CN114927803A - Battery temperature adjusting method and device, storage medium and vehicle - Google Patents
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Abstract
本发明公开了一种电池温度的调节方法、装置、存储介质和车辆。其中,该方法包括:获取车辆中电池在当前时刻的状态数据,其中,状态数据用于表征电池在当前时刻充放电过程中的状态;基于状态数据,确定电池的目标换热功率;基于目标换热功率,调节电池的实际换热功率;利用实际换热功率调节电池在当前时刻后在充放电过程中的温度。本发明解决了控制车辆的电池温度的效率低的技术问题。
The invention discloses a battery temperature adjustment method, device, storage medium and vehicle. The method includes: acquiring state data of the battery in the vehicle at the current moment, wherein the state data is used to represent the state of the battery during the charging and discharging process at the current moment; determining the target heat exchange power of the battery based on the state data; Thermal power, adjust the actual heat exchange power of the battery; use the actual heat exchange power to adjust the temperature of the battery during the charging and discharging process after the current moment. The present invention solves the technical problem of low efficiency in controlling the battery temperature of the vehicle.
Description
技术领域technical field
本发明涉及车辆领域,具体而言,涉及一种电池温度的调节方法、装置、存储介质和车辆。The present invention relates to the field of vehicles, and in particular, to a method, device, storage medium and vehicle for adjusting battery temperature.
背景技术Background technique
目前,电池作为车辆的能量来源,对电池热管理的控制通常是以电池温度为主要控制输入源,但是,电池中电芯的温度传感器都布置于电芯外表面,热量的传递需要时间,且以电池温度为主要控制输入源需要预留较多的阈值余量以保证将电池温度控制在适宜区间,因此上述方案具有滞后性,且会导致能耗的增加,进一步加剧续驶里程焦虑,从而存在控制车辆的电池温度的效率低的技术问题。At present, the battery is used as the energy source of the vehicle, and the control of the battery thermal management is usually based on the battery temperature as the main control input source. However, the temperature sensors of the cells in the battery are all arranged on the outer surface of the cells, and the heat transfer takes time, and Taking the battery temperature as the main control input source needs to reserve more threshold margin to ensure that the battery temperature is controlled in a suitable range. Therefore, the above scheme has a hysteresis and will lead to an increase in energy consumption, further aggravating the anxiety of driving range, and thus There is a technical problem of inefficiency in controlling the temperature of the battery of the vehicle.
针对上述现有技术存在的控制车辆的电池温度的效率低的问题,目前尚未提出有效的解决方案。For the problem of low efficiency in controlling the temperature of the battery of the vehicle in the above-mentioned prior art, no effective solution has been proposed so far.
发明内容SUMMARY OF THE INVENTION
本发明实施例提供了一种电池温度的调节方法、装置、存储介质和车辆,以至少解决控制车辆的电池温度的效率低的技术问题。Embodiments of the present invention provide a battery temperature adjustment method, device, storage medium, and vehicle, so as to at least solve the technical problem of low efficiency in controlling the battery temperature of the vehicle.
根据本发明实施例的一个方面,提供了一种电池温度的调节方法。该方法包括:获取车辆中电池在当前时刻的状态数据,其中,状态数据用于表征电池在当前时刻充放电过程中的状态;基于状态数据,确定电池的目标换热功率;基于目标换热功率,调节电池的实际换热功率;利用实际换热功率调节电池在当前时刻后在充放电过程中的温度。According to an aspect of the embodiments of the present invention, a method for adjusting the temperature of a battery is provided. The method includes: acquiring state data of a battery in the vehicle at the current moment, wherein the state data is used to represent the state of the battery in the process of charging and discharging at the current moment; determining the target heat exchange power of the battery based on the state data; and based on the target heat exchange power , adjust the actual heat exchange power of the battery; use the actual heat exchange power to adjust the temperature of the battery during the charging and discharging process after the current moment.
可选地,基于状态数据,确定电池的目标换热功率,包括:基于状态数据中的电池温度和状态数据中的电池电流,确定电池的产热功率;基于电池温度、电池所处的环境温度和车辆中的换热介质温度,确定目标系数,其中,目标系数用于表征环境温度和换热介质温度对电池的换热功率影响的程度;基于目标系数和产热功率,确定目标换热功率。Optionally, based on the state data, determining the target heat exchange power of the battery includes: determining the heat generation power of the battery based on the battery temperature in the state data and the battery current in the state data; based on the battery temperature and the ambient temperature where the battery is located and the temperature of the heat exchange medium in the vehicle to determine the target coefficient, where the target coefficient is used to characterize the degree of influence of the ambient temperature and the temperature of the heat exchange medium on the heat exchange power of the battery; based on the target coefficient and heat production power, determine the target heat exchange power .
可选地,基于电池温度、环境温度和换热介质温度,确定目标系数,包括:基于电池温度和环境温度,确定第一系数,其中,第一系数用于表征环境温度对电池的换热功率影响的程度;基于环境温度和换热介质温度,确定第二系数,其中,第二系数用于表征换热介质温度对电池的换热功率影响的程度;将第一系数和第二系数二者之间的比值,确定为目标系数。Optionally, determining the target coefficient based on the battery temperature, the ambient temperature and the heat exchange medium temperature includes: determining a first coefficient based on the battery temperature and the ambient temperature, where the first coefficient is used to characterize the heat exchange power of the battery from the ambient temperature The degree of influence; the second coefficient is determined based on the ambient temperature and the temperature of the heat exchange medium, wherein the second coefficient is used to characterize the degree of influence of the temperature of the heat exchange medium on the heat exchange power of the battery; the first coefficient and the second coefficient are two The ratio between them is determined as the target coefficient.
可选地,基于目标系数和产热功率,确定电池的目标换热功率,包括:将目标系数和产热功率二者之间的乘积,确定为目标换热功率。Optionally, determining the target heat exchange power of the battery based on the target coefficient and the heat generation power includes: determining a product between the target coefficient and the heat generation power as the target heat exchange power.
可选地,基于电池温度和环境温度,确定第一系数,包括以下之一:响应于电池温度不小于温度阈值,且电池温度大于环境温度,确定第一系数;响应于电池温度不小于温度阈值,且电池温度等于环境温度,确定第一系数;响应于电池温度不小于温度阈值,且电池温度小于环境温度,确定第一系数。Optionally, determining the first coefficient based on the battery temperature and the ambient temperature, including one of the following: determining the first coefficient in response to the battery temperature being not less than the temperature threshold and the battery temperature being greater than the ambient temperature; determining the first coefficient in response to the battery temperature being not less than the temperature threshold , and the battery temperature is equal to the ambient temperature, the first coefficient is determined; the first coefficient is determined in response to the battery temperature not being less than the temperature threshold and the battery temperature being less than the ambient temperature.
