pseudo-capacitive effect such as surface adsorption, reaction or bulk intercalation. Volta’s pile Ag/Zn (1800) 3

  4. Terminology e -  e -  Battery consists of one or more cells Cell consists of a pair of electrodes and an ion conductor Ag 2 O  2Ag Electrode consists of active Zn  ZnO material, current collector, and OH - e -   e - tab Positive electrode is called “cathode” Negative electrode is called ionic “anode” conductor Package, separator, insulators,       etc. Zn 2 OH ZnO H O 2 e 2       Ag O H O 2 e 2 Ag 2 OH 2 2    Ag O Zn 2 Ag ZnO 4 2

  5. 1991: Li Ion 1959: Alkaline 1980s: NiMH 1958: Organic Li primary 1947: O 2 1994: Doyle, Fuller, Recomb. Newman, DUAL Ni/Cd model Li Ion 2005: Garcia et al., 1962: Newman and Tobias, microstructural 1866: Dry cell Porous Electrode Theory model 1860: Pb Acid 1800: Volta invents battery 1930: Butler-Volmer Eqn 1905: Nernst Equation:  G=-nFE               1887: Peukert’s Law: I p  t d =constant a c i i exp exp     o       RT RT 5 1834: Faraday’s law of electrolysis

  6. Battery Market Only a few chemistries dominate market Rechargeable - Pb Acid - Lithium Ion Primary or single discharge - Alkaline

  7. North American Lead Acid SLI Battery Forecast @ $60/battery ~$8 Billions 7

  8. Worldwide Rechargeable Battery Sales Excluding Lead Acid by application Lithium Ion NiMH NiCd Lithium-ion dominates market for portable electronics. C. Pillot, Batteries 2009, Avicenne 8

  9. Li-Ion Cell World Market Size & Forecast ($Billions) 35 Consumer Other 30 25 Industrial Automotive 20 15 10 5 Huge growth in conversion used $1 = 100 Yen lithium-ion market Consumer - phones, computers, cameras, etc. Other - power tools, e-bikes, medical, aerospace is forecast for Industrial - smart-grid, residential, UPS vehicles Automotive - passenger vehicles excluding bus, railroad 9 S. Inagaki, Yano Research Institute, SAE Intl. Vehicle Battery Summit, Shangahi 2011

  10. Battery Requirements: Consumer Products • Consumer • Trends electronics – longer calendar life – high volumetric energy density – higher energy – low cost density – 1 year life – Safety • Power tools – high power density – low cost Largest market and – 2-3 year life growing. – safety 10

  11. Battery Requirements: Hybrid Electric Vehicles Typical is ~1 kWh systems • High Power (> 1 capable of providing ~25 kW kW/kg) • Low cost • 8+ year life • Abuse tolerance Nickel metal hydride batteries dominate but lithium-ion is projected to win out by providing smaller, lower cost packs 11

  12. Battery Requirements: Battery Electric Vehicles • High gravimetric Typical is 24 kWh systems capable of providing ~50 kW energy density (>100 Wh/kg) • Very low cost • 8+ year life • Abuse tolerance Lithium-ion is currently only viable chemistry with sufficient energy density for this application. 12

  13. Battery Requirements: Grid Regulation • High power, fast response (seconds) • Cost? Life? Abuse? Market is potentially larger than automotive, but large uncertainty as to economic feasibility. 13

  14. Lead Acid (Valve Regulated) - Actives and Separator Positive 2   cm 5 Negative a 2.3 10 2   cm 3 4 a 2.3 10 cm 3 cm   ~ 2 mm thick 40% ~ 2 mm thick   45% Charged PbO2 + 2e +2H + + 2H2SO4 Pb + H2SO4  PbSO4 + 2e + 2H +  PbSO4 + 2H2O Discharged Sep ~95% porous, ~1.3 mm thick D. Pavlov, V. Iliev, J. Power Src / 7 (1981) 153. J. H. Yan et al. , J. Power Src. 133 (2004) Lead-acid electrochemistry is very complex. 135-140.

