WO2024198565A1 - 储能电池包的温度管理方法及储能电池包的温度管理装置 - Google Patents

储能电池包的温度管理方法及储能电池包的温度管理装置 Download PDF

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Publication number
WO2024198565A1
WO2024198565A1 PCT/CN2023/141635 CN2023141635W WO2024198565A1 WO 2024198565 A1 WO2024198565 A1 WO 2024198565A1 CN 2023141635 W CN2023141635 W CN 2023141635W WO 2024198565 A1 WO2024198565 A1 WO 2024198565A1
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WIPO (PCT)
Prior art keywords
temperature
energy storage
storage battery
temperature value
phase change
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/CN2023/141635
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English (en)
French (fr)
Inventor
李全一
李佳
杨同欢
于泽群
王翱
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Viridi Energy Mobility Technology Ningbo Co Ltd
Zhejiang Geely Holding Group Co Ltd
Zhejiang Zeekr Intelligent Technology Co Ltd
Original Assignee
Viridi Energy Mobility Technology Ningbo Co Ltd
Zhejiang Geely Holding Group Co Ltd
Zhejiang Zeekr Intelligent Technology Co Ltd
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Application filed by Viridi Energy Mobility Technology Ningbo Co Ltd, Zhejiang Geely Holding Group Co Ltd, Zhejiang Zeekr Intelligent Technology Co Ltd filed Critical Viridi Energy Mobility Technology Ningbo Co Ltd
Publication of WO2024198565A1 publication Critical patent/WO2024198565A1/zh
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/63Control systems
    • H01M10/633Control systems characterised by algorithms, flow charts, software details or the like
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/48Accumulators combined with arrangements for measuring, testing or indicating the condition of cells, e.g. the level or density of the electrolyte
    • H01M10/486Accumulators combined with arrangements for measuring, testing or indicating the condition of cells, e.g. the level or density of the electrolyte for measuring temperature
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/61Types of temperature control
    • H01M10/613Cooling or keeping cold
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/61Types of temperature control
    • H01M10/615Heating or keeping warm
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/61Types of temperature control
    • H01M10/617Types of temperature control for achieving uniformity or desired distribution of temperature
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/62Heating or cooling; Temperature control specially adapted for specific applications
    • H01M10/625Vehicles
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/63Control systems
    • H01M10/635Control systems based on ambient temperature
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/64Heating or cooling; Temperature control characterised by the shape of the cells
    • H01M10/643Cylindrical cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/655Solid structures for heat exchange or heat conduction
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/655Solid structures for heat exchange or heat conduction
    • H01M10/6556Solid parts with flow channel passages or pipes for heat exchange
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/656Means for temperature control structurally associated with the cells characterised by the type of heat-exchange fluid
    • H01M10/6569Fluids undergoing a liquid-gas phase change or transition, e.g. evaporation or condensation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the present application relates to the field of batteries, and in particular to a temperature management method for an energy storage battery pack, a temperature management device for an energy storage battery pack, a computer-readable storage medium, and an electrical device.
  • the operating temperature of the energy storage battery has a great influence on its performance and life. If the operating temperature of the energy storage battery is too high, it will not only affect the service life of the energy storage battery, but also may cause dangerous situations such as combustion or explosion of the energy storage battery. If the operating temperature of the energy storage battery is too low, it will not only affect the capacity of the energy storage battery, but also may cause a short circuit.
  • the existing energy storage battery temperature management method mainly controls the temperature of the energy storage battery by liquid cooling or air cooling.
  • the temperature control uniformity of these two methods is poor, resulting in poor temperature uniformity of multiple single cells, which affects the working performance and service life of the energy storage battery pack.
  • the present application aims to solve one of the technical problems in the related art at least to some extent.
  • one purpose of the present application is to propose a temperature management method for an energy storage battery pack, which can control the temperature of the energy storage battery through a phase change medium, and can ensure that the temperatures of multiple single cells in the energy storage battery are consistent and/or can ensure that the temperatures of multiple battery modules in the energy storage battery are consistent, thereby facilitating improving the working performance of the energy storage battery and extending the service life of the energy storage battery.
  • the present application further proposes a temperature management device for an energy storage battery pack.
  • the present application further proposes a computer-readable storage medium.
  • the present application further proposes an electrical device.
  • the temperature management method of the energy storage battery pack includes: obtaining the temperature of the energy storage battery; determining the relationship between the temperature of the energy storage battery and a first preset temperature range; if the temperature of the energy storage battery is outside the first preset temperature range, determining the relationship between the temperature of the energy storage battery and a first temperature value and a second temperature value, wherein the The second temperature value is higher than the maximum temperature value of the first preset temperature interval, and the first temperature value is lower than the minimum temperature value of the first preset temperature interval; if the relationship is satisfied: the first temperature value ⁇ the temperature of the energy storage battery ⁇ the second temperature value, the temperature of the energy storage battery is adjusted by the phase change medium so that the temperature of the energy storage battery is within the first preset temperature zone.
  • the temperature of the energy storage battery can be controlled by a phase change medium.
  • the temperature control uniformity of the phase change medium is better, and the temperature of multiple single cells in the energy storage battery can be ensured to be consistent and/or the temperature of multiple battery modules in the energy storage battery can be ensured to be consistent, which is beneficial to improving the working performance of the energy storage battery and extending the service life of the energy storage battery.
  • the temperature management device of the energy storage battery pack includes: a temperature detection module, which is used to obtain the temperature of the energy storage battery; and a control module, which is used to determine the relationship between the temperature of the energy storage battery and a first preset temperature interval, and the relationship between the temperature of the energy storage battery and a first temperature value and a second temperature value.
  • the temperature of the energy storage battery is outside the first preset temperature interval and satisfies the relationship: the first temperature value ⁇ the temperature of the energy storage battery ⁇ the second temperature value, the temperature of the energy storage battery is adjusted by a phase change medium so that the temperature of the energy storage battery is within the first preset temperature zone; wherein the second temperature value is higher than the maximum temperature value of the first preset temperature interval, and the first temperature value is lower than the minimum temperature value of the first preset temperature interval.
  • the temperature of the energy storage battery can be controlled by a phase change medium.
  • the temperature control uniformity of the phase change medium is better, and the temperature of multiple single cells in the energy storage battery can be ensured to be consistent and/or the temperature of multiple battery modules in the energy storage battery can be ensured to be consistent, which is beneficial to improving the working performance of the energy storage battery and extending the service life of the energy storage battery.
  • a temperature management program for an energy storage battery pack is stored thereon, and when the temperature management program for the energy storage battery pack is executed by a processor, the temperature management method for the energy storage battery pack described above is implemented.
  • the temperature of the energy storage battery can be controlled by the phase change medium.
  • the temperature control uniformity of the phase change medium is better, and the temperature of multiple single cells in the energy storage battery can be ensured to be consistent and/or the temperature of multiple battery modules in the energy storage battery can be ensured to be consistent, which is beneficial to improving the working performance of the energy storage battery and extending the service life of the energy storage battery.
  • the electrical equipment includes a memory, a processor, and a temperature management program for an energy storage battery pack stored in the memory and executable on the processor.
  • the processor executes the temperature management program for the energy storage battery pack, the temperature management method for the energy storage battery pack is implemented.
  • the temperature of the energy storage battery can be controlled by the phase change medium.
  • the temperature control uniformity of the phase change medium is better, which can ensure that the temperatures of multiple single cells in the energy storage battery are consistent and/or the temperatures of multiple battery modules in the energy storage battery are consistent, thereby facilitating improving the working performance of the energy storage battery and extending the service life of the energy storage battery.
  • FIG1 is a flow chart of a temperature management method for an energy storage battery pack according to an embodiment of the present application
  • FIG2 is a flow chart of a specific embodiment of a temperature management method for an energy storage battery pack according to an embodiment of the present application
  • FIG3 is a block diagram of a temperature management device for an energy storage battery pack according to an embodiment of the present application.
  • FIG4 is a schematic diagram of an electrical device according to an embodiment of the present application.
  • FIG5 is a schematic diagram of an energy storage battery and a pipeline according to an embodiment of the present application.
  • FIG6 is a block diagram of a processor, a memory, a communication interface, and a communication bus according to an embodiment of the present application.
  • the reference numerals in the specification are as follows: Electrical equipment 100; Temperature management device 10; temperature detection module 11; control module 12; Heat exchanger 20; flow regulator 21; throttle valve 22; gas flow rate regulator 23; heater 24; WiFi module 25; Energy storage battery 30; single battery 31; Pipeline 40; Processor 1201 ; communication interface 1202 ; memory 1203 ; communication bus 1204 .
  • the temperature management method and the temperature management device 10 according to the embodiment of the present application are described below with reference to FIGS. 1 to 5 .
  • the temperature management device 10 includes: a temperature detection module 11 and a control module 12 .
  • the temperature detection module 11 is used to obtain the temperature of the energy storage battery 30, which means that the temperature detection module 11 can obtain the temperature of the energy storage battery 30; or that the temperature detection module 11 can obtain the temperature of the battery module in the energy storage battery 30; or that the temperature detection module 11 can obtain the temperature of the single battery 31 in the energy storage battery 30.
  • the energy storage battery 30 may include six battery modules, and the temperature detection module 11 can obtain the temperature of each of the six battery modules.
  • the energy storage battery 30 may include sixty single cells 31 , and the temperature detection module 11 may obtain the temperatures of the sixty single cells 31 .
  • the temperature of the energy storage battery 30 described herein may refer to the overall temperature of the energy storage battery 30 , the temperature of a battery module within the energy storage battery 30 , or the temperature of a single battery 31 within the energy storage battery 30 .
  • the temperature detection module 11 can transmit the acquired temperature of the energy storage battery 30 to the control module 12, and the control module 12 can determine the relationship between the received temperature of the energy storage battery 30 and the first preset temperature interval, and the control module 12 can also determine the relationship between the received temperature of the energy storage battery 30 and the first temperature value and the second temperature value.
  • the second temperature value is higher than the maximum temperature value of the first preset temperature interval
  • the first temperature value is lower than the minimum temperature value of the first preset temperature interval.
  • the temperature of the energy storage battery 30 satisfies the relationship: the first temperature value ⁇ the temperature of the energy storage battery 30 ⁇ the second temperature value (which can be understood as the first temperature value ⁇ the temperature of the energy storage battery 30 ⁇ the minimum temperature value of the first preset temperature range, or the maximum temperature value of the first preset temperature range ⁇ the temperature of the energy storage battery 30 ⁇ the second temperature value), the temperature of the energy storage battery 30 is adjusted by the phase change medium so that the temperature of the energy storage battery 30 is within the first preset temperature range.
  • the temperature detection module 11 can obtain the temperature of each of the sixty single cells 31 in the energy storage battery 30, and transmit the obtained temperature of each of the sixty single cells 31 to the control module 12.
  • the control module 12 can judge the temperature of each of the sixty single cells 31 respectively. If the temperature of one of the single cells 31 is outside the first preset temperature range and is greater than or equal to the first temperature value and less than the second temperature value, the temperature of the energy storage battery 30 is adjusted by the phase change medium.
  • the phase change medium can be arranged near the energy storage battery 30.