可选地,基于环境温度和换热介质温度,确定第二系数,包括以下之一:响应于换热介质温度大于环境温度,确定第二系数;响应于换热介质温度等于环境温度,确定第二系数;响应于换热介质温度小于环境温度,确定第二系数。Optionally, determining the second coefficient based on the ambient temperature and the temperature of the heat exchange medium, including one of the following: determining the second coefficient in response to the temperature of the heat exchange medium being greater than the ambient temperature; determining the first coefficient in response to the temperature of the heat exchange medium being equal to the ambient temperature. A second coefficient; the second coefficient is determined in response to the heat exchange medium temperature being less than the ambient temperature.
可选地,基于目标换热功率,调节电池的实际换热功率,包括:基于数据库中目标换热功率对应的换热介质流量或换热介质温度,对车辆中换热介质流量或车辆中换热介质温度进行调节;基于调节后的车辆中换热介质流量或车辆中换热介质温度,调节电池的实际换热功率。Optionally, based on the target heat exchange power, adjusting the actual heat exchange power of the battery includes: based on the heat exchange medium flow or heat exchange medium temperature corresponding to the target heat exchange power in the database, adjusting the heat exchange medium flow in the vehicle or the heat exchange medium in the vehicle. The temperature of the heat medium is adjusted; based on the adjusted flow rate of the heat exchange medium in the vehicle or the temperature of the heat exchange medium in the vehicle, the actual heat exchange power of the battery is adjusted.
根据本发明实施例的另一方面,还提供了一种电池温度的调节装置。该装置包括:获取单元,用于获取车辆中电池在当前时刻的状态数据,其中,状态数据用于表征电池在当前时刻充放电过程中的状态;确定单元,用于基于状态数据,确定电池的目标换热功率;第一调节单元,用于基于目标换热功率,调节电池的实际换热功率;第二调节单元,用于利用实际换热功率调节电池在当前时刻后在充放电过程中的温度。According to another aspect of the embodiments of the present invention, a device for adjusting the temperature of a battery is also provided. The device includes: an acquiring unit for acquiring state data of the battery in the vehicle at the current moment, wherein the state data is used to represent the state of the battery in the process of charging and discharging at the current moment; a determining unit is used for determining the state of the battery based on the state data The target heat exchange power; the first adjustment unit is used to adjust the actual heat exchange power of the battery based on the target heat exchange power; the second adjustment unit is used to use the actual heat exchange power to adjust the battery during the charging and discharging process after the current moment. temperature.
根据本发明实施例的另一方面,还提供了一种计算机可读存储介质。该计算机可读存储介质包括存储的程序,其中,在程序运行时控制计算机可读存储介质所在设备执行本发明实施例的电池温度的调节方法。According to another aspect of the embodiments of the present invention, a computer-readable storage medium is also provided. The computer-readable storage medium includes a stored program, wherein when the program runs, the device where the computer-readable storage medium is located is controlled to execute the method for adjusting the battery temperature of the embodiment of the present invention.
根据本发明实施例的另一方面,还提供了一种处理器。该处理器用于运行程序,其中,在程序运行时执行本发明实施例的电池温度的调节方法。According to another aspect of the embodiments of the present invention, a processor is also provided. The processor is used for running a program, wherein the method for adjusting the battery temperature of the embodiment of the present invention is executed when the program is running.
根据本发明实施例的另一方面,还提供了一种车辆。该车辆用于执行本发明实施例的电池温度的调节方法。According to another aspect of the embodiments of the present invention, a vehicle is also provided. The vehicle is used to implement the battery temperature adjustment method of the embodiment of the present invention.
在本发明实施例中,获取车辆中电池在当前时刻的状态数据,其中,状态数据用于表征电池在当前时刻充放电过程中的状态;基于状态数据,确定电池的目标换热功率;基于目标换热功率,调节电池的实际换热功率;利用实际换热功率调节电池在当前时刻后在充放电过程中的温度。也就是说,本发明实施例通过实时获取电池在当前充放电过程中的状态,确定电池的目标换热功率,从而调节电池的实际换热功率,利用实际换热功率实时调节电池在当前充放电过程中的温度,实现了提高控制车辆的电池温度的效率的技术效果,解决了控制车辆的电池温度的效率低的技术问题。In the embodiment of the present invention, the state data of the battery in the vehicle at the current moment is obtained, wherein the state data is used to represent the state of the battery during the charging and discharging process at the current moment; based on the state data, the target heat exchange power of the battery is determined; The heat exchange power is used to adjust the actual heat exchange power of the battery; the actual heat exchange power is used to adjust the temperature of the battery during the charging and discharging process after the current moment. That is to say, the embodiment of the present invention determines the target heat exchange power of the battery by acquiring the state of the battery in the current charging and discharging process in real time, so as to adjust the actual heat exchange power of the battery, and uses the actual heat exchange power to adjust the current charging and discharging power of the battery in real time. The temperature in the process achieves the technical effect of improving the efficiency of controlling the temperature of the battery of the vehicle, and solves the technical problem of low efficiency of controlling the temperature of the battery of the vehicle.
附图说明Description of drawings
此处所说明的附图用来提供对本发明的进一步理解,构成本申请的一部分,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。在附图中:The accompanying drawings described herein are used to provide a further understanding of the present invention and constitute a part of the present application. The exemplary embodiments of the present invention and their descriptions are used to explain the present invention and do not constitute an improper limitation of the present invention. In the attached image:
图1是根据本发明实施例的一种电池温度的调节方法的流程图;1 is a flowchart of a method for adjusting battery temperature according to an embodiment of the present invention;
图2是根据本发明实施例的另一种电池温度的调节方法的流程图;2 is a flowchart of another method for adjusting battery temperature according to an embodiment of the present invention;
图3是根据本发明实施例的一种电池热管理系统的标定结果的示意图;3 is a schematic diagram of a calibration result of a battery thermal management system according to an embodiment of the present invention;
图4是根据本发明实施例的一种电池热管理系统的装置示意图;4 is a schematic diagram of a device of a battery thermal management system according to an embodiment of the present invention;
图5是根据本发明实施例的一种电池温度的调节装置的示意图。FIG. 5 is a schematic diagram of an apparatus for adjusting the temperature of a battery according to an embodiment of the present invention.
