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State of charge dependent plating estimation and prevention — Cps Technology Holdings Llc (US20250192246A1)

Cps Technology Holdings Llc · Google Patents
Google Patents · Patents · License: Open Access
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cpstechnologyholdingsllc
patent, google patents, intellectual property, US20250192246A1, Cps Technology Holdings Llc, Zhenli Zhang, en, 2025

ABSTRACT

Abstract

A battery system includes a lithium ion battery configured to couple to an electrical system, and a battery management system configured to electrically couple to the lithium ion battery and to control one or more recharge parameters of the lithium ion battery. The battery management system is programmed with an electrochemical model, and the battery management system is configured to monitor parameters of the lithium ion battery, and to control the one or more recharge parameters of the lithium ion battery based on the electrochemical model and the one or more monitored parameters. The electrochemical model determines lithium plating reaction kinetics at an anode of the lithium ion battery, determines a quantity of plated lithium at the anode of the lithium ion battery, or both, and indicates a relationship between the one or more monitored parameters and the lithium plating reaction kinetics, the quantity of plated lithium, or both.

Description

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a Continuation Application of U.S. patent application Ser. No. 18/540,665, entitled “STATE OF CHARGE DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed Dec. 14, 2023; which is a Continuation Application of U.S. patent application Ser. No. 17/958,926, entitled “STATE OF CHARGE DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed Oct. 3, 2022, now U.S. Pat. No. 11,848,426; which is a Continuation Application of U.S. patent application Ser. No. 16/338,994 entitled “STATE OF CHARGE DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed Apr. 2, 2019, now U.S. Pat. No. 11,462,774; which is a U.S. National Stage Application under 35 U.S.C. § 371 of International Application No. PCT/US2017/054939 entitled “STATE OF CHARGE DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed on Oct. 3, 2017; which claims priority to and the benefit of U.S. Provisional Application No. 62/403,574, entitled “STATE OF CHARGE (“SOC”) DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed Oct. 3, 2016. Each of the proceeding applications is incorporated herein by reference.

BACKGROUND

The present disclosure generally relates to the field of batteries and battery modules. More specifically, the present disclosure relates to controlling charging operations of lithium ion batteries to reduce a likelihood of lithium plating on anodes of the lithium ion batteries.

This section is intended to introduce the reader to various aspects of art that may be related to various aspects of the present disclosure, which are described below. This discussion is believed to be helpful in providing the reader with background information to facilitate a better understanding of the various aspects of the present disclosure. Accordingly, it should be understood that these statements are to be read in this light, and not as admissions of prior art.

A vehicle that uses one or more battery systems for providing all or a portion of the motive power for the vehicle can be referred to as an xEV, where the term “xEV” is defined herein to include all of the following vehicles, or any variations or combinations thereof, that use electric power for all or a portion of their vehicular motive force. For example, xEVs include electric vehicles (EVs) that utilize electric power for all motive force. As will be appreciated by those skilled in the art, hybrid electric vehicles (HEVs), also considered xEVs, combine an internal combustion engine propulsion system and a battery-powered electric propulsion system, such as 48 Volt (V) or 130V systems. The term HEV may include any variation of a hybrid electric vehicle. For example, full hybrid electric vehicles (FHEVs) may provide motive and other electrical power to the vehicle using one or more electric motors, using only an internal combustion engine, or using both. In contrast, mild hybrid electric vehicles (MHEVs) disable the internal combustion engine when the vehicle is idling and utilize a battery system to continue powering the air conditioning unit, radio, or other electronics, as well as to restart the engine when propulsion is desired. The mild hybrid systems may also apply some level of power assistance, during acceleration for example, to supplement the internal combustion engine. Mild hybrids are typically 96V to 130V and recover braking energy through a belt or crank integrated starter generator. Further, a micro-hybrid electric vehicle (mHEV) also uses a “Stop-Start” system similar to the mild hybrids, but the micro-hybrid systems of a mHEV may or may not supply power assistance to the internal combustion engine and operates at a voltage below 60V. For the purposes of the present discussion, it should be noted that mHEVs typically do not technically use electric power provided directly to the crankshaft or transmission for any portion of the motive force of the vehicle, but an mHEV may still be considered as an xEV since it does use electric power to supplement a vehicle's power needs when the vehicle is idling with internal combustion engine disabled and recovers braking energy through an integrated starter generator. In addition, a plug-in electric vehicle (PEV) is any vehicle that can be charged from an external source of electricity, such as wall sockets, and the energy stored in the rechargeable battery packs drives or contributes to drive the wheels. PEVs are a subcategory of EVs that include all-electric or battery electric vehicles (BEVs), plug-in hybrid electric vehicles (PHEVs), and electric vehicle conversions of hybrid electric vehicles and conventional internal combustion engine vehicles.

xEVs as described above may provide a number of advantages as compared to more traditional gas-powered vehicles using only internal combustion engines and traditional electrical systems, which are typically 12V systems powered by a lead acid battery. For example, xEVs may produce fewer undesirable emission products and may exhibit greater fuel efficiency as compared to traditional internal combustion vehicles and, in some cases, such xEVs may eliminate the use of gasoline entirely, as is the case of certain types of EVs or PEVs.