  • the first temperature value ⁇ the temperature of the energy storage battery 30 ⁇ the lowest temperature value of the first preset temperature range it means that the temperature of the energy storage battery 30 is relatively low at this time, and the phase change medium arranged near the energy storage battery 30 can release heat to increase the temperature of the energy storage battery 30.
  • the maximum temperature value of the first preset temperature range ⁇ the temperature of the energy storage battery 30 ⁇ the second temperature value it means that the temperature of the energy storage battery 30 is relatively high at this time, and the phase change medium arranged near the energy storage battery 30 can absorb heat to reduce the temperature of the energy storage battery 30. This process is also applicable to the battery module or the single battery 31, and will not be repeated here.
  • Phase change medium refers to a substance that can change its state and provide latent heat without changing the temperature.
  • the state of the phase change medium can change from solid to solid, solid to liquid, solid to gas, liquid to liquid, liquid to gas, etc.
  • the temperature control uniformity of the phase change medium is better.
  • the temperature detection module 11 is communicatively connected with the control module 12.
  • the temperature detection module 11 and the control module 12 may be integrated or separately arranged.
  • the temperature detection module 11 and/or the control module 12 may be integrated with a BMS (battery management system - BAERY MANAGEMEN SYSEM).
  • the temperature detection module 11 and/or the control module 12 may also be integrated with a vehicle controller. This application does not impose any restrictions on this.
  • the phase change medium arranged near the battery module or the single cell 31 can adjust the temperature of the battery module or the single cell 31 to achieve precise temperature control.
  • the temperature of the energy storage battery 30 can be controlled by the phase change medium.
  • the temperature control uniformity of the phase change medium is better, which can ensure that the temperatures of multiple single cells 31 in the energy storage battery 30 are consistent and/or the temperatures of multiple battery modules in the energy storage battery 30 are consistent, thereby facilitating improving the working performance of the energy storage battery 30 and extending the service life of the energy storage battery 30.
  • a heat conductive member is provided between the pipeline 40 and the energy storage battery 30.
  • the heat conductive member can be constructed as a heat conductive silicon wafer with high thermal conductivity.
  • Such a configuration can improve the heat exchange efficiency between the phase change medium and the energy storage battery 30, and is conducive to improving the temperature control uniformity of the phase change medium, which can further ensure the temperature consistency of the multiple single cells 31 in the energy storage battery 30 and/or can further ensure the temperature consistency of the multiple battery modules in the energy storage battery 30.
  • the present application after determining that the temperature of the energy storage battery 30 is outside the first preset temperature zone, it also includes: if the temperature of the energy storage battery 30 is ⁇ the second temperature value, controlling the phase change medium to circulate and pass through the heat exchanger 20 (as shown in Figure 4).
  • the material state change of the phase change medium is preferably liquid-liquid.
  • the control module 12 determines that the temperature of the energy storage battery 30 is ⁇ the second temperature value, the control module 12 can control the pump (or other device for driving the flow of liquid) to make the phase change medium in the pipeline 40 flow and pass through the heat exchanger 20. It can be understood that if the temperature of the energy storage battery 30 is ⁇ the second temperature value, it means that the temperature of the energy storage battery 30 is high at this time. If only the phase change medium located nearby It is difficult to lower the temperature to within the first preset temperature range.
  • the phase change medium in the pipeline 40 can adjust the area with higher temperature of the energy storage battery 30 to quickly lower the temperature of the energy storage battery 30 to within the first preset temperature range, and it is beneficial to ensure that the temperature of multiple single cells 31 in the energy storage battery 30 is consistent and/or it is beneficial to ensure that the temperature of multiple battery modules in the energy storage battery 30 is consistent.
  • phase change medium in the pipe 40 can flow through the heat exchanger 20, and the phase change medium can quickly dissipate heat in the heat exchanger 20.
  • This arrangement can make the phase change medium flowing out of the heat exchanger 20 in a form that can absorb more heat, which is beneficial to improving the cooling rate of the temperature management device 10.
  • the phase change medium in the sub-pipe corresponding to the battery module can be controlled to flow and flow through the heat exchanger 20. This setting can achieve precise temperature control of the energy storage battery 30.
  • the difference between the temperature of the energy storage battery 30 and the second temperature value is calculated, and the flow rate of the phase change medium is adjusted according to the difference between the temperature of the energy storage battery 30 and the second temperature value.
  • the difference between the temperature of the energy storage battery 30 and the second temperature value is proportional to the flow rate of the phase change medium. That is, if the difference between the temperature of the energy storage battery 30 and the second temperature value is larger, it means that the temperature of the energy storage battery 30 is higher.
  • the temperature control rate of the temperature management device 10 can be improved.
  • the flow rate of the phase change medium can be adjusted by providing a flow regulator 21 and/or a throttle valve 22 in the pipeline 40.
  • each sub-pipeline can be provided with a flow regulator 21, so that the flow rate of the sub-pipeline can be controlled separately.
  • the flow of the phase change medium in all the pipes 40 can be controlled (including controlling the flow rate); when the temperature of the energy storage battery 30 refers to the temperature of a certain battery module in the energy storage battery 30, or refers to the temperature of a certain single cell 31 in the energy storage battery 30, the flow of the phase change medium in the sub-pipeline corresponding to the battery module or single cell 31 with abnormal temperature can be controlled (including controlling the flow rate).
  • the method includes: determining the relationship between the temperature of the energy storage battery 30 and a fourth temperature value, wherein the fourth temperature value is higher than the second temperature value; if the temperature of the energy storage battery 30 is ⁇ the fourth temperature value, the gas flow rate regulator 23 is controlled to operate to increase the air flow rate around the heat exchanger 20 and/or increase the air flow rate around the phase change medium.
  • the gas flow rate regulator 23 can be configured as a heat dissipation fan, and the gas flow rate regulator 23 can be arranged near the heat exchanger 20, or the gas flow rate regulator 23 can be arranged near the pipeline 40, or the gas flow rate regulator 23 can be arranged near the heat exchanger 20 and the pipeline 40.
  • the heat of the phase change medium in the pipeline 40 and/or the heat exchanger 20 can be quickly dissipated, thereby further improving the cooling rate of the temperature management device 10.
  • the difference between the temperature of the energy storage battery 30 and the fourth temperature value may be calculated.
  • the working condition of the gas flow rate regulator 23 (for example, the gear position of the cooling fan) is controlled according to the difference between the temperature of the energy storage battery 30 and the fourth temperature value. Specifically, if the difference between the temperature of the energy storage battery 30 and the fourth temperature value is larger, it means that the temperature of the energy storage battery 30 is higher, and the temperature control rate of the temperature management device 10 can be increased by increasing the rotation speed of the cooling fan.
  • the method further includes: if the temperature of the energy storage battery 30 is less than the first temperature value, controlling the phase change medium to circulate.
  • the material state change of the phase change medium is preferably liquid-liquid.
  • the control module 12 determines that the temperature of the energy storage battery 30 is less than the first temperature value, the control module 12 can control the pump (or other devices for driving liquid flow) to make the phase change medium located in the pipeline 40 flow. It can be understood that if the temperature of the energy storage battery 30 is less than the first temperature value, it means that the temperature of the energy storage battery 30 is relatively low at this time. If only the phase change medium located nearby is used, it is difficult to increase the temperature to the first preset temperature range.
  • the phase change medium in the pipeline 40 can adjust the area with lower temperature in the energy storage battery 30 to quickly increase the temperature of the energy storage battery 30 to the first preset temperature range, and it is beneficial to ensure that the temperatures of multiple single cells 31 in the energy storage battery 30 are consistent and/or it is beneficial to ensure that the temperatures of multiple battery modules in the energy storage battery 30 are consistent.
  • the flow of the phase change medium in the sub-pipe corresponding to the battery module can be controlled. Such a setting can achieve precise temperature control of the energy storage battery 30.
  • the difference between the temperature of the energy storage battery 30 and the first temperature value is calculated, and the flow rate of the phase change medium is adjusted according to the difference between the temperature of the energy storage battery 30 and the first temperature value.
  • the difference between the temperature of the energy storage battery 30 and the first temperature value is proportional to the flow rate of the phase change medium. That is, if the difference between the temperature of the energy storage battery 30 and the first temperature value is larger, it means that the temperature of the energy storage battery 30 is lower.
  • the temperature control rate of the temperature management device 10 can be improved.
  • the flow rate of the phase change medium can be adjusted by providing a flow regulator 21 and/or a throttle valve 22 in the pipeline 40.
  • a flow regulator 21 can be provided on each sub-pipeline, so that the flow rate of the sub-pipeline can be controlled separately.
  • the flow of the phase change medium in all the pipes 40 can be controlled (including controlling the flow rate); when the temperature of the energy storage battery 30 refers to the temperature of a certain battery module in the energy storage battery 30, or refers to the temperature of a certain single cell 31 in the energy storage battery 30, the flow of the phase change medium in the sub-pipeline corresponding to the battery module or single cell 31 with abnormal temperature can be controlled (including controlling the flow rate).
  • the method includes: determining the relationship between the temperature of the energy storage battery 30 and a third temperature value, wherein the third temperature value is lower than the first temperature value; if the temperature of the energy storage battery 30 is less than the third temperature value, controlling the heater 24 to operate to heat the phase change medium surrounding it.
  • the heater 24 may be constructed as a PTC heater (Positive Temperature Coefficient-heater).
  • the heater 24 may be disposed near the pipe 40 .
  • the phase change medium located near the heater 24 can be heated, and the heat of the phase change medium in the pipe 40 can be quickly increased, so that the heating rate of the temperature management device 10 can be further increased.
  • the difference between the temperature of the energy storage battery 30 and the third temperature value may be calculated, and the working condition of the heater 24 (for example, the gear of the heater 24) may be controlled according to the difference between the temperature of the energy storage battery 30 and the third temperature value. Specifically, if the difference between the temperature of the energy storage battery 30 and the third temperature value is larger, it means that the temperature of the energy storage battery 30 is lower, and by increasing the heat generation of the heater 24, the temperature control rate of the temperature management device 10 can be improved.
  • the temperature control of the energy storage battery 30 can be achieved by controlling the flow of the phase change medium in the pipeline 40, the flow rate of the phase change medium, the gas flow rate regulator 23 and the heater 24. At this time, only one heat exchanger 20, one gas flow rate regulator 23, one flow regulator 21 and one heater 24 are required.
  • the pipeline 40 can be divided into multiple sub-pipelines, the number of the multiple sub-pipelines can be the same as the number of battery modules in the energy storage battery 30, and the multiple sub-pipelines can be respectively set to correspond to the multiple battery modules (or the number of sub-pipelines is less than the number of battery modules, and one sub-pipeline corresponds to multiple battery modules; or the number of sub-pipelines is higher than the number of battery modules, and multiple sub-pipelines correspond to one battery module).
  • Each sub-pipeline may be provided with a heat exchanger 20, a gas flow rate regulator 23, a flow rate regulator 21 and a heater 24.
  • the pipeline 40 may also include a main pipeline connected to a plurality of sub-pipelines, the heat exchanger 20, the gas flow rate regulator 23 and the heater 24 may be provided in the main pipeline, and a throttle valve 22 may be provided on the main pipeline to assist in controlling the flow rate of the phase change medium.