具体实施方式Detailed ways
为了使本技术领域的人员更好地理解本发明方案,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分的实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都应当属于本发明保护的范围。In order to make those skilled in the art better understand the solutions of the present invention, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only Embodiments are part of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
需要说明的是,本发明的说明书和权利要求书及上述附图中的术语“第一”、“第二”等是用于区别类似的对象,而不必用于描述特定的顺序或先后次序。应该理解这样使用的数据在适当情况下可以互换,以便这里描述的本发明的实施例能够以除了在这里图示或描述的那些以外的顺序实施。此外,术语“包括”和“具有”以及他们的任何变形,意图在于覆盖不排他的包含,例如,包含了一系列步骤或单元的过程、方法、系统、产品或设备不必限于清楚地列出的那些步骤或单元,而是可包括没有清楚地列出的或对于这些过程、方法、产品或设备固有的其它步骤或单元。It should be noted that the terms "first", "second" and the like in the description and claims of the present invention and the above drawings are used to distinguish similar objects, and are not necessarily used to describe a specific sequence or sequence. It is to be understood that the data so used may be interchanged under appropriate circumstances such that the embodiments of the invention described herein can be practiced in sequences other than those illustrated or described herein. Furthermore, the terms "comprising" and "having" and any variations thereof, are intended to cover non-exclusive inclusion, for example, a process, method, system, product or device comprising a series of steps or units is not necessarily limited to those expressly listed Rather, those steps or units may include other steps or units not expressly listed or inherent to these processes, methods, products or devices.
实施例1Example 1
根据本发明实施例,提供了一种电池温度的调节方法的实施例,需要说明的是,在附图的流程图示出的步骤可以在诸如一组计算机可执行指令的计算机系统中执行,并且,虽然在流程图中示出了逻辑顺序,但是在某些情况下,可以以不同于此处的顺序执行所示出或描述的步骤。According to an embodiment of the present invention, an embodiment of a method for adjusting battery temperature is provided. It should be noted that the steps shown in the flowchart of the accompanying drawings can be executed in a computer system such as a set of computer-executable instructions, and , although a logical order is shown in the flowcharts, in some cases steps shown or described may be performed in an order different from that herein.
图1是根据本发明实施例的一种电池温度的调节方法的流程图,如图1所示的电池温度的调节方法流程图,该方法包括如下步骤:FIG. 1 is a flowchart of a method for adjusting battery temperature according to an embodiment of the present invention. As shown in FIG. 1 , the method for adjusting battery temperature includes the following steps:
步骤S102,获取车辆中电池在当前时刻的状态数据,其中,状态数据用于表征电池在当前时刻充放电过程中的状态。In step S102, state data of the battery in the vehicle at the current moment is acquired, wherein the state data is used to represent the state of the battery during the charging and discharging process at the current moment.
在本发明上述步骤S102提供的技术方案中,获取车辆中用于表征电池在当前时刻充放电过程中的状态的数据,该状态数据可以包括但不限于电池实时电流、电池温度、电池荷电状态(State Of Charge,简称为SOC)、电池性能状态(State Of Health,简称为SOH)等,其中,电池实时电流可以通过I进行表示,电池温度可以通过Tbat进行表示。In the technical solution provided by the above step S102 of the present invention, the data used to characterize the state of the battery during the charging and discharging process at the current moment in the vehicle is obtained, and the state data may include but not limited to the real-time current of the battery, the temperature of the battery, and the state of charge of the battery. (State Of Charge, referred to as SOC), battery performance state (State Of Health, referred to as SOH), etc., where the real-time current of the battery can be represented by I, and the battery temperature can be represented by T bat .
可选地,该实施例可以通过温度传感器获取电池温度;可以通过电流传感器获取电池实时电流;可以通过电池管理系统(Battery Management System,简称为BMS)计算获取当前电池荷电状态、电池性能状态等。Optionally, in this embodiment, the temperature of the battery can be obtained through a temperature sensor; the real-time current of the battery can be obtained through a current sensor; the current state of charge of the battery, the battery performance state, etc. .
举例而言,电池荷电状态也可以称为电池剩余电量,可以用于表示电池使用一段时间或长期搁置未使用后的剩余电量与其完全充电状态下的电量的比值,常用百分数表示,其取值范围可以为0~1,当电池荷电状态为0时,用于表示电池放电完全;当电池荷电状态为1时,用于表示电池完全充满;电池性能状态也可以称为蓄电池容量、电池健康度,可以用于表示电池使用一段时间后性能参数与标称参数的比值,常用百分数表示,比如,新出厂电池为100%,完全报废为0%,电池性能状态可以是电池从满充状态下以一定的倍率放电到截止电压所放出的容量与其对应的标称容量的比值,也可以为电池的极限容量大小。For example, the state of charge of the battery can also be called the remaining battery power, which can be used to represent the ratio of the remaining power of the battery after a period of use or a long period of unused use to the power in the fully charged state, usually expressed as a percentage, and its value The range can be from 0 to 1. When the battery state of charge is 0, it is used to indicate that the battery is fully discharged; when the battery state of charge is 1, it is used to indicate that the battery is fully charged; the battery performance state can also be referred to as battery capacity, battery The health degree can be used to indicate the ratio of the performance parameters to the nominal parameters after the battery has been used for a period of time. It is usually expressed as a percentage. For example, a new factory battery is 100%, and a completely scrapped battery is 0%. The battery performance state can be the battery from a fully charged state The ratio of the capacity released at a certain rate to the cut-off voltage and its corresponding nominal capacity can also be the limit capacity of the battery.
步骤S104,基于状态数据,确定电池的目标换热功率。Step S104, based on the state data, determine the target heat exchange power of the battery.
在本发明上述步骤S104提供的技术方案中,获取电池在当前时刻的状态数据,确定电池的状态数据之后,可以基于获取到的状态数据,确定电池的目标换热功率,该目标换热功率可以用于表征电池所要达到的换热功率的目标值,可以通过Q目换进行表示。In the technical solution provided in the above step S104 of the present invention, the state data of the battery at the current moment is obtained, and after the state data of the battery is determined, the target heat exchange power of the battery can be determined based on the obtained state data, and the target heat exchange power can be The target value used to characterize the heat exchange power to be achieved by the battery can be expressed by Q -exchange .
步骤S106,基于目标换热功率,调节电池的实际换热功率。Step S106, based on the target heat exchange power, adjust the actual heat exchange power of the battery.
在本发明上述步骤S106的技术方案中,获取电池的目标换热功率,在确定目标换热功率之后,可以基于目标换热功率,调节电池的实际换热功率,该实际换热功率可以用于表征电池换热功率的实际值,可以通过Q实换进行表示。In the technical solution of the above step S106 of the present invention, the target heat exchange power of the battery is obtained, and after the target heat exchange power is determined, the actual heat exchange power of the battery can be adjusted based on the target heat exchange power, and the actual heat exchange power can be used for The actual value that characterizes the heat exchange power of the battery can be expressed by Q real exchange .
可选地,对电池实际换热功率的调节过程可以通过热管理系统进行,比如,在热管理系统将电池的实际换热功率调节至目标换热功率的过程中,可以通过调整热管理系统的参数实现。Optionally, the process of adjusting the actual heat exchange power of the battery can be performed through the thermal management system. parameter implementation.