As technology continues to evolve, there is a need to provide improved power sources, particularly battery modules, for such vehicles. For example, the electric power used by the xEVs may be stored in lithium ion batteries. In some cases, active lithium ions within the lithium ion batteries of xEVs may deposit on an anode of the lithium ion batteries under certain conditions driving a charging operation of the lithium ion batteries. This effect is widely known as lithium plating, and the lithium plating may result in degradation of the lithium ion battery. The present disclosure is generally related to establishing dynamic parameters for charging operations to limit lithium plating on the anode of the lithium ion battery.

SUMMARY

A summary of certain embodiments disclosed herein is set forth below. It should be understood that these aspects are presented merely to provide the reader with a brief summary of these certain embodiments and that these aspects are not intended to limit the scope of this disclosure. Indeed, this disclosure may encompass a variety of aspects that may not be set forth below.

The present disclosure relates to a battery system. The battery system includes a lithium ion battery configured to couple to an electrical system, and a battery management system configured to electrically couple to the lithium ion battery and configured to control one or more recharge parameters of the lithium ion battery. The battery management system is programmed with an electrochemical model, and the battery management system is configured to monitor parameters of the lithium ion battery, and to control the one or more recharge parameters of the lithium ion battery based on the electrochemical model and the one or more monitored parameters. The electrochemical model determines lithium plating reaction kinetics at an anode of the lithium ion battery, determines a quantity of plated lithium at the anode of the lithium ion battery, or a combination thereof, and indicates a relationship between the one or more monitored parameters and the lithium plating reaction kinetics, the quantity of plated lithium, or the combination thereof.

The present disclosure also relates to a method to control a charging operation of a lithium ion battery. The method includes measuring one or more parameters of the lithium ion battery during the charging operation; determining lithium plating reaction kinetics at an anode of the lithium ion battery using an electrochemical model, determining a quantity of plated lithium at the anode of the lithium ion battery, or a combination thereof; indicating a relationship between the one or more monitored parameters and the lithium plating reaction kinetics, the quantity of plated lithium, or the combination thereof using the electrochemical model; and controlling the charging operation of the lithium ion battery based on the indicated relationship.

The present disclosure also relates to a lithium ion battery including a housing; a plurality of lithium ion battery cells disposed in the housing; one or more sensors disposed in the housing and configured to monitor one or more parameters of the plurality of lithium ion battery cells; and a battery management system communicatively coupled to the one or more sensors and disposed in the housing. The battery management system is configured to control a charging operation of the lithium ion battery, and is programmed with an electrochemical model comprising equations describing lithium plating reaction kinetics and quantifying plated lithium as a function of the lithium plating reaction kinetics. The battery management system is configured to use the electrochemical model to dynamically control the charging operation based on the one or more monitored parameters and modeled charging parameters generated by the electrochemical model to prevent lithium plating at an anode of the plurality of lithium ion battery cells.

BRIEF DESCRIPTION OF THE DRAWINGS

Various aspects of this disclosure may be better understood upon reading the following detailed description and upon reference to the drawings in which:

FIG. 1 is perspective view of a vehicle (an xEV) having a battery system contributing all or a portion of the power for the vehicle, in accordance with an embodiment of the present disclosure;.

FIG. 2 is a cutaway schematic view of the xEV of FIG. 1 in the form of a hybrid electric vehicle (HEV), in accordance with an embodiment of the present disclosure;

FIG. 3 is a schematic view of a lithium ion battery, in accordance with an embodiment of the present disclosure;

FIG. 4 is a cutaway view of a lithium ion battery cell with a spiral wound cell structure, in accordance with an embodiment of the present disclosure;

FIG. 5 is a process flow diagram describing a method for reducing the likelihood of lithium plating on an anode of a battery based on an electrochemical model of the battery, in accordance with an embodiment of the present approach;

FIG. 6 is a schematic representation of an electrochemical model including a framework for describing reactions at an anode, a separator, and a cathode of a lithium ion battery cell, in accordance with an embodiment of the present approach;

FIG. 7 is a schematic of the major reactions involved in lithium plating at an anode of a battery cell, in accordance with an embodiment of the present approach;

FIGS. 8 and 9 are plots of potential as a function of position at an anode of a battery cell during an initial state in which the battery cell is not being charged, and a state in which the battery cell is being charged, respectively, in accordance with an embodiment of the present approach;

FIG. 10 is a plot of plated lithium growth as a function of anode position for various charging current pulse durations according to the battery cell charging represented in FIG. 9 , in accordance with an embodiment of the present approach;

FIG. 11 is a plot illustrating the various electrical potentials across the anode after the charging current has stopped, in accordance with an embodiment of the present approach;

FIG. 12 is a plot of plated lithium amount as a function of anode position for various charging current pulse durations after the charging pulse has stopped, in accordance with an embodiment of the present approach;

FIG. 13 is a process flow diagram describing a method for reducing the likelihood of lithium plating on an anode of a battery based on current limit maps, degradation maps, and monitored lithium plating kinetics generated by an electrochemical model of the battery, in accordance with an embodiment of the present approach;

FIGS. 14 and 15 are example current limit maps generated by the electrochemical model, in accordance with an embodiment of the present approach;

FIG. 16 is an example battery degradation map generated by the electrochemical model by quantifying lithium plating, in accordance with an embodiment of the present approach;

FIGS. 17 and 18 illustrate driving profile simulation results for battery voltage and battery current, respectively, at a constant temperature T=25° C. and T=0° C., for a simulated battery, in accordance with an embodiment of the present approach;

FIG. 19 is a plot of average volume fraction of plated lithium corresponding to the simulated driving profiles described in FIGS. 17 and 18 , in accordance with an embodiment of the present approach; and

FIGS. 20 and 21 depict current limit maps for T=25° C. and 0° C., respectively, for a relatively thin (power cell) and relatively thick electrode (energy cell) designs generated using an electrochemical model, in accordance with an embodiment of the present approach.