  • the temperature management device 10 may also obtain the external environment temperature and the working condition of the electrical device 100, and adjust the first temperature value and/or the second temperature value and/or the third temperature value and/or the fourth temperature value according to the external environment temperature and the working condition of the electrical device 100;
  • the first temperature value and/or the second temperature value and/or the third temperature value and/or the fourth temperature value are adjusted through the cloud server.
  • the first temperature value, the second temperature value, the third temperature value and the fourth temperature value are not a constant value. Due to the characteristics of the phase change medium, the heat absorption and heat release capacity of the phase change medium has a certain relationship with the external ambient temperature, and the operating conditions of the electrical equipment 100 also have certain requirements for the temperature control of the energy storage battery 30.
  • the control module 12 can The working condition of the device 100 appropriately lowers the second temperature value and the fourth temperature value so as to quickly trigger the flow of the phase change medium and the operation of the gas flow rate regulator 23 .
  • control module 12 can appropriately increase the first temperature value and the third temperature value according to the outside ambient temperature so as to quickly trigger the flow of the phase change medium and the operation of the heater 24.
  • Such a setting can adjust the first temperature value and/or the second temperature value and/or the third temperature value and/or the fourth temperature value according to the external environment temperature and the working condition of the electrical equipment 100, so that the temperature management device 10 can reliably adjust the temperature of the energy storage battery 30.
  • the cloud server can remotely obtain the working condition of the power device 100 and the ambient temperature of the location of the power device 100, and adjust the first temperature value and/or the second temperature value and/or the third temperature value and/or the fourth temperature value according to the working condition of the power device 100 and the ambient temperature of the location of the power device 100.
  • the cloud server can be remotely controlled, so that the temperature of the energy storage battery 30 can be adjusted more reliably.
  • the temperature management device 10 may further include: a WiFi module 25 , which may be used to communicate with a cloud server.
  • FIG. 1 is a flow chart of a temperature management method according to an embodiment of the present application.
  • the temperature management device of the above embodiment can implement the temperature management method. As shown in FIG. 1 , the temperature management method includes the following steps:
  • the temperature detection module is used to obtain the temperature of the energy storage battery. It should be noted that the energy storage battery described in this application refers to the entire battery in the energy storage battery pack. In other words, the energy storage battery described in this application is a general term for all batteries in the energy storage battery pack.
  • the temperature detection module is used to obtain the temperature of the energy storage battery, which means that the temperature detection module can obtain the temperature of the energy storage battery; or that the temperature detection module can obtain the temperature of the battery module in the energy storage battery; or that the temperature detection module can obtain the temperature of the single battery in the energy storage battery.
  • the energy storage battery may include six battery modules, and the temperature detection module can obtain the temperature of each of the six battery modules.
  • the energy storage battery may include sixty single batteries, and the temperature detection module can obtain the temperature of each of the sixty single batteries.
  • the temperature of the energy storage battery described in this article may refer to the overall temperature of the energy storage battery, the temperature of a certain battery module in the energy storage battery, or the temperature of a certain single cell in the energy storage battery.
  • the temperature detection module can transmit the acquired temperature of the energy storage battery to the control module, and the control module can determine the relationship between the received temperature of the energy storage battery and the first preset temperature range.
  • the control module can determine the relationship between the received temperature of the energy storage battery and the first temperature value and the second temperature value.
  • the relationship between the temperature of the energy storage battery and the first temperature value and the second temperature value is determined.
  • the temperature of the energy storage battery satisfies the relationship: the first temperature value ⁇ the temperature of the energy storage battery ⁇ the second temperature value (this can be understood as the first temperature value ⁇ the temperature of the energy storage battery ⁇ the minimum temperature value of the first preset temperature range, or the maximum temperature value of the first preset temperature range ⁇ the temperature of the energy storage battery ⁇ the second temperature value), the temperature of the energy storage battery is adjusted by the phase change medium so that the temperature of the energy storage battery is within the first preset temperature range.
  • the temperature detection module can obtain the temperature of each of the sixty single cells in the energy storage battery, and transmit the obtained temperature of each of the sixty single cells to the control module.
  • the control module can judge the temperature of each of the sixty single cells separately. If the temperature of one of the single cells is outside the first preset temperature range and is greater than or equal to the first temperature value and less than the second temperature value, the temperature of the energy storage battery is adjusted by the phase change medium.
  • the phase change medium can be set near the energy storage battery.
  • the temperature of the energy storage battery is outside the first preset temperature range and satisfies the relationship: the first temperature value ⁇ the temperature of the energy storage battery ⁇ the lowest temperature value of the first preset temperature range, it means that the temperature of the energy storage battery is low at this time, and the phase change medium set near the energy storage battery can release heat to increase the temperature of the energy storage battery.
  • the maximum temperature value of the first preset temperature range ⁇ the temperature of the energy storage battery ⁇ the second temperature value it means that the temperature of the energy storage battery is high at this time, and the phase change medium set near the energy storage battery can absorb heat to reduce the temperature of the energy storage battery. This process is also applicable to battery modules or single cells, and will not be repeated here.
  • Phase change medium refers to a substance that can change its material state and provide latent heat without changing the temperature.
  • the material state change of the phase change medium can be solid-solid, solid-liquid, solid-gas, liquid-liquid, liquid-gas, etc.
  • the temperature control uniformity of the phase change medium is better.
  • the temperature detection module is communicatively connected with the control module.
  • the temperature detection module and the control module can be integrated or separately arranged.
  • the temperature detection module and/or the control module can be integrated with a BMS (battery management system - BAERY MANAGEMEN SYSEM).
  • the temperature detection module and/or the control module can also be integrated with a vehicle controller. This application does not impose any restrictions on this.
  • the temperature detection module when used to obtain the temperature of the energy storage battery, it refers to obtaining the temperature of the battery module in the energy storage battery, or it refers to obtaining the temperature of the single battery in the energy storage battery.
  • the phase change medium near the cell can adjust the temperature of the battery module or the temperature of the single cell to achieve precise temperature control.
  • the temperature of the energy storage battery can be controlled by the phase change medium, and the temperature control uniformity of the phase change medium is better, which can ensure that the temperatures of multiple single cells in the energy storage battery are consistent and/or the temperatures of multiple battery modules in the energy storage battery are consistent, thereby facilitating improving the working performance of the energy storage battery and extending the service life of the energy storage battery.
  • the phase change medium is located in a pipe, and the pipe is arranged around the energy storage battery.
  • the pipe can be divided into a plurality of sub-pipes, and the number of the plurality of sub-pipes can be the same as the number of battery modules in the energy storage battery, and the plurality of sub-pipes can be respectively arranged corresponding to the plurality of battery modules, so that when the temperature of a certain battery module (or the temperature of a certain single battery) is outside the first preset temperature range, the temperature of the battery module (or single battery) can be controlled by the phase change medium in the sub-pipe arranged corresponding to the battery module (or single battery), which is conducive to improving the accuracy of temperature control.
  • a heat conductor is provided between the pipeline and the energy storage battery.
  • the heat conductor can be constructed as a heat-conducting silicon wafer with high thermal conductivity. Such an arrangement can improve the heat exchange efficiency between the phase change medium and the energy storage battery, and is conducive to improving the temperature control uniformity of the phase change medium, which can further ensure that the temperature of multiple single cells in the energy storage battery is consistent and/or can further ensure that the temperature of multiple battery modules in the energy storage battery is consistent.
  • the present application after determining that the temperature of the energy storage battery is outside the first preset temperature zone, it also includes: if the temperature of the energy storage battery is ⁇ the second temperature value, controlling the phase change medium to circulate and pass through the heat exchanger.
  • the material state change of the phase change medium is preferably liquid-liquid.
  • the control module determines that the temperature of the energy storage battery is ⁇ the second temperature value, the control module can control the pump (or other device for driving the liquid to flow) to make the phase change medium located in the pipeline flow and pass through the heat exchanger. It can be understood that if the temperature of the energy storage battery is ⁇ the second temperature value, it means that the temperature of the energy storage battery is relatively high at this time. If only the phase change medium located nearby is used, it is difficult to lower the temperature to the first preset temperature range.
  • the phase change medium in the pipeline can adjust the area with a higher temperature of the energy storage battery to quickly lower the temperature of the energy storage battery to the first preset temperature range, and it is beneficial to ensure that the temperatures of multiple single cells in the energy storage battery are consistent and/or it is beneficial to ensure that the temperatures of multiple battery modules in the energy storage battery are consistent.
  • phase change medium in the pipeline can flow through the heat exchanger, and the phase change medium can quickly dissipate heat in the heat exchanger.
  • This arrangement can make the phase change medium flowing out of the heat exchanger in a form that can absorb more heat, which is conducive to increasing the cooling rate.
  • the phase change medium in the sub-pipe corresponding to the battery module can be controlled to flow and flow through the heat exchanger. This setting can achieve precise temperature control of the energy storage battery.
  • the difference between the temperature of the energy storage battery and the second temperature value is calculated, and the flow rate of the phase change medium is adjusted according to the difference between the temperature of the energy storage battery and the second temperature value.
  • the difference between the temperature of the energy storage battery and the second temperature value is proportional to the flow rate of the phase change medium. That is, if the difference between the temperature of the energy storage battery and the second temperature value is larger, it means that the temperature of the energy storage battery is higher.
  • the temperature control rate can be improved.
  • the flow rate of the phase change medium can be adjusted by providing a flow regulator and/or a throttle valve in the pipeline.
  • each sub-pipeline can be provided with a flow regulator, so that the flow rate of the sub-pipeline can be controlled individually.
  • the flow of phase change medium in all pipelines can be controlled (including controlling the flow rate); when the temperature of the energy storage battery refers to the temperature of a certain battery module in the energy storage battery, or refers to the temperature of a certain single cell in the energy storage battery, the flow of phase change medium in the sub-pipeline corresponding to the battery module or single cell with abnormal temperature can be controlled (including controlling the flow rate).
  • the method includes: determining the relationship between the temperature of the energy storage battery and a fourth temperature value, wherein the fourth temperature value is higher than the second temperature value; if the temperature of the energy storage battery is ⁇ the fourth temperature value, the gas flow rate regulator is controlled to operate to increase the air flow rate around the heat exchanger and/or increase the air flow rate around the phase change medium.
  • the gas flow rate regulator can be configured as a heat dissipation fan, and the gas flow rate regulator can be arranged near the heat exchanger, or the gas flow rate regulator can be arranged near the pipeline, or the gas flow rate regulator can be arranged near the heat exchanger and the pipeline.
  • the difference between the temperature of the energy storage battery and the fourth temperature value may be calculated, and the working condition of the gas flow rate regulator (for example, the gear position of the heat dissipation fan) may be controlled according to the difference between the temperature of the energy storage battery and the fourth temperature value. Specifically, if the difference between the temperature of the energy storage battery and the fourth temperature value is larger, it means that the temperature of the energy storage battery is higher, and the temperature control rate can be increased by increasing the rotation speed of the heat dissipation fan.
  • the working condition of the gas flow rate regulator for example, the gear position of the heat dissipation fan
  • the method further includes: if the temperature of the energy storage battery is less than the first temperature value, controlling the phase change medium to circulate.
  • the material state change of the phase change medium is preferably liquid-liquid.