举例而言,可以通过调节换热介质流量与换热介质温度,来控制实际换热功率,从而调节电池在当前时刻后在充放电过程中的温度,其中,调节换热介质流量可以通过q进行表示,换热介质温度可以通过Tq进行表示。For example, the actual heat exchange power can be controlled by adjusting the flow rate of the heat exchange medium and the temperature of the heat exchange medium, so as to adjust the temperature of the battery during the charging and discharging process after the current time, wherein the adjustment of the heat exchange medium flow rate can be performed by q Representation, the heat exchange medium temperature can be represented by T q .
再举例而言,假设电池的实际换热功率与电池温度(Tbat)和换热介质温度(Tq)的温差呈正相关,比如,温差越大,电池的实际换热功率越大,且随着换热介质流量的增大,实际换热功率变化趋于平缓,当换热介质流量达到一定数值后,实际换热功率几乎无变化,则可以通过调节换热介质流量与换热介质温度响应调节复杂度与响应速度时,可以优先考虑调整换热介质流量,当调节换热介质流量不能达到要求时,再通过调节控温装置对换热介质温度进行调整,进而调节电池温度(Tbat)与换热介质温度(Tq)的温差,从而达到基于目标换热功率,调节电池的实际换热功率的目的,其中,电池温度(Tbat)与换热介质温度(Tq)的温差可以通过ΔT进行表示。For another example, it is assumed that the actual heat exchange power of the battery is positively correlated with the temperature difference between the battery temperature (T bat ) and the temperature of the heat exchange medium (T q ). As the flow rate of the heat exchange medium increases, the actual heat exchange power change tends to be gentle. When the flow rate of the heat exchange medium reaches a certain value, the actual heat exchange power hardly changes. By adjusting the flow rate of the heat exchange medium and the temperature response of the heat exchange medium When adjusting the complexity and response speed, you can give priority to adjusting the flow of heat exchange medium. When the flow rate of heat exchange medium cannot meet the requirements, adjust the temperature of heat exchange medium by adjusting the temperature control device, and then adjust the temperature of the battery (T bat ) The temperature difference with the heat exchange medium temperature (T q ), so as to achieve the purpose of adjusting the actual heat exchange power of the battery based on the target heat exchange power, wherein the temperature difference between the battery temperature (T bat ) and the heat exchange medium temperature (T q ) can be It is represented by ΔT.
步骤S108,利用实际换热功率调节电池在当前时刻后在充放电过程中的温度。Step S108, using the actual heat exchange power to adjust the temperature of the battery during the charging and discharging process after the current time.
在本发明上述步骤S108技术方案中,获取电池的目标换热功率,确定目标换热功率之后,根据目标换热功率对电池的实际换热功率进行调节,利用调节后的实际换热功率对电池在当前时刻后在充放电过程中的温度进行控制。In the technical solution of the above step S108 of the present invention, the target heat exchange power of the battery is obtained, and after the target heat exchange power is determined, the actual heat exchange power of the battery is adjusted according to the target heat exchange power, and the adjusted actual heat exchange power is used for the battery. The temperature during charging and discharging is controlled after the current time.
举例而言,热量可以通过热传导从电池传递至换热装置,再通过换热介质热对流从换热装置传递至控温装置,从而完成电池在当前时刻后在充放电过程中的温度的调节过程,其中,换热装置可以为液冷系统的水冷板、风冷系统的风道、直冷系统的直冷板等;换热介质可以为液冷系统冷却液、风冷系统的空气、直冷系统的冷媒等;控温装置可以为液冷系统的Chiller、风冷系统的蒸发器、直冷系统的冷凝器、液冷系统的WPTC加热器、风冷系统的APTC加热器、模组加热膜、模组加热板等。For example, heat can be transferred from the battery to the heat exchange device through heat conduction, and then transferred from the heat exchange device to the temperature control device through the heat convection of the heat exchange medium, so as to complete the process of adjusting the temperature of the battery during the charging and discharging process after the current time. , wherein the heat exchange device can be the water cooling plate of the liquid cooling system, the air duct of the air cooling system, the direct cooling plate of the direct cooling system, etc.; the heat exchange medium can be the cooling liquid of the liquid cooling system, the air of the air cooling system, the direct cooling The refrigerant of the system, etc.; the temperature control device can be the Chiller of the liquid cooling system, the evaporator of the air cooling system, the condenser of the direct cooling system, the WPTC heater of the liquid cooling system, the APTC heater of the air cooling system, and the module heating film. , Module heating plate, etc.
再举例而言,系统通过采样分析模块采集电池数据(可以包括温度、电流、SOC、SOH)、换热介质数据(可以包括温度、流速)、环境温度,对电池数据及换热介质数据进行采集之后,导入控制模块计算电池产热功率、换热功率、换热参数(可以包括换热介质流量、换热介质和电池温差),最后确认需求控制参数(可以包括流量、制冷单元功率)并控制制冷单元、换热介质驱动单元实现调节控制。For another example, the system collects battery data (which may include temperature, current, SOC, SOH), heat exchange medium data (which may include temperature, flow rate), and ambient temperature through the sampling analysis module, and collects battery data and heat exchange medium data. After that, import the control module to calculate the battery heat production power, heat exchange power, and heat exchange parameters (which may include heat exchange medium flow, heat exchange medium and battery temperature difference), and finally confirm the demand control parameters (which may include flow rate, refrigeration unit power) and control The refrigeration unit and the heat exchange medium drive unit realize adjustment control.
本申请上述步骤S102至步骤S108,获取车辆中电池在当前时刻的状态数据,其中,状态数据用于表征电池在当前时刻充放电过程中的状态;基于状态数据,确定电池的目标换热功率;基于目标换热功率,调节电池的实际换热功率;利用实际换热功率调节电池在当前时刻后在充放电过程中的温度,进而实现了提高控制车辆的电池温度的效率的技术效果,解决了控制车辆的电池温度的效率低的技术问题。In the above steps S102 to S108 of the present application, state data of the battery in the vehicle at the current moment is obtained, wherein the state data is used to represent the state of the battery during the charging and discharging process at the current moment; based on the state data, the target heat exchange power of the battery is determined; Based on the target heat exchange power, the actual heat exchange power of the battery is adjusted; the actual heat exchange power is used to adjust the temperature of the battery during the charging and discharging process after the current time, thereby achieving the technical effect of improving the efficiency of controlling the battery temperature of the vehicle, solving the problem of The technical problem of inefficiency in controlling the temperature of the battery of the vehicle.
下面对该实施例的上述方法进行进一步介绍。The above method of this embodiment will be further described below.