DETAILED DESCRIPTION

One or more specific embodiments will be described below. In an effort to provide a concise description of these embodiments, not all features of an actual implementation are described in the specification. It should be appreciated that in the development of any such actual implementation, as in any engineering or design project, numerous implementation-specific decisions must be made to achieve the developers' specific goals, such as compliance with system-related and business-related constraints, which may vary from one implementation to another. Moreover, it should be appreciated that such a development effort might be complex and time consuming, but would nevertheless be a routine undertaking of design, fabrication, and manufacture for those of ordinary skill having the benefit of this disclosure.

The battery systems described herein may be used to provide power to various types of electric vehicles (xEVs) and other high voltage energy storage/expending applications (e.g., electrical grid power storage systems). Such battery systems may include one or more battery modules, each battery module having a number of battery cells (e.g., lithium-ion (Li-ion) el

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a Continuation Application of U.S. patent application Ser. No. 18/540,665, entitled “STATE OF CHARGE DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed Dec. 14, 2023; which is a Continuation Application of U.S. patent application Ser. No. 17/958,926, entitled “STATE OF CHARGE DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed Oct. 3, 2022, now U.S. Pat. No. 11,848,426; which is a Continuation Application of U.S. patent application Ser. No. 16/338,994 entitled “STATE OF CHARGE DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed Apr. 2, 2019, now U.S. Pat. No. 11,462,774; which is a U.S. National Stage Application under 35 U.S.C. § 371 of International Application No. PCT/US2017/054939 entitled “STATE OF CHARGE DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed on Oct. 3, 2017; which claims priority to and the benefit of U.S. Provisional Application No. 62/403,574, entitled “STATE OF CHARGE (“SOC”) DEPENDENT PLATING ESTIMATION AND PREVENTION,” filed Oct. 3, 2016. Each of the proceeding applications is incorporated herein by reference.

BACKGROUND

The present disclosure generally relates to the field of batteries and battery modules. More specifically, the present disclosure relates to controlling charging operations of lithium ion batteries to reduce a likelihood of lithium plating on anodes of the lithium ion batteries.

This section is intended to introduce the reader to various aspects of art that may be related to various aspects of the present disclosure, which are described below. This discussion is believed to be helpful in providing the reader with background information to facilitate a better understanding of the various aspects of the present disclosure. Accordingly, it should be understood that these statements are to be read in this light, and not as admissions of prior art.

A vehicle that uses one or more battery systems for providing all or a portion of the motive power for the vehicle can be referred to as an xEV, where the term “xEV” is defined herein to include all of the following vehicles, or any variations or combinations thereof, that use electric power for all or a portion of their vehicular motive force. For example, xEVs include electric vehicles (EVs) that utilize electric power for all motive force. As will be appreciated by those skilled in the art, hybrid electric vehicles (HEVs), also considered xEVs, combine an internal combustion engine propulsion system and a battery-powered electric propulsion system, such as 48 Volt (V) or 130V systems. The term HEV may include any variation of a hybrid electric vehicle. For example, full hybrid electric vehicles (FHEVs) may provide motive and other electrical power to the vehicle using one or more electric motors, using only an internal combustion engine, or using both. In contrast, mild hybrid electric vehicles (MHEVs) disable the internal combustion engine when the vehicle is idling and utilize a battery system to continue powering the air conditioning unit, radio, or other electronics, as well as to restart the engine when propulsion is desired. The mild hybrid systems may also apply some level of power assistance, during acceleration for example, to supplement the internal combustion engine. Mild hybrids are typically 96V to 130V and recover braking energy through a belt or crank integrated starter generator. Further, a micro-hybrid electric vehicle (mHEV) also uses a “Stop-Start” system similar to the mild hybrids, but the micro-hybrid systems of a mHEV may or may not supply power assistance to the internal combustion engine and operates at a voltage below 60V. For the purposes of the present discussion, it should be noted that mHEVs typically do not technically use electric power provided directly to the crankshaft or transmission for any portion of the motive force of the vehicle, but an mHEV may still be considered as an xEV since it does use electric power to supplement a vehicle's power needs when the vehicle is idling with internal combustion engine disabled and recovers braking energy through an integrated starter generator. In addition, a plug-in electric vehicle (PEV) is any vehicle that can be charged from an external source of electricity, such as wall sockets, and the energy stored in the rechargeable battery packs drives or contributes to drive the wheels. PEVs are a subcategory of EVs that include all-electric or battery electric vehicles (BEVs), plug-in hybrid electric vehicles (PHEVs), and electric vehicle conversions of hybrid electric vehicles and conventional internal combustion engine vehicles.

xEVs as described above may provide a number of advantages as compared to more traditional gas-powered vehicles using only internal combustion engines and traditional electrical systems, which are typically 12V systems powered by a lead acid battery. For example, xEVs may produce fewer undesirable emission products and may exhibit greater fuel efficiency as compared to traditional internal combustion vehicles and, in some cases, such xEVs may eliminate the use of gasoline entirely, as is the case of certain types of EVs or PEVs.

