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LEAD ACID BATTERY MODELING IEEE ESSB Summer 2016 Meeting
Frank X. Garcia 12 June 2016
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Presentation Objectives
Explain lead acid cell operation at the atomic level Present a Randles circuit model approximation of a lead acid cell Examine computer simulations trending using Randles circuit model
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Outline Battery Overview Randles circuit model Components
Electrochemistry Double layer capacitance State of health parameters Randles circuit model Single cell approximation Failure modes analysis Computer Simulations
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Battery Components A battery is an energy storage device
Converts chemical energy into electrical energy during a discharge, and can also Store electrical energy during a recharge The major components of a lead acid battery include: ELECTROLYTE - aqueous conductor of ions between the negative and positive plates, H2SO4 with H20 (38% concentration of sulfuric acid) ANODE - terminal post connected to the negative plates CATHODE- terminal post connected to the positive plates NEGATIVE PLATES - lead grids filled with pure, spongy Pb POSITIVE PLATES - lead grids filled with PbO2 SEPARATOR - non-conductive material that separates the negative and positive plates and prevents them from shorting The negative battery post terminal connects to a spongy lead (Pb) electrode grid The positive battery post terminal connects to a porous lead dioxide (PbO2) electrode grid Electrodes are arranged in a parallel matrix cluster of interspersed positive and negative electrodes, separated and immersed in electrolyte fluid, in which same voltage polarity electrodes are attached to each other Electrode matrix cluster creates one cell. Multiple electrode clusters are connected in series to form a battery. Electrolyte maintains chemical balance by maintaining system neutrality. Electrolyte contains sulfuric acid (H2SO4) in water (H20) to form an ionic media, in which ions pass in-between electrodes. Both plates are immersed in electrolyte fluid Separators are porous and conductive (???) and keep electrodes from shorting to each other.
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Electrochemistry - New electrodes inserted into electrolyte
Cathode + - Anode Cathode + H2O H+ SO4-2 Pb+2 - - Anode PbO2 Pb0 H2O H+ SO4-2 H+ H+ H+ SO4-2 SO4-2 H+ New electrodes inserted into electrolyte Reduction Oxidation
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Electrochemistry Reduction Oxidation - @ T = 25C - Anode
0V -0.36 V 1.69V Double Layer Capacitances Diffusion Layer s* * Discussed Later Vcell = 1.69V – (-0.36V) = 2.05V Cathode + H2O H+ SO4-2 Pb+2 - - Anode @ T = 25C Reduction Pb+4 + 2O-2(s) + 4H+(aq) + SO4-2(aq) + 2e PbSO4(s) + 2H2O(aq) Energy released E0 = 1.69 eV Oxidation Pb(s) + SO4-2(aq) PbSO4(s) + 2e- Energy released E0 = eV
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Charge Cycle: Electrochemical process is reversed
Electrochemistry Discharge Cycle Charge Cycle: Electrochemical process is reversed Vcell + - - I Iload - H2O H2O H+ SO4-2 - - - H2O SO4-2 SO4-2 Pb+2 Pb+2 Reduction Oxidation
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Double Layer Capacitance
Ions adsorbed to the surface of the electrode held by electrostatic force Positive ions too large to penetrate electrode metal surface Only electrons can travel through the metal conduction bands Solvated ions encapsulated by water molecules can migrate through diffusion layer A second layer of solvated ions create the outer layer forming capacitive double layer Double layer has an ionic density gradient which allow Ionic migration in the diffusion layer Bulk region maintains an equal concentration of electrolyte
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State of Health Parameters
Float voltage Set to recommended range for optimal battery life Life expectancy decreases as float voltage increases Float current A high float current indicates aging battery Negative post temperature Indefinite 10o C temperature rise decrease battery life by 50% Electrolyte Specific Gravity Sulfuric acid (H2SO4) concentration can indicate state of charge Fully charged: 1.26 to 1.3 specific gravity Admittance/Impedance/Resistance Trending Admittance will decrease as the battery ages Impedance and Resistance will increase as battery ages
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Complete Randles Circuit Model
Rm+ Rm- Lumped, metallic resistance of the posts, bus bars, grids, plates, and metallic joints at the cathode, Rm+, and the anode, Rm- Cdl+ Cdl- Double layer capacitance at the interface between the positive plate surface and the electrolyte, Cdl+, and the negative plate surface and the electrolyte interface, Cdl-. Cdl depends on the effective surface area of each plate, and the battery state of charge, and it is a combination of the series connection of a double layer capacitor and a diffusion layer capacitor. Rct+ Rct- Equivalent charge transfer resistance at the interface between the positive plate and the electrolyte due to the ionization losses of Pb, Rct+, and the interface between the negative plate and the electrolyte, Rct-. These are resistive paths that are tunneled through Cdl+ and Cdl-, respectively. Zdiff+ Zdiff- Diffusion layer impedance in the diffusion layer near the positive plate, Zdiff+, and the negative plate, Zdiff-. These elements are modeled using the Warburg Diffusion Element, which has a constant phase at all frequencies and a magnitude inversely proportional to the frequency. Refer to Appendix A for a review of the Warburg Diffusion Element. Cbulk Equivalent bulk capacitance of the electrolyte material. Note: Cbulk >> Cdl+, Cdl-. Rbulk Equivalent bulk resistance of the electrolyte material 1.69V Voltage potential at the cathode relative to the bulk electrolyte, stemming from the Reduction release of energy -0.36V Voltage potential at the negative plate relative to the bulk electrolyte, stemming from the Oxidation release of energy
