System and method for rapid charging lithium ion battery
US-2020136173-A1 · Apr 30, 2020 · US
US12237708B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12237708-B2 |
| Application number | US-202017004118-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 27, 2020 |
| Priority date | Dec 6, 2018 |
| Publication date | Feb 25, 2025 |
| Grant date | Feb 25, 2025 |
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A charging apparatus includes a control unit configured to determine an average ion concentration, a surface ion concentration and a solid phase potential for anode particles and an electrolyte potential in an anode, using a predefined electrochemical reduced order model. The control unit is further configured to determine a side reaction rate from the solid phase potential and the electrolyte potential. The control unit is further configured to reduce the magnitude of the charging current applied to a secondary battery based on at least one of a cutoff voltage, the surface ion concentration and the side reaction rate.
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What is claimed is: 1. A charging apparatus of a secondary battery, comprising: a voltage sensor configured to measure a voltage of the secondary battery; a temperature sensor configured to measure a temperature of the secondary battery; and a control unit configured to receive a measured voltage value and a measured temperature value from the voltage sensor and the temperature sensor, respectively, and to adjust a magnitude of a charging current applied to the secondary battery, wherein the control unit is configured to: determine an internal state of the secondary battery, which includes an average ion concentration of anode particles, a surface ion concentration of the anode particles, an anode particle potential and an anode electrolyte potential, using a predefined electrochemical reduced order model (ROM); determine a state of charge (SOC) of the secondary battery from the average ion concentration; determine a side reaction rate from the anode particle potential and the anode electrolyte potential; determine whether the measured voltage value reaches a cutoff voltage; determine whether the surface ion concentration of the anode particles reaches an upper limit concentration; determine whether the side reaction rate reaches an upper limit rate; and reduce the magnitude of the charging current applied to the secondary battery from a current charging current amount to an updated charging current amount in response to the measured voltage value reaching the cutoff voltage; reduce the magnitude of the charging current applied to the secondary battery from the current charging current amount to the updated charging current amount in response to the surface ion concentration of the anode particles reaching the upper limit concentration; and reduce the magnitude of the charging current applied to the secondary battery from the current charging current amount to the updated charging current amount in response to the side reaction rate reaching the upper limit rate, wherein the updated charging current amount corresponds to an updated SOC value in a prestored profile correlating charging rate values to SOC values, and wherein the updated SOC value is greater than the determined SOC of the secondary battery by a predetermined amount, wherein the predetermined amount is a constant value regardless of the determined SOC of the secondary battery. 2. The charging apparatus according to claim 1 , wherein the electrochemical reduced order model is derived from a full order model defined by an ion conservation equation in an electrode, an ion conservation equation in an electrolyte, a charge conservation equation in the electrode, a charge conservation equation in the electrolyte and an electrochemical kinetics equation, wherein the ion conservation equation in the electrode is represented by: ∂ c s ∂ t = D s r 2 ∂ ∂ r ( r 2 ∂ c s ∂ r ) 1 2 ∂ c s ∂ r | r = 0 = 0 and D s ∂ c s ∂ r | r = R s = - j Li a s F wherein C s is an ion concentration in solid phase, D s is a diffusion coefficient in solid phase, R s is a radius of a spherical electrode particle, j Li is a lithium reaction rate, a s is a specific surface area of the electrode, F is a Faraday constant, and r is a spherical coordinate wherein the ion conservation equation in the electrolyte is represented by: ∂ ( ɛ e c e ) ∂ f = ∂ ∂ x ( D
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