As technology continues to evolve, there is a need to provide improved power sources, particularly battery modules, for such vehicles. For example, the electric power used by the xEVs may be stored in lithium ion batteries. In some cases, active lithium ions within the lithium ion batteries of xEVs may deposit on an anode of the lithium ion batteries under certain conditions driving a charging operation of the lithium ion batteries. This effect is widely known as lithium plating, and the lithium plating may result in degradation of the lithium ion battery. The present disclosure is generally related to establishing dynamic parameters for charging operations to limit lithium plating on the anode of the lithium ion battery.

SUMMARY

A summary of certain embodiments disclosed herein is set forth below. It should be understood that these aspects are presented merely to provide the reader with a brief summary of these certain embodiments and that these aspects are not intended to limit the scope of this disclosure. Indeed, this disclosure may encompass a variety of aspects that may not be set forth below.

The present disclosure relates to a battery system. The battery system includes a lithium ion battery configured to couple to an electrical system, and a battery management system configured to electrically couple to the lithium ion battery and configured to control one or more recharge parameters of the lithium ion battery. The battery management system is programmed with an electrochemical model, and the battery management system is configured to monitor parameters of the lithium ion battery, and to control the one or more recharge parameters of the lithium ion battery based on the electrochemical model and the one or more monitored parameters. The electrochemical model determines lithium plating reaction kinetics at an anode of the lithium ion battery, determines a quantity of plated lithium at the anode of the lithium ion battery, or a combination thereof, and indicates a relationship between the one or more monitored parameters and the lithium plating reaction kinetics, the quantity of plated lithium, or the combination thereof.

The present disclosure also relates to a method to control a charging operation of a lithium ion battery. The method includes measuring one or more parameters of the lithium ion battery during the charging operation; determining lithium plating reaction kinetics at an anode of the lithium ion battery using an electrochemical model, determining a quantity of plated lithium at the anode of the lithium ion battery, or a combination thereof; indicating a relationship between the one or more monitored parameters and the lithium plating reaction kinetics, the quantity of plated lithium, or the combination thereof using the electrochemical model; and controlling the charging operation of the lithium ion battery based on the indicated relationship.

The present disclosure also relates to a lithium ion battery including a housing; a plurality of lithium ion battery cells disposed in the housing; one or more sensors disposed in the housing and configured to monitor one or more parameters of the plurality of lithium ion battery cells; and a battery management system communicatively coupled to the one or more sensors and disposed in the housing. The battery management system is configured to control a charging operation of the lithium ion battery, and is programmed with an electrochemical model comprising equations describing lithium plating reaction kinetics and quantifying plated lithium as a function of the lithium plating reaction kinetics. The battery management system is configured to use the electrochemical model to dynamically control the charging operation based on the one or more monitored parameters and modeled charging parameters generated by the electrochemical model to prevent lithium plating at an anode of the plurality of lithium ion battery cells.

BRIEF DESCRIPTION OF THE DRAWINGS

Various aspects of this disclosure may be better understood upon reading the following detailed description and upon reference to the drawings in which:

FIG. 1 is perspective view of a vehicle (an xEV) having a battery system contributing all or a portion of the power for the vehicle, in accordance with an embodiment of the present disclosure;.

FIG. 2 is a cutaway schematic view of the xEV of FIG. 1 in the form of a hybrid electric vehicle (HEV), in accordance with an embodiment of the present disclosure;

FIG. 3 is a schematic view of a lithium ion battery, in accordance with an embodiment of the present disclosure;

FIG. 4 is a cutaway view of a lithium ion battery cell with a spiral wound cell structure, in accordance with an embodiment of the present disclosure;

FIG. 5 is a process flow diagram describing a method for reducing the likelihood of lithium plating on an anode of a battery based on an electrochemical model of the battery, in accordance with an embodiment of the present approach;

FIG. 6 is a schematic representation of an electrochemical model including a framework for describing reactions at an anode, a separator, and a cathode of a lithium ion battery cell, in accordance with an embodiment of the present approach;

FIG. 7 is a schematic of the major reactions involved in lithium plating at an anode of a battery cell, in accordance with an embodiment of the present approach;

FIGS. 8 and 9 are plots of potential as a function of position at an anode of a battery cell during an initial state in which the battery cell is not being charged, and a state in which the battery cell is being charged, respectively, in accordance with an embodiment of the present approach;

FIG. 10 is a plot of plated lithium growth as a function of anode position for various charging current pulse durations according to the battery cell charging represented in FIG. 9 , in accordance with an embodiment of the present approach;

FIG. 11 is a plot illustrating the various electrical potentials across the anode after the charging current has stopped, in accordance with an embodiment of the present approach;

FIG. 12 is a plot of plated lithium amount as a function of anode position for various charging current pulse durations after the charging pulse has stopped, in accordance with an embodiment of the present approach;

FIG. 13 is a process flow diagram describing a method for reducing the likelihood of lithium plating on an anode of a battery based on current limit maps, degradation maps, and monitored lithium plating kinetics generated by an electrochemical model of the battery, in accordance with an embodiment of the present approach;