  • the control module determines that the temperature of the energy storage battery is less than the first temperature value, the control module can control the pump (or other device for driving liquid flow) to make the phase change medium in the pipeline flow. It can be understood that if the temperature of the energy storage battery is less than the first temperature value, it means that the temperature of the energy storage battery is relatively low at this time. If only the phase change medium located nearby is used, it is difficult to increase the temperature to the first preset temperature range.
  • the phase change medium in the pipeline can adjust the area with lower temperature in the energy storage battery to quickly increase the temperature of the energy storage battery to the first preset temperature range, and it is beneficial to ensure that the temperature of multiple single cells in the energy storage battery is consistent and/or it is beneficial to ensure the temperature of multiple battery modules in the energy storage battery. Consistent.
  • the flow of the phase change medium in the sub-pipe corresponding to the battery module can be controlled. Such a setting can achieve precise temperature control of the energy storage battery.
  • the difference between the temperature of the energy storage battery and the first temperature value is calculated, and the flow rate of the phase change medium is adjusted according to the difference between the temperature of the energy storage battery and the first temperature value.
  • the difference between the temperature of the energy storage battery and the first temperature value is proportional to the flow rate of the phase change medium. That is, if the difference between the temperature of the energy storage battery and the first temperature value is larger, it means that the temperature of the energy storage battery is lower, and by increasing the flow rate of the phase change medium, the temperature control rate can be improved.
  • the flow rate of the phase change medium can be adjusted by providing a flow regulator and/or a throttle valve in the pipeline.
  • each sub-pipeline can be provided with a flow regulator, so that the flow rate of the sub-pipeline can be controlled individually.
  • the flow of phase change medium in all pipelines can be controlled (including controlling the flow rate); when the temperature of the energy storage battery refers to the temperature of a certain battery module in the energy storage battery, or refers to the temperature of a certain single cell in the energy storage battery, the flow of phase change medium in the sub-pipeline corresponding to the battery module or single cell with abnormal temperature can be controlled (including controlling the flow rate).
  • the method includes: determining the relationship between the temperature of the energy storage battery and a third temperature value, wherein the third temperature value is lower than the first temperature value; if the temperature of the energy storage battery is less than the third temperature value, controlling the heater to operate to heat the phase change medium surrounding it.
  • the heater can be constructed as a PTC heating element (Positive Temperature Coefficient-heater).
  • the heater can be set near the pipeline. By controlling the operation of the heater, the phase change medium near the heater can be heated, and the heat of the phase change medium in the pipeline can be quickly increased, thereby further improving the heating rate.
  • the difference between the temperature of the energy storage battery and the third temperature value may be calculated, and the working condition of the heater (e.g., the gear position of the heater) may be controlled according to the difference between the temperature of the energy storage battery and the third temperature value. Specifically, if the difference between the temperature of the energy storage battery and the third temperature value is larger, it means that the temperature of the energy storage battery is lower, and the temperature control rate can be improved by increasing the heat generation of the heater.
  • the temperature control of the energy storage battery can be achieved by controlling the flow of the phase change medium in the pipeline, the flow rate of the phase change medium, the gas flow rate regulator and the heater. At this time, only a heat exchanger, a gas flow rate regulator, a flow regulator and a heater are needed.
  • the pipeline can be divided into multiple sub-pipelines, the number of the multiple sub-pipelines can be the same as the number of battery modules in the energy storage battery, and the multiple sub-pipelines can be respectively set corresponding to the multiple battery modules (or the number of sub-pipelines is less than the number of battery modules, and one sub-pipeline corresponds to multiple battery modules; or the number of sub-pipelines is higher than the number of battery modules).
  • the number of groups, multiple sub-pipelines correspond to one battery module).
  • Each sub-pipeline may be provided with a heat exchanger, a gas flow rate regulator, a flow rate regulator and a heater.
  • the pipeline may also include a main pipeline connected to a plurality of sub-pipelines, the heat exchanger, the gas flow rate regulator and the heater may be provided in the main pipeline, and a throttle valve may be provided on the main pipeline to assist in controlling the flow rate of the phase change medium.
  • the temperature management method of the energy storage battery pack further includes: obtaining the external environment temperature and the operating condition of the electrical equipment, and adjusting the first temperature value and/or the second temperature value and/or the third temperature value and/or the fourth temperature value according to the external environment temperature and the operating condition of the electrical equipment;
  • the first temperature value and/or the second temperature value and/or the third temperature value and/or the fourth temperature value are adjusted through the cloud server.
  • the first temperature value, the second temperature value, the third temperature value and the fourth temperature value are not a fixed value. Due to the characteristics of the phase change medium, the heat absorption and heat release capacity of the phase change medium has a certain relationship with the external ambient temperature, and the operating conditions of the electrical equipment also have certain requirements for the temperature control of the energy storage battery.
  • control module can appropriately lower the second temperature value and the fourth temperature value according to the working conditions of the electrical equipment to quickly trigger the flow of the phase change medium and the operation of the gas flow rate regulator.
  • the control module can appropriately increase the first temperature value and the third temperature value according to the outside ambient temperature so as to quickly trigger the flow of the phase change medium and the operation of the heater.
  • Such a setting can adjust the first temperature value and/or the second temperature value and/or the third temperature value and/or the fourth temperature value according to the external environment temperature and the working condition of the electrical equipment, so as to reliably adjust the temperature of the energy storage battery.
  • the cloud server can remotely obtain the working condition of the power consumption equipment and the ambient temperature of the place where the power consumption equipment is located, and adjust the first temperature value and/or the second temperature value and/or the third temperature value and/or the fourth temperature value according to the working condition of the power consumption equipment and the ambient temperature of the place where the power consumption equipment is located.
  • remote control can be performed through the cloud server, so that the temperature of the energy storage battery can be adjusted more reliably.
  • the temperature management method may include the following steps:
  • step S02 if the judgment is yes, then the process proceeds to step S03, and if the judgment is no, then the process returns to step S01.
  • step S03 if the judgment is yes, then the process proceeds to step S04, and if the judgment is no, then the process returns to step S01.
  • step S05 if the judgment is yes, then the process proceeds to step S06, and if the judgment is no, then the process returns to step S03.
  • step S07 if the judgment is yes, then the process proceeds to step S08, and if the judgment is no, then the process returns to step S05.
  • step S09 if the judgment is yes, then the process proceeds to step S10, and if the judgment is no, then the process returns to step S03.
  • step S11 if the judgment is yes, then the process proceeds to step S12, and if the judgment is no, then the process returns to step S09.
  • the present application proposes a computer-readable storage medium on which a temperature management program for an energy storage battery pack is stored.
  • the temperature management program is executed by a processor, the temperature management method of the above embodiments can be implemented.
  • the temperature of the energy storage battery can be controlled by the phase change medium.
  • the temperature control uniformity of the phase change medium is better, and the temperature of multiple single cells in the energy storage battery can be ensured to be consistent and/or the temperature of multiple battery modules in the energy storage battery can be ensured to be consistent, which is beneficial to improving the working performance of the energy storage battery and extending the service life of the energy storage battery.
  • the present application also proposes an electrical device, which includes a memory, a processor, and a temperature management program for an energy storage battery pack stored in the memory and executable on the processor.
  • the processor executes the temperature management program, the temperature management method of the above embodiments can be implemented.
  • the processor executes the temperature management program of the energy storage battery pack stored in the memory, and the temperature of the energy storage battery can be controlled through the phase change medium.
  • the temperature control uniformity of the phase change medium is better, and the temperature of multiple single cells in the energy storage battery can be ensured to be consistent and/or the temperature of multiple battery modules in the energy storage battery can be ensured to be consistent, which is beneficial to improving the working performance of the energy storage battery and extending the service life of the energy storage battery.
  • the electric device may include at least one processor 1201, at least one communication interface 1202, at least one memory 1203, and at least one communication bus 1204.
  • the number of the processor 1201, the communication interface 1202, the memory 1203, and the communication bus 1204 is at least one, and the processor 1201, the communication interface 1202, and the memory 1203 communicate with each other through the communication bus 1204.
  • the memory 1203 may be, but is not limited to, a random access memory (RAM), a read-only memory (ROM), a programmable read-only memory (PROM), an erasable programmable read-only memory (EPROM), an electrically erasable read-only memory (EEPROM), etc.
  • RAM random access memory
  • ROM read-only memory
  • PROM programmable read-only memory
  • EPROM erasable programmable read-only memory
  • EEPROM electrically erasable read-only memory
  • Processor 1201 may be an integrated circuit chip with signal processing capabilities.
  • the above-mentioned processor may be a general-purpose processor, including a central processing unit (CPU), a network processor (NP), etc.; it may also be a digital signal processor (DSP), an application-specific integrated circuit (ASIC), a field programmable gate array (FPGA) or other programmable logic devices, discrete gates or transistor logic devices, discrete hardware components.
  • DSP digital signal processor
  • ASIC application-specific integrated circuit
  • FPGA field programmable gate array
  • the various methods, steps and logic block diagrams disclosed in the embodiments of the present application can be implemented or executed.
  • the general-purpose processor may be a microprocessor or the processor may also be any conventional processor, etc.
  • computer-readable media include the following: an electrical connection portion with one or more wirings (electronic device), a portable computer disk box (magnetic device), a random access memory (RAM), a read-only memory (ROM), an erasable and programmable read-only memory (EPROM or flash memory), an optical fiber device, and a portable compact disk read-only memory (CDROM).
  • the computer-readable medium may even be paper or other suitable medium on which the program is printed, since the program may be obtained electronically, for example, by optically scanning the paper or other medium and then editing, interpreting or processing in other suitable ways if necessary, and then stored in a computer memory.
  • first feature or “second feature” may include one or more of the features.
  • a first feature being “on” or “under” a second feature may include that the first and second features are directly in contact with each other, or may include that the first and second features are not in direct contact with each other but are in contact with each other via another feature therebetween.
  • first feature to a second feature includes the first feature being directly above and obliquely above the second feature, or simply means that the first feature is horizontally higher than the second feature.