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Randles Circuit Model Simplification
Step 1 Ignore Cbulk since its magnitude is much larger than Cdl- and Cd+ Step 2 Add the series resistances Rm+, Rm- and Rbulk Step 3 Add the 2 voltage potentials V +0.36V = 2.05V
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Randles Circuit Model Simplification
Note 1 Most models in the literature combine the half-cell circuits resulting in Cdl_eq, Rct_eq and Zdiff_eq Note 2 Many models in the literature often ignore Zdiff
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Failure Modes Analysis
Description Battery Admittance Corrosion Negative strap corrosion Plate lugs, plate strap/lead corrosion Positive grid corrosion (grid expansion) Part of aging process Decreases Dry-out Electrolyte Reduction due to overcharging Premature capacity loss Shedding of positive active material due to heavy cycling Sulphation Negative electrode irreversible sulphation (lead sulfate crystallizing on plate due to undercharging) Electrolyte Stratification Electrolyte settles to the bottom of the cell when not in use or not fully charged Loss of Compression VRLA glass mat
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Randles Circuit Parameters Progression
Listed research shows that Randles circuit parameters can represent battery aging affects and failure modes. A SINGLE INTEGRATED CIRCUIT APPROACH TO REAL CAPACITY ESTIMATION AND LIFE MANAGEMENT OF VRLA BATTERIES N.D. Scott Guardian Link Ltd, United Kingdom Scott NO., Schooling S. A breakthrough in on"line VRLA battery testing. Proc.ERA battery conference 98- Schooling S, Welstead P, 'et aI. A systems identification approach to the analysis of VRLA batteries. Proc. INTELEC 1999 Champlin KS., Bertness K. A fundamentally new approach to battery, performance analysis using DFRAIDFIS technology. Proc. INTELEC 2000 Randles circuit parameters progression over the cell lifetime or discharge
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Complete Randles Model
Computer Simulations Strategy Examine degradation of a cell using complete Randles Circuit Model Simulate Nyquist plots of baseline, +20% and +40% impedance due to cell aging Synthesize component values to determine parametric changes Circuit Model (one cell) Schematic Designation Equivalent, Complete Randles Model R3 Rm+ + Rm- R1 Rct+ C1 Cdl+ R2 Rct- C2 Cdl- X1 Zdiff+ (Warburg Constant Phase Element, cpe) X2 Zdiff- (Warburg Constant Phase Element, cpe) C3 Cbulk R4 Rbulk
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Computer Simulations Zim Zre Nyquist Plots Component Synthesis
Baseline impedance: 1 +20% Impedance: 2 Component Synthesis Schematic Designation Randles Equivalent Change From Baseline R3 Rm+ + Rm- R1 Rct+ C1 Cdl+ R2 Rct- C2 Cdl- C* Zdiff+ Zdiff- * - C3 Cbulk R4 Rbulk 1 2 Zim Figure 1 reference and +20% aged/degraded impedance curve Battery Aged/Degraded by 20% Nyquist plot of reference battery impedance with an aged/degraded 20% increased battery impedance. Smaller curve represents the reference battery impedance and the wider curve is the degraded impedance curve. Most synthesized battery component values appear to track the impedance spectra. So if the battery degrades, then its impedance increases, and battery model values would trend accordingly. Battery model resistor components should increase and capacitor values should decrease. 5kHz Hz Zre * C – constant of the Warburg element, - constant phase of the Warburg element
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Computer Simulations Zim Zre Nyquist Plots Component Synthesis
Baseline impedance: 1 +40% Impedance: 2 Component Synthesis Schematic Designation Randles Equivalent Change From Baseline R3 Rm+ + Rm- + R1 Rct+ C1 Cdl+ - R2 Rct- C2 Cdl- C* Zdiff+ Zdiff- * - C3 Cbulk R4 Rbulk 1 2 Zim Figure 1 reference and +20% aged/degraded impedance curve Battery Aged/Degraded by 20% Nyquist plot of reference battery impedance with an aged/degraded 20% increased battery impedance. Smaller curve represents the reference battery impedance and the wider curve is the degraded impedance curve. Most synthesized battery component values appear to track the impedance spectra. So if the battery degrades, then its impedance increases, and battery model values would trend accordingly. Battery model resistor components should increase and capacitor values should decrease. 5kHz Hz Zre * C – constant of the Warburg element, - constant phase of the Warburg element
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Summary Randles circuit model approximates electrochemistry of a lead acid cell Simplified Randles circuit model reduces analysis accuracy Trending in Randles element values add visibility to battery state of health Baseline immitance using Discrete Frequency Immitance Spectroscopy Synthesize Randles circuit model battery elements Analyze battery degradation by comparing element value changes from a known reference
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