FIGS. 14 and 15 are example current limit maps generated by the electrochemical model, in accordance with an embodiment of the present approach;

FIG. 16 is an example battery degradation map generated by the electrochemical model by quantifying lithium plating, in accordance with an embodiment of the present approach;

FIGS. 17 and 18 illustrate driving profile simulation results for battery voltage and battery current, respectively, at a constant temperature T=25° C. and T=0° C., for a simulated battery, in accordance with an embodiment of the present approach;

FIG. 19 is a plot of average volume fraction of plated lithium corresponding to the simulated driving profiles described in FIGS. 17 and 18 , in accordance with an embodiment of the present approach; and

FIGS. 20 and 21 depict current limit maps for T=25° C. and 0° C., respectively, for a relatively thin (power cell) and relatively thick electrode (energy cell) designs generated using an electrochemical model, in accordance with an embodiment of the present approach.

DETAILED DESCRIPTION

One or more specific embodiments will be described below. In an effort to provide a concise description of these embodiments, not all features of an actual implementation are described in the specification. It should be appreciated that in the development of any such actual implementation, as in any engineering or design project, numerous implementation-specific decisions must be made to achieve the developers' specific goals, such as compliance with system-related and business-related constraints, which may vary from one implementation to another. Moreover, it should be appreciated that such a development effort might be complex and time consuming, but would nevertheless be a routine undertaking of design, fabrication, and manufacture for those of ordinary skill having the benefit of this disclosure.

The battery systems described herein may be used to provide power to various types of electric vehicles (xEVs) and other high voltage energy storage/expending applications (e.g., electrical grid power storage systems). Such battery systems may include one or more battery modules, each battery module having a number of battery cells (e.g., lithium-ion (Li-ion) electrochemical cells) arranged and electrically interconnected to provide particular voltages and/or currents useful to power, for example, one or more components of an xEV. As another example, battery modules in accordance with present embodiments may be incorporated with or provide power to stationary power systems (e.g., non-automotive systems).

Based on the advantages over traditional gas-powered vehicles, manufactures, which generally produce traditional gas-powered vehicles, may desire to utilize improved vehicle technologies (e.g., regenerative braking technology) within their vehicle lines. Often, these manufacturers may utilize one of their traditional vehicle platforms as a starting point. Accordingly, since traditional gas-powered vehicles are designed to utilize 12 volt battery systems, a 12 volt lithium ion battery may be used to supplement a 12 volt lead-acid battery. More specifically, the 12 volt lithium ion battery may be used to more efficiently capture electrical energy generated during regenerative braking and subsequently supply electrical energy to power the vehicle's electrical system.

As advancements occur with vehicle technologies, relatively high voltage electrical devices may also be included in the vehicle's electrical system. For example, the lithium ion battery may supply electrical energy to an electric motor in a mild-hybrid vehicle. Often, these high voltage electrical devices utilize voltage greater than 12volts, for example, up to 48 volts. Accordingly, in some embodiments, the output voltage of a 12 volt lithium ion battery may be boosted using a DC-DC converter to supply power to the high voltage devices. Additionally or alternatively, a 48 volt lithium ion battery may be used to supplement a 12 volt lead-acid battery. More specifically, the 48 volt lithium ion battery may be used to more efficiently capture electrical energy generated during regenerative braking and subsequently supply electrical energy to power the high voltage devices.

Thus, the design choice regarding whether to utilize a 12 volt lithium ion battery or a 48 volt lithium ion battery may depend directly on the electrical devices included in a particular vehicle. Nevertheless, although the voltage characteristics may differ, the operational principles of a 12 volt lithium ion battery and a 48 volt lithium ion battery are generally similar. More specifically, as described above, both may be used to capture electrical energy during regenerative braking and subsequently supply electrical energy to power electrical devices in the vehicle.

Accordingly, to simplify the following discussion, the present techniques will be described in relation to a battery system with a 12 volt lithium ion battery and a 12 volt lead-acid battery. However, one of ordinary skill in art is able to adapt the present techniques to other battery systems, such as a battery system with a 48 volt lithium ion battery and a 12 volt lead-acid battery.

As generally set forth above, the present disclosure relates to limiting lithium plating at anodes of lithium ion batteries. For example, the present disclosure provides, among other things, certain systems and approaches for monitoring and mitigating such lithium plating, based on experimental observations. When a lithium ion battery charges, it may be advantageous to limit certain charge parameters to lessen the likelihood of lithium plating at the anodes of the lithium ion batteries. To reduce the likelihood of lithium plating while still maintaining an efficient charge rate, limits to various charge parameters may be dynamically altered to correspond to measured parameters (e.g., charge current, temperature, or state of charge of the lithium ion battery) presently experienced by the lithium ion battery, which may affect the lithium ion battery's propensity toward experiencing lithium plating.

With the preceding in mind, the present disclosure describes systems and methods for controlling charging operations of a battery system to prevent the lithium ion batteries from experiencing lithium plating on anodes of the lithium ion batteries. Traditionally, to combat lithium plating, lithium ion battery manufacturers have provided a current limit for charging operations of lithium ion batteries. However, these current limits are often overly conservative for the specific circumstances surrounding a lithium ion battery, which may result in inefficient charging operations by unnecessarily limiting charge current levels. In addition, such charge current limits are often established based on constant current charging. While constant current charging is useful in certain applications such as in EVs and PHEVs, other applications such as hybrid vehicles (e.g., mild hybrids, micro hybrids) may, in some instances, use pulse charging. Indeed, it is now recognized that pulsed charging currents may have different lithium plating dynamics than continuous charging currents. It is also now recognized that the current limits for such pulsed charging currents can more appropriately be determined using the systems and methods described herein, as opposed to basing the current limits on continuous charging current limits.