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Abstract

一种储能电池包的温度管理方法及储能电池包的温度管理装置,储能电池包的温度管理方法包括:获取储能电池的温度;判断储能电池的温度与第一预设温度区间的关系;若储能电池的温度处于第一预设温度区间外,则判断储能电池的温度与第一温度值、第二温度值的关系;若满足关系式:第一温度值≤储能电池的温度<第二温度值,通过相变介质调节储能电池的温度以使储能电池的温度处于第一预设温度区内。

Description

储能电池包的温度管理方法及储能电池包的温度管理装置
相关申请的交叉引用
本申请基于申请号为202310349926.0、申请日为2023年03月29日的中国专利申请提出,并要求上述中国专利申请的优先权,上述中国专利申请的全部内容在此引入本申请作为参考。
技术领域
本申请涉及电池领域,尤其是涉及一种储能电池包的温度管理方法、储能电池包的温度管理装置、计算机可读存储介质以及用电设备。
背景技术
相关技术中,储能电池的工作温度对其性能和寿命具有很大影响,若储能电池的工作温度过高,不仅会影响储能电池的使用寿命,还有可能发生储能电池燃烧或者爆炸等危险情况,若储能电池的工作温度过低,不仅会影响储能电池的电容量,还有可能发生短路的情况。
现有的储能电池温度管理方法,主要通过液冷或者风冷的方式对储能电池进行控温,然而,这两种方式的控温均匀程度较差,导致多个单体电池的温度均匀性较差,影响储能电池包的工作性能和使用寿命。
申请内容
本申请旨在至少在一定程度上解决相关技术中的技术问题之一。
为此,本申请的一个目的在于提出一种储能电池包的温度管理方法,该储能电池包的温度管理方法能够通过相变介质对储能电池进行控温,能够保证储能电池中的多个单体电池的温度一致和/或能够保证储能电池中的多个电池模组的温度一致,从而有利于提高储能电池的工作性能,有利于延长储能电池的使用寿命。
本申请进一步地提出了一种储能电池包的温度管理装置。
本申请进一步地提出了一种计算机可读存储介质。
本申请进一步地提出了一种用电设备。
根据本申请的储能电池包的温度管理方法,包括:获取储能电池的温度;判断所述储能电池的温度与第一预设温度区间的关系;若所述储能电池的温度处于所述第一预设温度区间外,则判断所述储能电池的温度与第一温度值、第二温度值的关系,其中,所 述第二温度值高于所述第一预设温度区间的最大温度值,所述第一温度值低于所述第一预设温度区间的最低温度值;若满足关系式:所述第一温度值≤所述储能电池的温度<所述第二温度值,通过相变介质调节所述储能电池的温度以使所述储能电池的温度处于所述第一预设温度区内。
据本申请的储能电池包的温度管理方法,能够通过相变介质对储能电池进行控温,相变介质的控温均匀程度较佳,能够保证储能电池中的多个单体电池的温度一致和/或能够保证储能电池中的多个电池模组的温度一致,从而有利于提高储能电池的工作性能,有利于延长储能电池的使用寿命。
根据本申请的储能电池包的温度管理装置,包括:温度检测模块,用于获取储能电池的温度;控制模块,用于判断所述储能电池的温度与第一预设温度区间的关系、以及所述储能电池的温度与第一温度值、第二温度值的关系,若所述储能电池的温度处于所述第一预设温度区间外,且满足关系式:所述第一温度值≤所述储能电池的温度<所述第二温度值,则通过相变介质调节所述储能电池的温度以使所述储能电池的温度处于所述第一预设温度区内;其中,所述第二温度值高于所述第一预设温度区间的最大温度值,所述第一温度值小于所述第一预设温度区间的最低温度值。
根据本申请的储能电池包的温度管理装置,能够通过相变介质对储能电池进行控温,相变介质的控温均匀程度较佳,能够保证储能电池中的多个单体电池的温度一致和/或能够保证储能电池中的多个电池模组的温度一致,从而有利于提高储能电池的工作性能,有利于延长储能电池的使用寿命。
根据本申请的计算机可读存储介质,其上存储有储能电池包的温度管理程序,该储能电池包的温度管理程序被处理器执行时实现上述的储能电池包的温度管理方法。
根据本申请的计算机可读存储介质,能够通过相变介质对储能电池进行控温,相变介质的控温均匀程度较佳,能够保证储能电池中的多个单体电池的温度一致和/或能够保证储能电池中的多个电池模组的温度一致,从而有利于提高储能电池的工作性能,有利于延长储能电池的使用寿命。
根据本申请的用电设备,包括存储器、处理器及存储在存储器上并可在处理器上运行的储能电池包的温度管理程序,所述处理器执行所述储能电池包的温度管理程序时,实现上述的储能电池包的温度管理方法。
根据本申请的用电设备,能够通过相变介质对储能电池进行控温,相变介质的控温均匀程度较佳,能够保证储能电池中的多个单体电池的温度一致和/或能够保证储能电池中的多个电池模组的温度一致,从而有利于提高储能电池的工作性能,有利于延长储能电池的使用寿命。
本申请的附加方面和优点将在下面的描述中部分给出,部分将从下面的描述中变得明显,或通过本申请的实践了解到。
附图说明
图1是根据本申请实施例的储能电池包的温度管理方法的流程图;
图2是根据本申请实施例的储能电池包的温度管理方法的一个具体实施例的流程图;
图3是根据本申请实施例的储能电池包的温度管理装置的方框示意图;
图4是根据本申请实施例的用电设备的示意图;
图5是根据本申请实施例的储能电池和管道的示意图;
图6是根据本申请实施例的处理器、存储器、通信接口、通信总线的方框示意图。
说明书中的附图标记如下:
用电设备100;
温度管理装置10;温度检测模块11;控制模块12;
换热器20;流量调节器21;节流阀22;气体流速调节器23;加热器24;WiFi模块25;
储能电池30;单体电池31;
管道40;
处理器1201;通信接口1202;存储器1203;通信总线1204。
具体实施方式
下面详细描述本申请的实施例,所述实施例的示例在附图中示出,其中自始至终相同或类似的标号表示相同或类似的元件或具有相同或类似功能的元件。下面通过参考附图描述的实施例是示例性的,旨在用于解释本申请,而不能理解为对本申请的限制。
下面参考图1-图5描述根据本申请实施例的温度管理方法和温度管理装置10。
如图3所示,根据本申请实施例的温度管理装置10包括:温度检测模块11和控制模块12。
其中,温度检测模块11用于获取储能电池30的温度。需要说明的是,本申请所述的储能电池30,是指储能电池包内的电池整体,换句话说,本申请所述的储能电池30,是对储能电池包内的所有电池的总称。
温度检测模块11用于获取储能电池30的温度,是指温度检测模块11可以获取储能电池30的温度;或者指温度检测模块11可以获取储能电池30内的电池模组的温度;或者指温度检测模块11可以获取储能电池30内的单体电池31的温度,例如,储能电池30可以包括六个电池模组,温度检测模块11可以获取六个电池模组各自的温度,再 例如,储能电池30可以包括六十个单体电池31,温度检测模块11可以获取六十个单体电池31各自的温度。
因此,本文中所述的储能电池30的温度,可以指储能电池30整体温度,也可以指储能电池30内的某一电池模组的温度,也可以指储能电池30内的某一单体电池31的温度。
温度检测模块11能够将获取的储能电池30的温度传递给控制模块12,控制模块12能够判断其接收到的储能电池30的温度与第一预设温度区间的关系,控制模块12还能够判断其接收到的储能电池30的温度与第一温度值、第二温度值的关系。其中,第二温度值高于第一预设温度区间的最大温度值,第一温度值小于第一预设温度区间的最低温度值。
若储能电池30的温度处于第一预设温度区间外(即储能电池30的温度高于第一预设温度区间的最大温度值,或者储能电池30的温度小于第一预设温度区间的最低温度值),判断储能电池30的温度与第一温度值、第二温度值的关系,若储能电池30的温度满足关系式:第一温度值≤储能电池30的温度<第二温度值(对此可以理解为,第一温度值≤储能电池30的温度<第一预设温度区间的最低温度值,或者,第一预设温度区间的最大温度值<储能电池30的温度<第二温度值),则通过相变介质调节储能电池30的温度,以使储能电池30的温度处于第一预设温度区内。
例如,温度检测模块11可以获取储能电池30中的六十个单体电池31各自的温度,并将获取的六十个单体电池31各自的温度传递给控制模块12,控制模块12可以对六十个单体电池31各自的温度分别进行判断,若其中一个单体电池31的温度处于第一预设温度区间外,而且大于等于第一温度值、小于第二温度值,则通过相变介质调节储能电池30的温度。
相变介质可以设置在储能电池30的附近,当储能电池30的温度处于第一预设温度区间外,而且满足关系式:第一温度值≤储能电池30的温度<第一预设温度区间的最低温度值,说明此时储能电池30的温度较低,设置在储能电池30附近的相变介质能够释放热量以提升储能电池30的温度。当储能电池30的温度处于第一预设温度区间外,而且满足关系式:第一预设温度区间的最大温度值<储能电池30的温度<第二温度值,说明此时储能电池30的温度较高,设置在储能电池30附近的相变介质能够吸收热量以降低储能电池30的温度。此过程对电池模组或者单体电池31也适用,在此不再赘述。
相变介质(PCM-Phase Change Material)是指温度不变的情况下而改变物质状态并能提供潜热的物质,相变介质的物质状态变化可以为固-固、固-液、固-气、液-液、液-气等。相变介质的控温均匀程度较佳,通过相变介质来调节储能电池30的温度,能 够保证储能电池30中的多个单体电池31的温度一致,换句话说,能够使多个单体电池31的温度维持较小的温度差异,能够使多个电池模组的温度维持较小的温度差异,从而有利于提高储能电池30的工作性能,延长储能电池30的使用寿命。
可选地,温度检测模块11与控制模块12通讯连接,温度检测模块11与控制模块12可以集成设置,温度检测模块11与控制模块12也可以单独设置,温度检测模块11和/或控制模块12可以与BMS(电池管理系统-BAERY MANAGEMEN SYSEM)集成设置,温度检测模块11和/或控制模块12也可以与整车控制器集成设置,本申请对此不做限制。
进一步地,当温度检测模块11用于获取储能电池30的温度是指获取储能电池30内的电池模组的温度,或者是指获取储能电池30内的单体电池31的温度时,设置在电池模组或者单体电池31附近的相变介质能够调节电池模组的温度或者调节单体电池31的温度,以实现精准温控。
由此,根据本申请的温度管理装置10,能够通过相变介质对储能电池30进行控温,相变介质的控温均匀程度较佳,能够保证储能电池30中的多个单体电池31的温度一致和/或能够保证储能电池30中的多个电池模组的温度一致,从而有利于提高储能电池30的工作性能,有利于延长储能电池30的使用寿命。
在本申请的一些实施例中,如图5所示,相变介质位于管道40内,管道40绕设于储能电池30设置。可选地,管道40可以分为多个子管道,多个子管道的数量可以与储能电池30内的电池模组的数量相同,多个子管道可以分别与多个电池模组对应设置,这样当某一电池模组的温度(或某一单体电池31的温度)处于第一预设温度区间外时,可以通过与该电池模组(或单体电池31)对应设置的子管道内的相变介质对该电池模组(或单体电池31)进行温度控制,这样有利于提高控温的精确度。
进一步地,管道40与储能电池30之间设置有导热件,导热件可以构造为导热率较高的导热硅片,这样设置可以提高相变介质与储能电池30的换热效率,并且,有利于提高相变介质的控温均匀程度,能够进一步保证储能电池30中的多个单体电池31的温度一致和/或能够进一步保证储能电池30中的多个电池模组的温度一致。