  15. Li-ion Cell Cross-Section Li + + e + Mn2O4  LiMn2O4 LiC 6  Li + + e + C 6 Z. G. Li et al. J. Electrochem. Soc. , 150 (9) A1171 (2003) Lithium ion battery operation is relatively simple. 15

  16. Typical Lead-Acid Battery DOE-HDBK-1084-95 September 1995 16

  17. Spirally-Wound Cells 17

  18. Tesla Powertrain Technology Small Cells 18650 K. Kelty, 26 th Intl. Battery Sem., Ft. Lauderdale, Fl, 2009 18

  19. Mitsubishi iMiEV Battery 22 modules (4 cells/module) 19

  20. Summary • 2011 World Markets for Batteries – Primary • estimated at ~$4 Billions for alkaline and ~$1.5 billions for others – Rechargeable • lead acid ~$20 Billions • lithium ion ~$12 Billions • nickel metal hydride ~$1.5 Billions • Automotive market is growing rapidly and is amenable to design • Opportunities for – design tools for batteries – prediction of life and abuse tolerance 20

  21. Overview A. Battery History B. Battery Market C. Battery Modeling 21

  22. Battery Modeling • Concept of Electroactive Species • Concept of Exchange Current Density • Battery Equations and Modeling Approaches 22

  23.  1  +  2 c           3 o Fe F G RT ln 1 2 c  2 Fe Nernst Equation Can compute voltage based on chemistry. 23

  24.  1  +  2 c           3 o Fe F G RT ln 1 2 c  2 Fe Nernst Equation Can compute voltage based on chemistry. 24

  25.  +      1 3 2 Fe e Fe            c 1 2 i k c exp    f f , o 3   Fe RT      2 3 Fe Fe e 2          a 1 2 i k c exp    2 b b , o   Fe RT   i i i net f b Butler-Volmer Equation Can compute reaction rates. 25

  26.  +      1 3 2 Fe e Fe            c 1 2 i k c exp    f f , o 3   Fe RT      2 3 Fe Fe e 2          a 1 2 i k c exp    , 2 b b o   Fe RT   i i i net f b Butler-Volmer Equation Can compute reaction rates. 26

  27. Lead Acid Battery   1 , Pb 1 PbO , 2   2 2     PbO 2 H SO Pb 2 PbSO 2 H O 27 2 2 4 4 2

  28.     Pb 2 H SO PbO 2 PbSO 2 H O 2 4 2 4 2   1 , Pb 1 PbO , 2   2 2 28

  29.   1 , Pb 1 PbO , 2  T        c p k T S Eulerian strain        t 1 T       * E I X X    x x RT 2         o  i 1 2 t ln a 2  2 2  F c       D c 2  i 2  t Ohm ' s Law               i i 1 v  1 1 t       Poisson 2 PbO 2 H SO 2 e PbSO 2 H O SO 2 2 4 4 2 4                       2   2 a 1 2 c 1 2 j k exp k c exp j      j PbO , a   PbO , c H SO   RT RT 2 2 2 4 1 j      2 Pb SO PbSO 2 e 4 4                    a 1 2 c 1 2 j k c exp k exp      , 2 , Pb a   Pb a   SO RT RT 4 29

  30. Macro-Homogeneous Modeling Phenomena included in macro- J. Newman, C. Tobias, “Theoretical Analysis of homogeneous battery models Current Distribution in Porous Electrodes,” J. Echem. (partial) Soc ., 109,1183 (1962) L Separator • multi-component electrolytes • precipitation • side reactions Negative Positive • particle size distribution Electrode Electrode • mixtures of active materials • expansion/contraction of particles • convection • current distribution along r collectors • local heat generation • stress generation r  2 2 L 30

  31. Hierarchy of Battery Simulation STAR-CCM+ Vehicle Module/Pack C BD Full Cell Unit Cell Hierarchy enables higher level models to be built on lower level models. 31

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