作为一种可选的实施例方式,步骤S104,基于状态数据,确定电池的目标换热功率,包括:基于状态数据中的电池温度和状态数据中的电池电流,确定电池的产热功率;基于电池温度、电池所处的环境温度和车辆中的换热介质温度,确定目标系数,其中,目标系数用于表征环境温度和换热介质温度对电池的换热功率影响的程度;基于目标系数和产热功率,确定目标换热功率。As an optional embodiment, in step S104, determining the target heat exchange power of the battery based on the state data, including: determining the heat production power of the battery based on the battery temperature in the state data and the battery current in the state data; The battery temperature, the ambient temperature where the battery is located, and the temperature of the heat exchange medium in the vehicle, determine the target coefficient, where the target coefficient is used to characterize the degree of influence of the ambient temperature and the temperature of the heat exchange medium on the heat exchange power of the battery; based on the target coefficient and Heat production power, determine the target heat exchange power.
在该实施例中,获取电池的状态数据,利用获取到的状态数据中的电池温度与电池电流,确定电池的产热功率;同时,可以基于状态数据中的电池温度、电池所处的环境温度与车辆中的换热介质温度,确定目标系数;基于计算得到的目标系数与产热功率,确定电池的目标换热功率,其中,目标系数可以用于表征环境温度和换热介质温度对电池的换热功率影响的程度;电池产热功率可以用于表征电池放电过程中的产热,可以通过Q产进行表示。In this embodiment, the state data of the battery is obtained, and the battery temperature and battery current in the obtained state data are used to determine the heat generation power of the battery; at the same time, the battery temperature in the state data and the ambient temperature where the battery is located can be determined. Determine the target coefficient with the heat exchange medium temperature in the vehicle; determine the target heat exchange power of the battery based on the calculated target coefficient and heat production power, where the target coefficient can be used to characterize the environmental temperature and the heat exchange medium temperature on the battery. The degree of influence of heat exchange power; the heat generation power of the battery can be used to characterize the heat generation during the discharge process of the battery, which can be expressed by Q production .
可选地,可以通过获取到的电池的状态数据,进行电池产热功率的实时计算,计算方式可以为将电池实时电流(I)的平方值与电池内阻(R)的乘积确定为电池产热功率(Q产),可以用下述公式进行表示:Optionally, the real-time calculation of the heat-producing power of the battery can be performed by using the obtained state data of the battery, and the calculation method can be as follows: Thermal power (Q production ) can be expressed by the following formula:
Q产=I2RQ production = I 2 R
其中,电池内阻可以提前对电芯进行测试,得到在不同电池实时电流、电池温度、电池荷电状态、电池性能状态四项参数下,电阻的对应参数,可以用下述公式进行表示:Among them, the internal resistance of the battery can be tested on the battery in advance, and the corresponding parameters of the resistance can be expressed by the following formula under the four parameters of different battery real-time current, battery temperature, battery state of charge, and battery performance state:
R=f(SOC,Tbat,SOH,I)R=f(SOC, T bat , SOH, I)
可选地,当输入电池实时电流、电池温度、电池荷电状态、电池性能状态四项数值时,利用提前得到的数据关系,可以确定电阻的大小。Optionally, when four numerical values of battery real-time current, battery temperature, battery state of charge, and battery performance state are input, the magnitude of the resistance can be determined by using the data relationship obtained in advance.
作为一种可选的实施例方式,基于电池温度、环境温度和换热介质温度,确定目标系数,包括:基于电池温度和环境温度,确定第一系数,其中,第一系数用于表征环境温度对电池的换热功率影响的程度;基于环境温度和换热介质温度,确定第二系数,其中,第二系数用于表征换热介质温度对电池的换热功率影响的程度;将第一系数和第二系数二者之间的比值,确定为目标系数。As an optional embodiment, determining the target coefficient based on the battery temperature, the ambient temperature and the heat exchange medium temperature includes: determining a first coefficient based on the battery temperature and the ambient temperature, where the first coefficient is used to characterize the ambient temperature The degree of influence on the heat exchange power of the battery; the second coefficient is determined based on the ambient temperature and the temperature of the heat exchange medium, wherein the second coefficient is used to characterize the degree of influence of the temperature of the heat exchange medium on the heat exchange power of the battery; the first coefficient The ratio between the second coefficient and the second coefficient is determined as the target coefficient.
在该实施例中,获取电池的状态数据,根据电池的状态数据,确定电池温度、环境温度与换热介质温度,根据获取到的电池温度与环境温度,确定第一系数,根据获取到的环境温度与换热介质温度,确定第二系数,其中,第一系数可以用于表征环境温度对电池的换热功率影响的程度,也可以称为电池环境系数,可以用α进行表示;第二系数可以用于表征换热介质温度对电池的换热功率影响的程度,可以称为车辆热管理系统的热效率,可以用β进行表示;确定第一系数与第二系数之后,将第一系数与第二系数二者之间的比值,确定为目标系数。In this embodiment, the state data of the battery is obtained, the battery temperature, the ambient temperature and the temperature of the heat exchange medium are determined according to the state data of the battery, the first coefficient is determined according to the obtained battery temperature and the ambient temperature, and the first coefficient is determined according to the obtained environment The temperature and the temperature of the heat exchange medium determine the second coefficient, where the first coefficient can be used to characterize the degree of influence of the ambient temperature on the heat exchange power of the battery, and can also be called the battery environmental coefficient, which can be represented by α; the second coefficient It can be used to characterize the degree to which the temperature of the heat exchange medium affects the heat exchange power of the battery, which can be called the thermal efficiency of the vehicle thermal management system, which can be represented by β; after determining the first coefficient and the second coefficient, the first coefficient and the The ratio between the two coefficients is determined as the target coefficient.
可选地,通过获取到的状态数据中的电池温度、电池所处的环境温度与车辆中的换热介质温度,确定目标系数,可以确定电池的适宜温度区间,其中,电池的适宜温度区间可以用于表征电池可承受的最大温度值,可以通过Tmax进行表示,确定电池的适宜温度区间,将电池温度与电池适宜温度区间相比较,确定第一系数,需要注意的是,比较结果不同对应的第一系数值也不同。Optionally, by determining the target coefficient through the battery temperature in the obtained state data, the ambient temperature where the battery is located, and the temperature of the heat exchange medium in the vehicle, the appropriate temperature range of the battery can be determined, wherein the appropriate temperature range of the battery can be It is used to characterize the maximum temperature value that the battery can withstand, which can be expressed by T max , determine the suitable temperature range of the battery, compare the battery temperature with the suitable temperature range of the battery, and determine the first coefficient. It should be noted that the comparison results are different corresponding to The value of the first coefficient is also different.