作为本申请的一些实施例,判断储能电池30的温度处于第一预设温度区外后,还包括:若储能电池30的温度≥第二温度值,控制相变介质循环流动并通过换热器20(如图4所示)。
相变介质的物质状态变化优选为液-液,当控制模块12判断储能电池30的温度≥第二温度值时,控制模块12可以通过控制泵(或者其他驱动液体流动的装置),以使位于管道40内的相变介质流动并通过换热器20,可以理解的是,若储能电池30的温度≥第二温度值,则说明此时储能电池30的温度较高,若仅通过位于附近的相变介质 难以将温度下降至第一预设温度区间内,因此,通过控制相变介质流动,可以使管道40内的相变介质均能够调节储能电池30温度较高的区域,以迅速将储能电池30的温度下降至第一预设温度区间内,而且有利于保证储能电池30中的多个单体电池31的温度一致和/或有利于保证储能电池30中的多个电池模组的温度一致。
进一步地,管道40内的相变介质能够流经换热器20,相变介质在换热器20内能够快速将热量散去,这样设置可以使从换热器20流出的相变介质处于能够吸收较多热量的形态,有利于提高温度管理装置10的降温速率。
需要说明的是,若某一电池模组的温度≥第二温度值,可以控制与该电池模组对应的子管道内的相变介质流动并且流经换热器20,这样设置能够实现对储能电池30的精准温控。
进一步地,计算储能电池30的温度与第二温度值的差值,根据储能电池30的温度与第二温度值的差值调节相变介质的流量。具体来说,储能电池30的温度与第二温度值的差值与相变介质的流量成正比,也就是说,若储能电池30的温度与第二温度值的差值越大,说明储能电池30的温度越高,通过增大相变介质的流量,能够提高温度管理装置10的温控速率。
其中,如图4所示,可以通过在管道40中设置流量调节器21和/或节流阀22来调节相变介质的流量。作为一种可选实施例,每个子管道上均可以设置有流量调节器21,这样设置可以实现对子管道流量的单独控制。
简而言之,当储能电池30的温度指储能电池30整体温度时,可以控制所有管道40内的相变介质流动(包括控制流量),当储能电池30的温度指储能电池30内的某一电池模组的温度,或者指储能电池30内的某一单体电池31的温度时,可以控制与温度异常的电池模组或单体电池31对应的子管道内的相变介质流动(包括控制流量)。
作为本申请的一些实施例,判断储能电池30的温度≥第二温度值后,包括:判断储能电池30的温度与第四温度值的关系,其中,第四温度值高于第二温度值,若储能电池30的温度≥第四温度值,则控制气体流速调节器23工作以提高换热器20周围的空气流速和/或提高相变介质周围的空气流速。
其中,如图4所示,气体流速调节器23可以构造为散热风机,气体流速调节器23可以设置在换热器20附近,或者气体流速调节器23可以设置在管道40附近,或者气体流速调节器23可以设置在换热器20和管道40附近。通过气体流速调节器23提高空气流速,能够快速将管道40和/或换热器20内的相变介质的热量散去,从而可以进一步提高温度管理装置10的降温速率。
可选地,作为一种实施例,可以计算储能电池30的温度与第四温度值的差值,根 据储能电池30的温度与第四温度值的差值控制气体流速调节器23的工况(例如散热风机的档位)。具体来说,若储能电池30的温度与第四温度值的差值越大,说明储能电池30的温度越高,通过增大散热风机的转速,能够提高温度管理装置10的温控速率。
作为本申请的一些实施例,判断储能电池30的温度处于第一预设温度区外后,还包括:若储能电池30的温度<第一温度值,控制相变介质循环流动。
相变介质的物质状态变化优选为液-液,当控制模块12判断储能电池30的温度<第一温度值时,控制模块12可以通过控制泵(或者其他驱动液体流动的装置),以使位于管道40内的相变介质流动,可以理解的是,若储能电池30的温度<第一温度值,则说明此时储能电池30的温度较低,若仅通过位于附近的相变介质难以将温度升高至第一预设温度区间内,因此,通过控制相变介质流动,可以使管道40内的相变介质均能够调节储能电池30内温度较低的区域,以迅速将储能电池30的温度升高至第一预设温度区间内,而且有利于保证储能电池30中的多个单体电池31的温度一致和/或有利于保证储能电池30中的多个电池模组的温度一致。
需要说明的是,若某一电池模组的温度<第一温度值,可以控制与该电池模组对应的子管道内的相变介质流动,这样设置能够实现对储能电池30的精准温控。
进一步地,计算储能电池30的温度与第一温度值的差值,根据储能电池30的温度与第一温度值的差值调节相变介质的流量。具体来说,储能电池30的温度与第一温度值的差值与相变介质的流量成正比,也就是说,若储能电池30的温度与第一温度值的差值越大,说明储能电池30的温度越低,通过增大相变介质的流量,能够提高温度管理装置10的温控速率。
其中,可以通过在管道40中设置流量调节器21和/或节流阀22来调节相变介质的流量。作为一种可选实施例,每个子管道上均可以设置有流量调节器21,这样设置可以实现对子管道流量的单独控制。
简而言之,当储能电池30的温度指储能电池30整体温度时,可以控制所有管道40内的相变介质流动(包括控制流量),当储能电池30的温度指储能电池30内的某一电池模组的温度,或者指储能电池30内的某一单体电池31的温度时,可以控制与温度异常的电池模组或单体电池31对应的子管道内的相变介质流动(包括控制流量)。
作为本申请的一些实施例,判断储能电池30的温度<第一温度值后,包括:判断储能电池30的温度与第三温度值的关系,其中,第三温度值低于第一温度值;若储能电池30的温度<第三温度值,则控制加热器24工作以加热其周围的相变介质。
其中,如图4所示,加热器24可以构造为PTC加热件(Positive Temperature Coefficient-heater),加热器24可以设置在管道40附近,通过控制加热器24工作, 能够对位于加热器24附近的相变介质进行加热,能够快速提高管道40内的相变介质的热量,从而可以进一步提高温度管理装置10的升温速率。
可选地,作为一种实施例,可以计算储能电池30的温度与第三温度值的差值,根据储能电池30的温度与第三温度值的差值控制加热器24的工况(例如加热器24的档位)。具体来说,若储能电池30的温度与第三温度值的差值越大,说明储能电池30的温度越低,通过增大加热器24的发热量,能够提高温度管理装置10的温控速率。
需要强调的是,当储能电池30的温度指储能电池30整体温度时,可以通过控制管道40内相变介质的流动、相变介质的流速、气体流速调节器23以及加热器24来实现对储能电池30的温控,此时仅需要设置一个换热器20、一个气体流速调节器23、一个流量调节器21和一个加热器24。
当储能电池30的温度指储能电池30内的某一电池模组的温度,或者指储能电池30内的某一单体电池31的温度时,管道40可以分为多个子管道,多个子管道的数量可以与储能电池30内的电池模组的数量相同,多个子管道可以分别与多个电池模组对应设置(或者子管道的数量少于电池模组的数量,一个子管道对应多个电池模组;或者子管道的数量高于电池模组的数量,多个子管道对应一个电池模组)。
每个子管道均可以设置有换热器20、气体流速调节器23、流量调节器21和加热器24。或者,管道40还可以包括与多个子管道连通的总管道,换热器20、气体流速调节器23和加热器24可以设置在总管道,并且,总管道上可以设置有节流阀22以辅助控制相变介质的流量
当然,也可以根据实际需求来设计换热器20、气体流速调节器23、流量调节器21和加热器24的设置数量以及设置位置。本申请只是提出几个优选实施例,并不能理解为对本申请的限制。
作为本申请的一些实施例,温度管理装置10还可以获取外界环境温度以及用电设备100工况,根据外界环境温度和用电设备100工况调节第一温度值和/或第二温度值和/或第三温度值和/或第四温度值;
和/或,通过云服务器调节第一温度值和/或第二温度值和/或第三温度值和/或第四温度值。
需要说明的是,第一温度值、第二温度值、第三温度值以及第四温度值不是一个定值,由于相变介质的特性,相变介质的吸热、放热能力与外界环境温度具有一定的关系,并且,用电设备100的工况对储能电池30的温度控制也具有一定的要求。
例如,若此时用电设备100处于剧烈的工作状态下,储能电池30的温度会以较快的速度升高,此时需要快速对储能电池30进行降温,因此,控制模块12可以根据用电 设备100的工况适当调低第二温度值和第四温度值,以便于快速触发相变介质流动以及气体流速调节器23工作。
再例如,若此时外界温度非常低,并且储能电池30的温度处于较低状态时,需要快速对储能电池30进行升温,因此,控制模块12可以根据外界环境温度适当调高第一温度值和第三温度值,以便快速触发相变介质流动以及加热器24工作。
如此设置可以根据外界环境温度和用电设备100工况调节第一温度值和/或第二温度值和/或第三温度值和/或第四温度值,以使温度管理装置10能够可靠的调节储能电池30的温度。
此外,云服务器可以远程获取用电设备100工况以及用电设备100所处地的环境温度,并根据用电设备100工况以及用电设备100所处地的环境温度调节第一温度值和/或第二温度值和/或第三温度值和/或第四温度值。如此设置当遭遇极端环境温度或者极端工况,超出用电设备100预设的算法或者控制参照表所能处理的范围时,可以通过云服务器远程操控,从而能够更加可靠的调节储能电池30的温度。
具体地,作为本申请的一个具体实施例,如图4所示,上述的温度管理装置10还可以包括:WiFi模块25,WiFi模块25可以用于与云服务器通讯。
图1为根据本申请实施例的温度管理方法的流程图,上述实施例的温度管理装置可以实现该温度管理方法,如图1所示,该温度管理方法包括以下步骤:
S1,获取储能电池的温度。其中,温度检测模块用于获取储能电池的温度。需要说明的是,本申请所述的储能电池,是指储能电池包内的电池整体,换句话说,本申请所述的储能电池,是对储能电池包内的所有电池的总称。
温度检测模块用于获取储能电池的温度,是指温度检测模块可以获取储能电池的温度;或者指温度检测模块可以获取储能电池内的电池模组的温度;或者指温度检测模块可以获取储能电池内的单体电池的温度,例如,储能电池可以包括六个电池模组,温度检测模块可以获取六个电池模组各自的温度,再例如,储能电池可以包括六十个单体电池,温度检测模块可以获取六十个单体电池各自的温度。
因此,本文中所述的储能电池的温度,可以指储能电池整体温度,也可以指储能电池内的某一电池模组的温度,也可以指储能电池内的某一单体电池的温度。
S2,判断所述储能电池的温度与第一预设温度区间的关系。温度检测模块能够将获取的储能电池的温度传递给控制模块,控制模块能够判断其接收到的储能电池的温度与第一预设温度区间的关系。
S3,若所述储能电池的温度处于所述第一预设温度区间外,则判断所述储能电池的温度与第一温度值、第二温度值的关系,其中,所述第二温度值高于所述第一预设温度 区间的最大温度值,所述第一温度值低于所述第一预设温度区间的最低温度值。控制模块能够判断其接收到的储能电池的温度与第一温度值、第二温度值的关系。
若储能电池的温度处于第一预设温度区间外(即储能电池的温度高于第一预设温度区间的最大温度值,或者储能电池的温度小于第一预设温度区间的最低温度值),判断储能电池的温度与第一温度值、第二温度值的关系,若储能电池的温度满足关系式:第一温度值≤储能电池的温度<第二温度值(对此可以理解为,第一温度值≤储能电池的温度<第一预设温度区间的最低温度值,或者,第一预设温度区间的最大温度值<储能电池的温度<第二温度值),则通过相变介质调节储能电池的温度,以使储能电池的温度处于第一预设温度区内。