In accordance with the present disclosure, a battery management system may utilize an advanced method that prevents plating and estimates plating in a more accurate manner as compared with traditional methods. The battery management system of the present disclosure thereby maximizes the battery performance in service while preventing plating and related aging. As an example, it is now recognized that the “plating current,” or the current at which lithium plating at the anode occurs, is a strong function of both temperature and state of charge for pulsed charging regimes.

Various methods to construct one or more models used by the battery management system to quantify and prevent plating are also described herein. For example, the present disclosure provides an electrochemical model that explicitly accounts for the lithium plating reaction. The model enables both determination of plating onset and quantification of plated lithium. The battery management systems described herein may, for instance, measure operating parameters of the lithium ion batteries and, using such a model, control the charging operations to avoid operating parameter values of the lithium ion batteries that may result in an increased likelihood of lithium plating on the anodes based not only on instant values of the monitored parameters, but also based on quantified lithium plating, the state of the lithium ion battery based on historical usage, and so forth, generated by the model.

To help illustrate, FIG. 1 is a perspective view of an embodiment of a vehicle 10 , which may utilize a regenerative braking system. Although the following discussion is presented in relation to vehicles with regenerative braking systems, the techniques described herein are adaptable to other vehicles that capture/store electrical energy with a battery, which may include electric-powered and gas-powered vehicles.

As discussed above, it would be desirable for a battery system 12 to be largely compatible with traditional vehicle designs. Accordingly, the battery system 12 may be placed in a location in the vehicle 10 that would have housed a traditional battery system. For example, as illustrated, the vehicle 10 may include the battery system 12 positioned similarly to a lead-acid battery of a typical combustion-engine vehicle (e.g., under the hood of the vehicle 10 ). Furthermore, as will be described in more detail below, the battery system 12 may be positioned to facilitate managing temperature of the battery system 12 . For example, in some embodiments, positioning a battery system 12 under the hood of the vehicle 10 may enable an air duct to channel airflow over the battery system 12 and cool the battery system 12 . The battery system 12 may include or be associated with a battery management system that is programmed to perform monitoring, estimation, and control of the battery system 12 to limit lithium plating, as described in further detail below.

A more detailed view of the battery system 12 is described in FIG. 2 . As depicted, the battery system 12 includes an energy storage component 14 coupled to an ignition system 16 , an alternator 18 , a vehicle console 20 , and optionally to an electric motor 22 . Generally, the energy storage component 14 may capture/store electrical energy generated in the vehicle 10 and output electrical energy to power electrical devices in the vehicle 10 .

In other words, the battery system 12 may supply power to components of the vehicle's electrical system, which may include radiator cooling fans, climate control systems, electric power steering systems, active suspension systems, auto park systems, electric oil pumps, electric super/turbochargers, electric water pumps, heated windscreen/defrosters, window lift motors, vanity lights, tire pressure monitoring systems, sunroof motor controls, power seats, alarm systems, infotainment systems, navigation features, lane departure warning systems, electric parking brakes, external lights, or any combination thereof. Illustratively, in the depicted embodiment, the energy storage component 14 supplies power to the vehicle console 20 and the ignition system 16 , which may be used to start (e.g., crank) an internal combustion engine 24 .

Additionally, the energy storage component 14 may capture electrical energy generated by the alternator 18 and/or the electric motor 22 . In some embodiments, the alternator 18 may generate electrical energy while the internal combustion engine 24 is running. More specifically, the alternator 18 may convert the mechanical energy produced by the rotation of the internal combustion engine 24 into electrical energy. Additionally or alternatively, when the vehicle 10 includes an electric motor 22 , the electric motor 22 may generate electrical energy by converting mechanical energy produced by the movement of the vehicle 10 (e.g., rotation of the wheels) into electrical energy. Thus, in some embodiments, the energy storage component 14 may capture electrical energy generated by the alternator 18 and/or the electric motor 22 during regenerative braking. As such, the alternator 18 and/or the electric motor 22 are generally referred to herein as a regenerative braking system.

To facilitate capturing and supplying electric energy, the energy storage component 14 may be electrically coupled to the vehicle's electric system via a bus 26 . For example, the bus 26 may enable the energy storage component 14 to receive electrical energy generated by the alternator 18 and/or the electric motor 22 . Additionally, the bus 26 may enable the energy storage component 14 to output electrical energy to the ignition system 16 and/or the vehicle console 20 . Accordingly, when a 12 volt battery system 12 is used, the bus 26 may carry electrical power typically between 8-18 volts.

Additionally, as depicted, the energy storage component 14 may include multiple battery modules. For example, in the depicted embodiment, the energy storage component 14 includes a lead acid (e.g., a first) battery module 28 in accordance with present embodiments, and a lithium ion (e.g., a second) battery module 30 , where each battery module

28 , 30 includes one or more battery cells. In other embodiments, the energy storage component 14 may include any number of battery modules. Additionally, although the first battery module 28 and the second battery module 30 are depicted adjacent to one another, they may be positioned in different areas around the vehicle. For example, the second battery module 30 may be positioned in or about the interior of the vehicle 10 while the first battery module 28 may be positioned under the hood of the vehicle 10 .