可选地,通过比较电池环境温度与电池换热介质温度,获取第二系数,其中,电池环境温度可以用于表征电池所处环境的温度值,可以用Trt进行表示,第二系数可以用β进行表示,需要注意的是,比较结果不同对应的第二系数值也不同。Optionally, the second coefficient is obtained by comparing the battery ambient temperature and the battery heat exchange medium temperature, where the battery ambient temperature can be used to characterize the temperature value of the environment where the battery is located, which can be represented by T rt , and the second coefficient can be expressed by β is represented. It should be noted that the second coefficient values corresponding to different comparison results are also different.
可选地,目标系数可以为第一系数与第二系数的比值,可以通过α/β进行表示。Optionally, the target coefficient may be the ratio of the first coefficient to the second coefficient, which may be represented by α/β.
作为一种可选的实施例方式,基于目标系数和产热功率,确定电池的目标换热功率,包括:将目标系数和产热功率二者之间的乘积,确定为目标换热功率。As an optional embodiment, determining the target heat exchange power of the battery based on the target coefficient and the heat generation power includes: determining the product of the target coefficient and the heat generation power as the target heat exchange power.
在该实施例中,获取电池的目标系数与产热功率,电池的目标换热效率可以为目标系数与电池在放电过程中产热值的乘积,可以通过下述公式进行表示:In this embodiment, the target coefficient and heat production power of the battery are obtained, and the target heat exchange efficiency of the battery can be the product of the target coefficient and the heat production value of the battery during the discharge process, which can be expressed by the following formula:
Q目换=Q产·α/βQ eye change = Q production · α/β
作为一种可选的实施例方式,基于电池温度和环境温度,确定第一系数,包括以下之一:响应于电池温度不小于温度阈值,且电池温度大于环境温度,确定第一系数;响应于电池温度不小于温度阈值,且电池温度等于环境温度,确定第一系数;响应于电池温度不小于温度阈值,且电池温度小于环境温度,确定第一系数。As an optional embodiment, determining the first coefficient based on the battery temperature and the ambient temperature includes one of the following: determining the first coefficient in response to the battery temperature being not less than a temperature threshold and the battery temperature being greater than the ambient temperature; The battery temperature is not less than the temperature threshold and the battery temperature is equal to the ambient temperature, the first coefficient is determined; the first coefficient is determined in response to the battery temperature being not less than the temperature threshold and the battery temperature is less than the ambient temperature.
在该实施例中,获取电池温度与环境温度,对电池温度和环境温度二者之间的大小进行判断,响应于电池温度大于等于温度阈值,且电池温度大于环境温度时,则可以确定第一系数为a1;响应于电池温度大于等于温度阈值,且电池温度等于环境温度时,则可以确定第一系数为a2;响应于电池温度大于等于温度阈值,且电池温度小于环境温度时,则可以确定第一系数为a3,其中,温度阈值可以为根据实际情况设定的值,a1<a2<a3,a1、a2、a3可以为根据实际情况或实验数据确定的值,此处不对a1、a2、a3的大小做具体限制。In this embodiment, the battery temperature and the ambient temperature are obtained, and the magnitude between the battery temperature and the ambient temperature is judged. In response to the battery temperature being greater than or equal to the temperature threshold, and the battery temperature is greater than the ambient temperature, the first The coefficient is a 1 ; when the battery temperature is greater than or equal to the temperature threshold and the battery temperature is equal to the ambient temperature, the first coefficient can be determined to be a 2 ; when the battery temperature is greater than or equal to the temperature threshold and the battery temperature is less than the ambient temperature, then The first coefficient can be determined as a 3 , wherein the temperature threshold can be a value set according to the actual situation, a 1 <a 2 <a 3 , and a 1 , a 2 , and a 3 can be determined according to the actual situation or experimental data value, there is no specific restriction on the size of a 1 , a 2 , and a 3 .
作为一种可选的实施例方式,基于环境温度和换热介质温度,确定第二系数,包括以下之一:响应于换热介质温度大于环境温度,确定第二系数;响应于换热介质温度等于环境温度,确定第二系数;响应于换热介质温度小于环境温度,确定第二系数。As an optional embodiment, determining the second coefficient based on the ambient temperature and the temperature of the heat exchange medium includes one of the following: determining the second coefficient in response to the temperature of the heat exchange medium being greater than the ambient temperature; determining the second coefficient in response to the temperature of the heat exchange medium Equal to the ambient temperature, the second coefficient is determined; in response to the heat exchange medium temperature being less than the ambient temperature, the second coefficient is determined.
在该实施例中,获取环境温度与换热介质温度,对环境温度与换热介质温度二者之间的大小进行判断,响应于换热介质温度大于环境温度时,则可以确定第二系数为b1;响应于换热介质温度等于环境温度时,则可以确定第二系数为b2;响应于换热介质温度小于环境温度时,则可以确定第二系数为b3,b1<b2<b3,b1、b2、b3可以为根据实际情况或实验数据确定的值,此处不对b1、b2、b3的大小做具体限制。In this embodiment, the ambient temperature and the temperature of the heat exchange medium are obtained, and the size between the ambient temperature and the temperature of the heat exchange medium is judged. In response to the temperature of the heat exchange medium being greater than the ambient temperature, the second coefficient can be determined as b 1 ; in response to the temperature of the heat exchange medium being equal to the ambient temperature, the second coefficient can be determined to be b 2 ; in response to the temperature of the heat exchange medium being lower than the ambient temperature, the second coefficient can be determined to be b 3 , b 1 <b 2 <b 3 , b 1 , b 2 , and b 3 may be values determined according to actual conditions or experimental data, and the sizes of b 1 , b 2 , and b 3 are not specifically limited here.
作为一种可选的实施例方式,步骤S106,基于目标换热功率,调节电池的实际换热功率,包括:基于数据库中目标换热功率对应的换热介质流量或换热介质温度,对车辆中换热介质流量或车辆中换热介质温度进行调节;基于调节后的车辆中换热介质流量或车辆中换热介质温度,调节电池的实际换热功率。As an optional embodiment, in step S106, based on the target heat exchange power, adjusting the actual heat exchange power of the battery includes: based on the heat exchange medium flow rate or heat exchange medium temperature corresponding to the target heat exchange power in the database, adjusting the heat exchange medium to the vehicle. The flow rate of the heat exchange medium in the vehicle or the temperature of the heat exchange medium in the vehicle is adjusted; based on the adjusted flow rate of the heat exchange medium in the vehicle or the temperature of the heat exchange medium in the vehicle, the actual heat exchange power of the battery is adjusted.