例如,温度检测模块可以获取储能电池中的六十个单体电池各自的温度,并将获取的六十个单体电池各自的温度传递给控制模块,控制模块可以对六十个单体电池各自的温度分别进行判断,若其中一个单体电池的温度处于第一预设温度区间外,而且大于等于第一温度值、小于第二温度值,则通过相变介质调节储能电池的温度。
相变介质可以设置在储能电池的附近,当储能电池的温度处于第一预设温度区间外,而且满足关系式:第一温度值≤储能电池的温度<第一预设温度区间的最低温度值,说明此时储能电池的温度较低,设置在储能电池附近的相变介质能够释放热量以提升储能电池的温度。当储能电池的温度处于第一预设温度区间外,而且满足关系式:第一预设温度区间的最大温度值<储能电池的温度<第二温度值,说明此时储能电池的温度较高,设置在储能电池附近的相变介质能够吸收热量以降低储能电池的温度。此过程对电池模组或者单体电池也适用,在此不再赘述。
相变介质(PCM-Phase Change Material)是指温度不变的情况下而改变物质状态并能提供潜热的物质,相变介质的物质状态变化可以为固-固、固-液、固-气、液-液、液-气等。相变介质的控温均匀程度较佳,通过相变介质来调节储能电池的温度,能够保证储能电池中的多个单体电池的温度一致,换句话说,能够使多个单体电池的温度维持较小的温度差异,能够使多个电池模组的温度维持较小的温度差异,从而有利于提高储能电池的工作性能,延长储能电池的使用寿命。
可选地,温度检测模块与控制模块通讯连接,温度检测模块与控制模块可以集成设置,温度检测模块与控制模块也可以单独设置,温度检测模块和/或控制模块可以与BMS(电池管理系统-BAERY MANAGEMEN SYSEM)集成设置,温度检测模块和/或控制模块也可以与整车控制器集成设置,本申请对此不做限制。
进一步地,当温度检测模块用于获取储能电池的温度是指获取储能电池内的电池模组的温度,或者是指获取储能电池内的单体电池的温度时,设置在电池模组或者单体电 池附近的相变介质能够调节电池模组的温度或者调节单体电池的温度,以实现精准温控。
由此,根据本申请的温度管理方法,能够通过相变介质对储能电池进行控温,相变介质的控温均匀程度较佳,能够保证储能电池中的多个单体电池的温度一致和/或能够保证储能电池中的多个电池模组的温度一致,从而有利于提高储能电池的工作性能,有利于延长储能电池的使用寿命。
作为本申请的一些实施例中,相变介质位于管道内,管道绕设于储能电池设置。可选地,管道可以分为多个子管道,多个子管道的数量可以与储能电池内的电池模组的数量相同,多个子管道可以分别与多个电池模组对应设置,这样当某一电池模组的温度(或某一单体电池的温度)处于第一预设温度区间外时,可以通过与该电池模组(或单体电池)对应设置的子管道内的相变介质对该电池模组(或单体电池)进行温度控制,这样有利于提高控温的精确度。
进一步地,管道与储能电池之间设置有导热件,导热件可以构造为导热率较高的导热硅片,这样设置可以提高相变介质与储能电池的换热效率,并且,有利于提高相变介质的控温均匀程度,能够进一步保证储能电池中的多个单体电池的温度一致和/或能够进一步保证储能电池中的多个电池模组的温度一致。
在本申请的一些实施例中,判断储能电池的温度处于第一预设温度区外后,还包括:若储能电池的温度≥第二温度值,控制相变介质循环流动并通过换热器。
相变介质的物质状态变化优选为液-液,当控制模块判断储能电池的温度≥第二温度值时,控制模块可以通过控制泵(或者其他驱动液体流动的装置),以使位于管道内的相变介质流动并通过换热器,可以理解的是,若储能电池的温度≥第二温度值,则说明此时储能电池的温度较高,若仅通过位于附近的相变介质难以将温度下降至第一预设温度区间内,因此,通过控制相变介质流动,可以使管道内的相变介质均能够调节储能电池温度较高的区域,以迅速将储能电池的温度下降至第一预设温度区间内,而且有利于保证储能电池中的多个单体电池的温度一致和/或有利于保证储能电池中的多个电池模组的温度一致。
进一步地,管道内的相变介质能够流经换热器,相变介质在换热器内能够快速将热量散去,这样设置可以使从换热器流出的相变介质处于能够吸收较多热量的形态,有利于提高降温速率。
需要说明的是,若某一电池模组的温度≥第二温度值,可以控制与该电池模组对应的子管道内的相变介质流动并且流经换热器,这样设置能够实现对储能电池的精准温控。
进一步地,计算储能电池的温度与第二温度值的差值,根据储能电池的温度与第二温度值的差值调节相变介质的流量。具体来说,储能电池的温度与第二温度值的差值与相变介质的流量成正比,也就是说,若储能电池的温度与第二温度值的差值越大,说明储能电池的温度越高,通过增大相变介质的流量,能够提高温控速率。
其中,可以通过在管道中设置流量调节器和/或节流阀来调节相变介质的流量。作为一种可选实施例,每个子管道上均可以设置有流量调节器,这样设置可以实现对子管道流量的单独控制。
简而言之,当储能电池的温度指储能电池整体温度时,可以控制所有管道内的相变介质流动(包括控制流量),当储能电池的温度指储能电池内的某一电池模组的温度,或者指储能电池内的某一单体电池的温度时,可以控制与温度异常的电池模组或单体电池对应的子管道内的相变介质流动(包括控制流量)。
在本申请的一些实施例中,判断储能电池的温度≥第二温度值后,包括:判断储能电池的温度与第四温度值的关系,其中,第四温度值高于第二温度值,若储能电池的温度≥第四温度值,则控制气体流速调节器工作以提高换热器周围的空气流速和/或提高相变介质周围的空气流速。
其中,气体流速调节器可以构造为散热风机,气体流速调节器可以设置在换热器附近,或者气体流速调节器可以设置在管道附近,或者气体流速调节器可以设置在换热器和管道附近。通过气体流速调节器提高空气流速,能够快速将管道和/或换热器内的相变介质的热量散去,从而可以进一步提高降温速率。
可选地,作为一种实施例,可以计算储能电池的温度与第四温度值的差值,根据储能电池的温度与第四温度值的差值控制气体流速调节器的工况(例如散热风机的档位)。具体来说,若储能电池的温度与第四温度值的差值越大,说明储能电池的温度越高,通过增大散热风机的转速,能够提高温控速率。
在本申请的一些实施例中,判断储能电池的温度处于第一预设温度区外后,还包括:若储能电池的温度<第一温度值,控制相变介质循环流动。
相变介质的物质状态变化优选为液-液,当控制模块判断储能电池的温度<第一温度值时,控制模块可以通过控制泵(或者其他驱动液体流动的装置),以使位于管道内的相变介质流动,可以理解的是,若储能电池的温度<第一温度值,则说明此时储能电池的温度较低,若仅通过位于附近的相变介质难以将温度升高至第一预设温度区间内,因此,通过控制相变介质流动,可以使管道内的相变介质均能够调节储能电池内温度较低的区域,以迅速将储能电池的温度升高至第一预设温度区间内,而且有利于保证储能电池中的多个单体电池的温度一致和/或有利于保证储能电池中的多个电池模组的温度 一致。
需要说明的是,若某一电池模组的温度<第一温度值,可以控制与该电池模组对应的子管道内的相变介质流动,这样设置能够实现对储能电池的精准温控。
进一步地,计算储能电池的温度与第一温度值的差值,根据储能电池的温度与第一温度值的差值调节相变介质的流量。具体来说,储能电池的温度与第一温度值的差值与相变介质的流量成正比,也就是说,若储能电池的温度与第一温度值的差值越大,说明储能电池的温度越低,通过增大相变介质的流量,能够提高温控速率。
其中,可以通过在管道中设置流量调节器和/或节流阀来调节相变介质的流量。作为一种可选实施例,每个子管道上均可以设置有流量调节器,这样设置可以实现对子管道流量的单独控制。
简而言之,当储能电池的温度指储能电池整体温度时,可以控制所有管道内的相变介质流动(包括控制流量),当储能电池的温度指储能电池内的某一电池模组的温度,或者指储能电池内的某一单体电池的温度时,可以控制与温度异常的电池模组或单体电池对应的子管道内的相变介质流动(包括控制流量)。
在本申请的一些实施例中,判断储能电池的温度<第一温度值后,包括:判断储能电池的温度与第三温度值的关系,其中,第三温度值低于第一温度值;若储能电池的温度<第三温度值,则控制加热器工作以加热其周围的相变介质。
其中,加热器可以构造为PTC加热件(Positive Temperature Coefficient-heater),加热器可以设置在管道附近,通过控制加热器工作,能够对位于加热器附近的相变介质进行加热,能够快速提高管道内的相变介质的热量,从而可以进一步提高升温速率。
可选地,作为一种实施例,可以计算储能电池的温度与第三温度值的差值,根据储能电池的温度与第三温度值的差值控制加热器的工况(例如加热器的档位)。具体来说,若储能电池的温度与第三温度值的差值越大,说明储能电池的温度越低,通过增大加热器的发热量,能够提高温控速率。
需要强调的是,当储能电池的温度指储能电池整体温度时,可以通过控制管道内相变介质的流动、相变介质的流速、气体流速调节器以及加热器来实现对储能电池的温控,此时仅需要设置一个换热器、一个气体流速调节器、一个流量调节器和一个加热器。
当储能电池的温度指储能电池内的某一电池模组的温度,或者指储能电池内的某一单体电池的温度时,管道可以分为多个子管道,多个子管道的数量可以与储能电池内的电池模组的数量相同,多个子管道可以分别与多个电池模组对应设置(或者子管道的数量少于电池模组的数量,一个子管道对应多个电池模组;或者子管道的数量高于电池模 组的数量,多个子管道对应一个电池模组)。
每个子管道均可以设置有换热器、气体流速调节器、流量调节器和加热器。或者,管道还可以包括与多个子管道连通的总管道,换热器、气体流速调节器和加热器可以设置在总管道,并且,总管道上可以设置有节流阀以辅助控制相变介质的流量
当然,也可以根据实际需求来设计换热器、气体流速调节器、流量调节器和加热器的设置数量以及设置位置。本申请只是提出几个优选实施例,并不能理解为对本申请的限制。
在本申请的一些实施例中,储能电池包的温度管理方法还包括:获取外界环境温度以及用电设备工况,根据外界环境温度和用电设备工况调节第一温度值和/或第二温度值和/或第三温度值和/或第四温度值;
和/或,通过云服务器调节第一温度值和/或第二温度值和/或第三温度值和/或第四温度值。
需要说明的是,第一温度值、第二温度值、第三温度值以及第四温度值不是一个定值,由于相变介质的特性,相变介质的吸热、放热能力与外界环境温度具有一定的关系,并且,用电设备的工况对储能电池的温度控制也具有一定的要求。
例如,若此时用电设备处于剧烈的工作状态下,储能电池的温度会以较快的速度升高,此时需要快速对储能电池进行降温,因此,控制模块可以根据用电设备的工况适当调低第二温度值和第四温度值,以便于快速触发相变介质流动以及气体流速调节器工作。
再例如,若此时外界温度非常低,并且储能电池的温度处于较低状态时,需要快速对储能电池进行升温,因此,控制模块可以根据外界环境温度适当调高第一温度值和第三温度值,以便快速触发相变介质流动以及加热器工作。
如此设置可以根据外界环境温度和用电设备工况调节第一温度值和/或第二温度值和/或第三温度值和/或第四温度值,从而能够可靠的调节储能电池的温度。
此外,云服务器可以远程获取用电设备工况以及用电设备所处地的环境温度,并根据用电设备工况以及用电设备所处地的环境温度调节第一温度值和/或第二温度值和/或第三温度值和/或第四温度值。如此设置当遭遇极端环境温度或者极端工况,超出用电设备预设的算法或者控制参照表所能处理的范围时,可以通过云服务器远程操控,从而能够更加可靠的调节储能电池的温度。