In some embodiments, the energy storage component 14 may include multiple battery modules to utilize multiple different battery chemistries. For example, the first battery module 28 may utilize a lead-acid battery chemistry and the second battery module 30 may utilize a lithium ion battery chemistry. In such an embodiment, the performance of the battery system 12 may be improved since the lithium ion battery chemistry generally has a higher coulombic efficiency and/or a higher power charge acceptance rate (e.g., higher maximum charge current or charge voltage) than the lead-acid battery chemistry. As such, the capture, storage, and/or distribution efficiency of the battery system 12 may be improved.

To facilitate supply of power from the battery system 12 to the various components in the vehicle's electrical system (e.g., HVAC system and vehicle console 20 ), the energy storage component 14 (i.e., battery module) includes a first terminal 32 and a second terminal 34 . In some embodiments, the second terminal 34 may provide a ground connection and the first terminal 32 may provide a positive voltage ranging between 7-18 volts.

In still further embodiments, the energy storage component 14 may only include a single battery module, such as the lithium ion battery module 30 . In such embodiments, the lithium ion battery module 30 may have electrical characteristics that enable it to replace a traditional lead-acid battery. By way of example, the lithium ion battery module 30 may be a 12V starter battery.

As illustrated, the energy storage component may be associated with a battery management system (BMS) 36 . As used herein, the BMS 36 generally refers to control components that control operation of the battery system 12 , such as relays within the battery module or switches in the alternator 18 . Additionally, the BMS 36 may be disposed within the lithium ion battery module 30 (e.g., within a housing of the module), or the BMS 36 may be remote to the lithium ion battery module 30 , as depicted in FIG. 2 . As also shown in FIG. 2 , the operation of the lithium ion battery module 30 , and indeed the energy storage component 14 , may be controlled by the BMS 36 . For example, the BMS 36 may regulate an amount of electrical energy captured/supplied by each battery module 28 or 30 (e.g., to de-rate and re-rate the battery system 12 ), perform load balancing between the battery modules

28 , 30 , control charging and discharging of the battery modules 28 , 30 (e.g., via relays or DC/DC converters), determine a state of charge of each battery module

28 , 30 and/or the entire energy storage component 14 , activate an active cooling mechanism, activate a short circuit protection system, and the like.

Accordingly, the BMS 36 may include a memory 38 and a processor 40 programmed to execute control algorithms for performing such tasks. More specifically, the processor 40 may include one or more application specific integrated circuits (ASICs), one or more field programmable gate arrays (FPGAs), one or more general purpose processors, or any combination thereof. Additionally, the memory 38 may include volatile memory, such as random access memory (RAM), and/or non-volatile memory, such as read-only memory (ROM), optical drives, hard disc drives, or solid-state drives. In some embodiments, the BMS 36 may include portions of a vehicle control unit (VCU) and/or a separate battery control module. Additionally, as depicted, the BMS 36 may be included separate from the energy storage component 14 , such as a standalone module. In other embodiments, the BMS 36 may be included within the energy storage component 14 .

Additionally, as depicted in FIG. 2 , the lead- acid battery 28 and the lithium ion battery module 30 are connected in parallel across the first terminal 32 and the second terminal 34 to enable charging and discharging of the batteries. As described above, the battery terminals

32 and 34 may output the power stored in the energy storage component 14 to provide power to the vehicle's electrical system. Further, the battery terminals

32 and 34 may also input power to the energy storage component 14 to enable the lead- acid battery 28 and the lithium ion battery module 30 to charge, for example, when the alternator 18 generates electrical power through regenerative braking.

To provide more detail as to the charging process of the lithium ion battery module 30 , FIG. 3 illustrates a schematic view of components of the lithium ion battery module 30 . For simplicity, the lithium ion battery module 30 is depicted schematically to show the various internal components of a constituent battery cell contained within the lithium ion battery module 30 . In other words, the internals of the lithium ion battery module 30 shown in FIG. 3 are simplified to facilitate discussion. However, it should be appreciated that there are a number of additional components internal to the lithium ion battery module that are not specifically shown, such as a plurality of battery cells, bus bars used to connect the battery cells, and so forth.

Turning briefly to FIG. 4 , for instance, a cutaway view of a lithium ion battery cell 42 with a spiral wound cell structure is illustrated. Specifically, the battery cell 42 has a cell housing or cell casing 44 , which may take many forms but is illustrated as cylindrical. Other embodiments of the lithium ion battery cell 42 may have, for example, a prismatic shape or a pouch configuration for the cell casing 44 .

The lithium ion battery cell 42 also includes a <figure-callout id="46" label="first cell terminal" filenames="US20250192246A1-20250612-D00003.png" state="{

CLAIMS

Claims ( 20 )

1 . A battery system, comprising:

a lithium ion battery configured to couple to an electrical system; a battery management system electrically coupled to the lithium ion battery for a control of one or more recharge parameters of the lithium ion battery; and the battery management system programmed with an electrochemical model having an output for an adjustment of a plating current limit to prevent lithium plating on an anode of the lithium ion battery.