在该实施例中,获取电池目标换热功率,基于目标换热功率确定目标换热功率所对应的换热介质流量或换热介质温度,基于数据库中的目标换热功率所对应的换热介质流量或换热介质温度,对车辆中的换热介质流量或车辆中的换热介质温度进行调节,基于调节后的车辆中换热介质流量或车辆中换热介质温度,完成对电池实际换热功率的调节。In this embodiment, the target heat exchange power of the battery is obtained, the heat exchange medium flow rate or the heat exchange medium temperature corresponding to the target heat exchange power is determined based on the target heat exchange power, and the heat exchange medium corresponding to the target heat exchange power in the database is determined. Flow or heat exchange medium temperature, adjust the heat exchange medium flow in the vehicle or the heat exchange medium temperature in the vehicle, and complete the actual heat exchange of the battery based on the adjusted heat exchange medium flow in the vehicle or the heat exchange medium temperature in the vehicle Power regulation.
可选地,通过对电池热管理系统的标定工作,得到通过调整热管理系统的参数,从而确定如何调节电池实际换热功率。Optionally, by calibrating the battery thermal management system, parameters of the thermal management system are obtained by adjusting the parameters of the thermal management system, thereby determining how to adjust the actual heat exchange power of the battery.
在电池换热过程中,对流换热系数在风冷或液冷的情况下均为单相强制对流换热,因此对流换热系数的计算方式可以为换热介质速度、特征长度、流体密度、流体动力粘度、导热系数与定压比热容的特定函数关系,其中对流换热系数可以用h进行表示,换热介质速度可以用v进行表示,特征长度可以用l进行表示,流体密度可以用ρ进行表示,流体动力粘度可以用η进行表示,导热系数可以用λ进行表示,定压比热容可以用Cp进行表示,函数关系可以通过下述公式进行表示:In the process of battery heat exchange, the convective heat transfer coefficient is single-phase forced convective heat transfer in the case of air cooling or liquid cooling, so the calculation method of the convective heat transfer coefficient can be the heat transfer medium speed, characteristic length, fluid density, The specific functional relationship between fluid dynamic viscosity, thermal conductivity and constant pressure specific heat capacity, in which the convective heat transfer coefficient can be expressed by h, the heat transfer medium velocity can be expressed by v, the characteristic length can be expressed by l, and the fluid density can be expressed by ρ The fluid dynamic viscosity can be represented by η, the thermal conductivity can be represented by λ, the specific heat capacity at constant pressure can be represented by C p , and the functional relationship can be represented by the following formula:
h=f(v,l,ρ,η,λ,Cp)h=f(v, l, ρ, η, λ, C p )
其中,由于特定结构流道特征长度保持不变,以及同一工作温度范围内特定流体的流体密度、流体动力粘度、导热系数以及定压比热容的变化不大,因此上述公式可以进一步简化,可以通过下述公式进行表示:Among them, since the characteristic length of the flow channel of the specific structure remains unchanged, and the fluid density, hydrodynamic viscosity, thermal conductivity and constant pressure specific heat capacity of the specific fluid within the same working temperature range do not change much, the above formula can be further simplified. The above formula is expressed as:
h=f(v)h=f(v)
因此,实际换热功率可通过Q实换=f(v,ΔT)进行表示,即,可以确认电池在当前时刻的实际换热功率,实际换热功率(Q实换)可以为对流换热系数(h)、换热面积(A)与换热介质和换热面二者之间的温差(ΔT),上述三者的乘积,可以通过下述公式进行表示:Therefore, the actual heat exchange power can be represented by Q actual exchange = f(v, ΔT), that is, the actual heat exchange power of the battery at the current moment can be confirmed, and the actual heat exchange power (Q actual exchange ) can be the convection heat transfer coefficient. (h), the heat exchange area (A) and the temperature difference (ΔT) between the heat exchange medium and the heat exchange surface, the product of the above three can be expressed by the following formula:
Q实换=h·A·ΔTQ real conversion = h·A·ΔT
因此,可以通过确认换热介质流量(q)、换热介质温度(Tq)、电池温度(Tbat)三个变量与实际换热功率(Q实换)之间的关系,来确定对电池的实际换热功率调节的情况,其中,对于特定结构的电池可以只考虑对流换热系数(h)与换热介质和换热面的温差(ΔT)。Therefore, by confirming the relationship between the three variables of heat exchange medium flow (q), heat exchange medium temperature (T q ), battery temperature (T bat ) and the actual heat exchange power (Q actual exchange ) The actual heat exchange power adjustment situation, in which, for a specific structure of the battery, only the convection heat transfer coefficient (h) and the temperature difference (ΔT) between the heat exchange medium and the heat exchange surface can be considered.
可选地,进行电池热管理系统的标定工作可以先搭建电池热管理参数标定台架,其中,标定台架至少可以包括:含有热管理系统的电池包、换热介质回路、制冷单元、换热介质驱动单元、温度监控测试装置、电池包充放电装置以及恒温环境仓等,其中,温度监控测试装置可以包括测试电池温度与换热介质温度。Optionally, to perform the calibration of the battery thermal management system, a battery thermal management parameter calibration bench may be built first, wherein the calibration bench may at least include: a battery pack containing a thermal management system, a heat exchange medium circuit, a refrigeration unit, a heat exchange A medium drive unit, a temperature monitoring and testing device, a battery pack charging and discharging device, a constant temperature environment chamber, etc., wherein the temperature monitoring and testing device may include testing the temperature of the battery and the temperature of the heat exchange medium.
可选地,热管理系统的标定方法可以为:将电池荷电状态调整至50%,并将电池放置于特定温度环境仓进行浸湿,完成条件后电池的平均温度处于环境温度上下浮动0.5℃范围内,其中,特定温度可以用Trt1进行表示;将电池荷电状态调整至50%后,使用恒定倍率电流将电池荷电状态由50%充电至60%,再放电至50%,并持续此循环,同时持续通入特定流量与特定温度的换热介质,并记录每个放电循环过程结束时的电池温度,其中,恒定倍率电流可以用I1进行表示,换热介质的特定流量可以用q1进行表示,换热介质的特定温度可以用Tq1进行表示,每个放电循环结束时的电池温度可以分别用Tbat1、Tbat2、Tbat3……Tbatn进行表示,需要说明的是此处符号表示仅为举例说明,只要可以表示出指定量的符号都可以为本发明实施例可以保护的范围。Optionally, the calibration method of the thermal management system can be as follows: adjust the state of charge of the battery to 50%, place the battery in a specific temperature environment chamber for soaking, and after the conditions are completed, the average temperature of the battery is within the ambient temperature and fluctuates by 0.5°C. range, where a specific temperature can be represented by Trt1; after adjusting the battery state of charge to 50%, use a constant rate current to charge the battery state of charge from 50% to 60%, and then discharge it to 50%, and continue this cycle, while continuously feeding a heat exchange medium with a specific flow rate and a specific temperature, and record the battery temperature at the end of each discharge cycle process. 1 , the specific temperature of the heat exchange medium can be represented by T q1 , and the battery temperature at the end of each discharge cycle can be represented by T bat1 , T bat2 , T bat3 ...... T batn respectively. The symbol representation is only for illustration, and as long as the symbol can represent the specified quantity, it can be within the protection scope of the embodiments of the present invention.