具体地,如图2所示,作为本申请的一个具体实施例,上述的温度管理方法可以包括以下步骤:
S01,获取储能电池的温度;
S02,判断储能电池的温度是否处于第一预设温度区间外;
S03,判断储能电池的温度是否满足关系式:第一温度值≤储能电池的温度<第二温度值;
S04,通过相变介质调节储能电池的温度;
S05,判断储能电池的温度是否满足关系式:储能电池的温度≥第二温度值;
S06,控制相变介质循环流动并通过换热器;
S07,判断储能电池的温度是否满足关系式:储能电池的温度≥第四温度值;
S08,控制气体流速调节器工作;
S09,判断储能电池的温度是否满足关系式:储能电池的温度<第一温度值;
S10,控制相变介质循环流动;
S11,判断储能电池的温度是否满足关系式:储能电池的温度<第三温度值;
S12,控制加热器工作。
其中,在步骤S02中,若判断是,则进入步骤S03,若判断否,则返回步骤S01。在步骤S03中,若判断是,则进入步骤S04,若判断否,则返回步骤S01。在步骤S05中,若判断是,则进入步骤S06,若判断否,则返回步骤S03。在步骤S07中,若判断是,则进入步骤S08,若判断否,则返回步骤S05。在步骤S09中,若判断是,则进入步骤S10,若判断否,则返回步骤S03。在步骤S11中,若判断是,则进入步骤S12,若判断否,则返回步骤S09。
为了实现上述实施例,本申请提出一种计算机可读存储介质,其上存储有便储能电池包的温度管理程序,该温度管理程序被处理器执行时,可以实现上述实施例的温度管理方法。
根据本申请实施例的计算机可读存储介质,能够通过相变介质对储能电池进行控温,相变介质的控温均匀程度较佳,能够保证储能电池中的多个单体电池的温度一致和/或能够保证储能电池中的多个电池模组的温度一致,从而有利于提高储能电池的工作性能,有利于延长储能电池的使用寿命。
为了实现上述实施例,本申请还提出一种用电设备,用电设备包括存储器、处理器及存储在存储器上并可在处理器上运行的储能电池包的温度管理程序,处理器执行该温度管理程序时,可以实现上述实施例的温度管理方法。
根据本申请实施例的用电设备,通过处理器执行存储器上存储的储能电池包的温度管理程序,能够通过相变介质对储能电池进行控温,相变介质的控温均匀程度较佳,能够保证储能电池中的多个单体电池的温度一致和/或能够保证储能电池中的多个电池模组的温度一致,从而有利于提高储能电池的工作性能,有利于延长储能电池的使用寿命。
如图6所示,该用电设备可以包括至少一个处理器1201,至少一个通信接口1202,至少一个存储器1203和至少一个通信总线1204。在本申请的实施例中,处理器1201、通信接口1202、存储器1203、通信总线1204的数量为至少一个,且处理器1201、通信接口1202、存储器1203通过通信总线1204完成相互间的通信。
其中,存储器1203可以是,但不限于,随机存取存储器(Random Access Memory,RAM),只读存储器(Read Only Memory,ROM),可编程只读存储器(Programmable Read-Only Memory,PROM),可擦除只读存储器(Erasable Programmable Read-Only Memory,EPROM),电可擦除只读存储器(Electric Erasable Programmable Read-Only Memory,EEPROM)等。其中,存储器1203用于存储程序,处理器1201在接收到执行指令后,执行所述程序,实现上述实施例描述的储能电池包的温度管理方法的步骤。
处理器1201可能是一种集成电路芯片,具有信号的处理能力。上述的处理器可以是通用处理器,包括中央处理器(Central Processing Unit,CPU)、网络处理器(NetworkProcessor,NP)等;还可以是数字信号处理器(DSP)、专用集成电路(ASIC)、现场可编程门阵列(FPGA)或者其他可编程逻辑器件、分立门或者晶体管逻辑器件、分立硬件组件。可以实现或者执行本申请实施例中的公开的各方法、步骤及逻辑框图。通用处理器可以是微处理器或者该处理器也可以是任何常规的处理器等。
需要说明的是,在流程图中表示或在此以其他方式描述的逻辑和/或步骤,例如,可以被认为是用于实现逻辑功能的可执行指令的定序列表,可以具体实现在任何计算机可读介质中,以供指令执行系统、装置或设备(如基于计算机的系统、包括处理器的系统或其他可以从指令执行系统、装置或设备取指令并执行指令的系统)使用,或结合这些指令执行系统、装置或设备而使用。就本说明书而言,"计算机可读介质"可以是任何可以包含、存储、通信、传播或传输程序以供指令执行系统、装置或设备或结合这些指令执行系统、装置或设备而使用的装置。计算机可读介质的更具体的示例(非穷尽性列表)包括以下:具有一个或多个布线的电连接部(电子装置),便携式计算机盘盒(磁装置),随机存取存储器(RAM),只读存储器(ROM),可擦除可编辑只读存储器(EPROM或闪速存储器),光纤装置,以及便携式光盘只读存储器(CDROM)。另外,计算机可读介质甚至可以是可在其上打印所述程序的纸或其他合适的介质,因为可以例如通过对纸或其他介质进行光学扫描,接着进行编辑、解译或必要时以其他合适方式进行处理来以电子方式获得所述程序,然后将其存储在计算机存储器中。
应当理解,本申请的各部分可以用硬件、软件、固件或它们的组合来实现。在上述实施方式中,多个步骤或方法可以用存储在存储器中且由合适的指令执行系统执行的软件或固件来实现。例如,如果用硬件来实现,和在另一实施方式中一样,可用本领域公 知的下列技术中的任一项或他们的组合来实现:具有用于对数据信号实现逻辑功能的逻辑门电路的离散逻辑电路,具有合适的组合逻辑门电路的专用集成电路,可编程门阵列(PGA),现场可编程门阵列(FPGA)等。
在本申请的描述中,需要理解的是,术语“中心”、“纵向”、“横向”、“长度”、“宽度”、“厚度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”、“顺时针”、“逆时针”、“轴向”、“径向”、“周向”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本申请和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。
在本申请的描述中,“第一特征”、“第二特征”可以包括一个或者更多个该特征。
在本申请的描述中,“多个”的含义是两个或两个以上。
在本申请的描述中,第一特征在第二特征“之上”或“之下”可以包括第一和第二特征直接接触,也可以包括第一和第二特征不是直接接触而是通过它们之间的另外的特征接触。
在本申请的描述中,第一特征在第二特征“之上”、“上方”和“上面”包括第一特征在第二特征正上方和斜上方,或仅仅表示第一特征水平高度高于第二特征。
在本说明书的描述中,参考术语“一个实施例”、“一些实施例”、“示意性实施例”、“示例”、“具体示例”、或“一些示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本申请的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不一定指的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任何的一个或多个实施例或示例中以合适的方式结合。
尽管已经示出和描述了本申请的实施例,本领域的普通技术人员可以理解:在不脱离本申请的原理和宗旨的情况下可以对这些实施例进行多种变化、修改、替换和变型,本申请的范围由权利要求及其等同物限定。

Claims (10)

  1. 一种储能电池包的温度管理方法,其中,包括:
    获取储能电池的温度;
    判断所述储能电池的温度与第一预设温度区间的关系;
    若所述储能电池的温度处于所述第一预设温度区间外,则判断所述储能电池的温度与第一温度值、第二温度值的关系,其中,所述第二温度值高于所述第一预设温度区间的最大温度值,所述第一温度值低于所述第一预设温度区间的最低温度值;
    若满足关系式:所述第一温度值≤所述储能电池的温度<所述第二温度值,通过相变介质调节所述储能电池的温度以使所述储能电池的温度处于所述第一预设温度区内。
  2. 根据权利要求1所述的储能电池包的温度管理方法,其中,判断所述储能电池的温度处于所述第一预设温度区外后,还包括:
    若所述储能电池的温度≥所述第二温度值,控制所述相变介质循环流动并通过换热器;
    计算所述储能电池的温度与所述第二温度值的差值,根据所述储能电池的温度与所述第二温度值的差值调节所述相变介质的流量。
  3. 根据权利要求2所述的储能电池包的温度管理方法,其中,判断所述储能电池的温度≥所述第二温度值后,包括:
    判断所述储能电池的温度与第四温度值的关系,其中,所述第四温度值高于所述第二温度值;
    若所述储能电池的温度≥所述第四温度值,则控制气体流速调节器工作以提高所述换热器周围的空气流速和/或提高所述相变介质周围的空气流速。
  4. 根据权利要求3所述的储能电池包的温度管理方法,其中,判断所述储能电池的温度处于所述第一预设温度区外后,还包括:
    若所述储能电池的温度<所述第一温度值,控制所述相变介质循环流动;
    计算所述储能电池的温度与所述第一温度值的差值,根据所述储能电池的温度与所述第一温度值的差值调节所述相变介质的流量。
  5. 根据权利要求4所述的储能电池包的温度管理方法,其中,判断所述储能电池的温度<所述第一温度值后,包括:
    判断所述储能电池的温度与第三温度值的关系,其中,所述第三温度值低于所述第一温度值;
    若所述储能电池的温度<所述第三温度值,则控制加热器工作以加热其周围的所述相变介质。
  6. 根据权利要求5所述的储能电池包的温度管理方法,其中,还包括:获取外界环境温度以及用电设备工况,根据所述外界环境温度和所述用电设备工况调节所述第一温度值和/或所述第二温度值和/或所述第三温度值和/或所述第四温度值;
    和/或,通过云服务器调节所述第一温度值和/或所述第二温度值和/或所述第三温度值和/或所述第四温度值。
  7. 一种储能电池包的温度管理装置,其中,包括:
    温度检测模块,用于获取储能电池的温度;
    控制模块,用于判断所述储能电池的温度与第一预设温度区间的关系、以及所述储能电池的温度与第一温度值、第二温度值的关系,若所述储能电池的温度处于所述第一预设温度区间外,且满足关系式:所述第一温度值≤所述储能电池的温度<所述第二温度值,则通过相变介质调节所述储能电池的温度以使所述储能电池的温度处于所述第一预设温度区内;
    其中,所述第二温度值高于所述第一预设温度区间的最大温度值,所述第一温度值小于所述第一预设温度区间的最低温度值。
  8. 根据权利要求7所述的储能电池包的温度管理装置,其中,所述相变介质位于管道内,所述管道绕设于所述储能电池,所述管道与所述储能电池之间设有导热件。
  9. 一种计算机可读存储介质,其中,其上存储有储能电池包的温度管理程序,该储能电池包的温度管理程序被处理器执行时实现根据权利要求1-6中任一项所述的储能电池包的温度管理方法。
  10. 一种用电设备,其中,包括存储器、处理器及存储在存储器上并可在处理器上运行的储能电池包的温度管理程序,所述处理器执行所述储能电池包的温度管理程序时,实现根据权利要求1-6中任一项所述的储能电池包的温度管理方法。
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