2 . The battery system of claim 1 , wherein the electrochemical model has a determination of at least one of a lithium plating reaction kinetics at the anode of the lithium ion battery and a quantity of plated lithium at the anode of the lithium ion battery, and an indication of a relationship between the one or more recharge parameters and the lithium plating reaction kinetics, the quantity of plated lithium, or a combination thereof, with the determination and the indication having one or more outputs for an adjustment of the plating current limit for charging operations of the lithium ion battery to prevent the lithium plating at the anode.

3 . The battery system of claim 1 , wherein the battery management system is configured to control charging current provided to the lithium ion battery as a function of the one or more outputs generated by the electrochemical model relating to the lithium plating at the anode.

4 . The battery system of claim 3 , wherein the battery management system is configured to control pulse duration and current level of the charging current as a function of a state of charge of the lithium ion battery according to plating current limits generated by the electrochemical model, with the battery system is configured to adjust the plating current limit.

5 . The battery system of claim 3 , wherein the battery management system is configured to control pulse duration and current level of the charging current as a function of a state of charge of the lithium ion battery and a temperature of the lithium ion battery according to plating current limits generated by the electrochemical model.

6 . The battery system of claim 2 , wherein the electrochemical model comprises equations describing the lithium plating reaction kinetics and quantifying plated lithium as a function of the lithium plating reaction kinetics.

7 . The battery system of claim 1 , wherein the electrochemical model comprises an equation that describes Butler-Volmer kinetics of a lithium plating reaction at the anode of the lithium ion battery.

8 . The battery system of claim 1 , wherein the electrochemical model comprises a second equation that calculates plated lithium as a result of a reaction occurring at the anode and side reactions involving plated lithium at the anode.

9 . The battery system of claim 8 , wherein with the battery management system is configured to use the electrochemical model to evaluate battery degradation due to the side reactions involving plated lithium at the anode.

10 . The battery system of claim 2 , wherein the adjustment is according to a current limit map generated by the electrochemical model, with the adjustment based on the electrochemical model and the one or more recharge parameters.

11 . The battery system of claim 10 , wherein the current limit map describes plating current limit as a function of a temperature and a state of charge of the lithium ion battery for a variety of charging current pulse durations.

12 . The battery system of claim 1 , wherein the lithium ion battery has a plurality of battery cells, at least one battery cell of the plurality of battery cells having a carbon-based anode active material.

13 . A method to control a charging of a lithium ion battery, comprising:

monitoring a parameter of the lithium ion battery during the charging by a battery management system coupled to the lithium ion battery; determining and finding a relationship between one or more of lithium plating reaction kinetics of the lithium ion battery using an electrochemical model and a quantity of plated lithium at an anode of the lithium ion battery; and controlling the charging of the lithium ion battery by the battery management system based on the relationship by adjusting a plating current limit according to a current limit map.

14 . The method of claim 13 , wherein the determination of the lithium plating reaction kinetics is at the anode, with the battery management system determining one or more of the lithium plating reaction kinetics using the electrochemical model and the quantity of plated lithium at an anode of the lithium ion battery; and

the finding of the relationship, by the battery management system, is between one or more of the parameter and the lithium plating reaction kinetics, the quantity of plated lithium, or a combination thereof using the electrochemical model.

15 . The method of claim 13 , comprising:

varying a state of charge of the lithium ion battery and performing electrochemical tests to determine overpotentials of cathode and an anode of the lithium ion battery and a plating current associated with lithium plating at the anode; calibrating the electrochemical model using results from the electrochemical tests to model a negative overpotential and a plating current limit as a function of a state of charge of the lithium ion battery; generating the current limit map to prevent lithium plating using the modeled plating current limit, wherein the current limit map describes the plating current limit as a function of a temperature and a state of charge of the lithium ion battery for a variety of charging current pulse durations; and the relationship is the current limit to be used for pulse charging of the lithium ion battery, the current limit being based on a correlation between monitored state of charge, monitored temperature, and a duration of charging current pulses defined by the current limit map.

16 . The method of claim 13 , wherein the electrochemical model comprises equations describing lithium plating reaction kinetics and quantifying plated lithium as a function of the lithium plating reaction kinetics.

17 . A lithium ion battery comprising:

a housing with a lithium ion battery cell and a battery management system; a sensor disposed in the housing and coupled to a battery management system to monitor a parameter of the lithium ion battery cell; the battery management system having an electrochemical model and configured to control a charging operation of the lithium ion battery; and the battery management system being configured to prevent lithium plating at an anode of the lithium ion battery according to a current limit map generated by the electrochemical model.

18 . The lithium ion battery of claim 17 , wherein the battery management system dynamically controls the charging operation of the lithium ion battery based on the monitored parameter and the electrochemical model to prevent lithium plating at the anode, which includes dynamically adjustment of a plating current limit for pulsed current charging operations of the lithium ion battery.

19 . The lithium ion battery of claim 17 , wherein, the electrochemical model comprises equations with the equations describing lithium plating reaction kinetics and quantifying the lithium plating as a function of the lithium plating reaction kinetics; and

the electrochemical model comprises an equation that describes Butler-Volmer kinetics of a lithium plating reaction at the anode of the lithium ion battery cell.

20 . The lithium ion battery of claim 17 , wherein the electrochemical model comprises an equation that calculates plated lithium as a result of a plating reaction occurring at the anode and side reactions involving plated lithium at the anode.

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