记录出每个放电循环过程结束时的电池温度之后,将某一放电过程结束后的电池温度与上一放电过程结束后的电池温度相比较,当某一放电过程结束后的电池温度与上一放电过程结束后的电池温度的差值小于等于0.2℃时,可以通过Tbatn-Tbat(n-1)≤0.2℃进行表示,此时电池达到热平衡状态,其中,热平衡状态可以为电池的产热功率与换热功率相等,达到热平衡状态后停止充放电循环,记录此时的换热值、换热介质流量、换热介质温度与电池温度。After recording the battery temperature at the end of each discharge cycle, compare the battery temperature after a discharge process with the battery temperature after the previous discharge process. When the difference in battery temperature after the discharge process is less than or equal to 0.2°C, it can be represented by T batn -T bat(n-1) ≤ 0.2°C, and the battery reaches a thermal equilibrium state. The thermal power is equal to the heat exchange power. After reaching the thermal equilibrium state, the charge-discharge cycle is stopped, and the heat exchange value, heat exchange medium flow rate, heat exchange medium temperature and battery temperature are recorded at this time.
在上述过程的基础上,得到换热值、换热介质流量、换热介质温度与电池温度保持充放电倍率保持不变,改变换热介质流量与换热介质温度,重复电池充放电的循环过程以及放电过程结束后的电池温度与上一放点过程结束后的电池温度的比较,得出新的换热功率;改变充放电倍率,重复上述操作,最终完成对热管理系统的标定工作,得出换热介质流量(q)、换热介质温度(Tq)、电池温度(Tbat)三个变量与实际换热功率(Q实换)之间的关系,可以通过下述公式进行表示:On the basis of the above process, the heat exchange value, heat exchange medium flow rate, heat exchange medium temperature and battery temperature are obtained, and the charge-discharge rate remains unchanged. And compare the battery temperature after the discharge process with the battery temperature after the previous discharge process to obtain a new heat exchange power; change the charge and discharge rate, repeat the above operations, and finally complete the calibration of the thermal management system. The relationship between the three variables of the heat exchange medium flow (q), the heat exchange medium temperature (T q ), the battery temperature (T bat ) and the actual heat exchange power (Q actual exchange ) can be expressed by the following formula:
Q实换=f(q,Tq,Tbat)Q real conversion = f(q, T q , T bat )
可选地,由于电池热管理系统中的换热介质温度(Tq)变化较小,因此上述公式可以通过Q实换=f(q,ΔT)进行表示,其中,ΔT可以为电池温度(Tbat)与换热介质温度(Tq)的差值,可以通过Q实换=f[q,(Tq-Tbat)]进行表示,因此,在电池温度(Tbat)保持不变的情况下,可以通过调节换热介质流量(q)与换热介质温度(Tq)控制实际换热功率。Optionally, since the temperature of the heat exchange medium (T q ) in the battery thermal management system changes little, the above formula can be expressed by Q = f(q, ΔT), where ΔT can be the battery temperature (T bat ) and the temperature of the heat exchange medium (T q ), can be expressed by Q real exchange =f[q, (T q -T bat )], therefore, when the battery temperature (T bat ) remains unchanged The actual heat exchange power can be controlled by adjusting the heat exchange medium flow rate (q) and the heat exchange medium temperature (T q ).
该实施例通过实时获取车辆中电池在当前时刻的状态数据,确定出电池的目标换热功率,基于目标换热功率,调节电池的实际换热功率,利用实际换热功率调节电池在当前时刻后在充放电过程中的温度,从而实现了提高控制车辆的电池温度的效率的技术效果,解决了控制车辆的电池温度的效率低的技术问题。In this embodiment, the state data of the battery in the vehicle at the current moment is acquired in real time, the target heat exchange power of the battery is determined, the actual heat exchange power of the battery is adjusted based on the target heat exchange power, and the actual heat exchange power is used to adjust the battery after the current moment. The temperature in the process of charging and discharging, thereby achieving the technical effect of improving the efficiency of controlling the temperature of the battery of the vehicle, and solving the technical problem of low efficiency of controlling the temperature of the battery of the vehicle.
实施例2Example 2
下面结合优选的实施方式对本发明实施例的技术方案进行举例说明。The technical solutions of the embodiments of the present invention are illustrated below with reference to the preferred embodiments.
在车辆行驶中,对于电池热管理的控制是保证电池安全性的重要指标,因此,在对电池热管理的控制中,通过对电池目标换热功率与实际换热功率的计算,利用实际换热功率调节电池在当前时刻后在充放电过程中的温度,实现了对电池热管理的控制,提高了控制车辆电池温度的效率。During vehicle driving, the control of battery thermal management is an important indicator to ensure battery safety. Therefore, in the control of battery thermal management, the actual heat exchange power is calculated by calculating the target heat exchange power and the actual heat exchange power of the battery. The power adjusts the temperature of the battery during the charging and discharging process after the current time, realizes the control of the thermal management of the battery, and improves the efficiency of controlling the temperature of the vehicle battery.
在一种相关技术中,对于车辆电池热管理的控制方法通常以电池温度作为主要控制输入源,但是现有电池电芯的温度传感器都布置在电芯外表面,而热量的传递需要时间,这种以温度作为主要输入源的控制方法具有滞后性,且需要预留较多阈值余量以保证将电池温度控制在适宜区间,会导致能耗的增加,进一步加剧续驶里程焦虑。In a related art, the control method for vehicle battery thermal management usually takes the battery temperature as the main control input source, but the temperature sensors of the existing battery cells are all arranged on the outer surface of the battery cells, and the heat transfer takes time, which requires time. This control method that uses temperature as the main input source has hysteresis, and needs to reserve more threshold margin to ensure that the battery temperature is controlled within a suitable range, which will lead to an increase in energy consumption and further aggravate the anxiety of driving range.
在另一种相关技术中,提出了一种基于干预时间的动力电池热管理方法,该方法对于电池温度调节与否,取决于系统等效对流换热系数h与其前期标定的系统临界换热系数hcr的对比,并需要根据当前工况对未来某一段时间的电池温度进行预测,以确定温度干预模式,但该方法需要对电池的温度进行预测,存在控制精准度低的问题。In another related technology, a power battery thermal management method based on intervention time is proposed. Whether or not the method adjusts the battery temperature depends on the system equivalent convective heat transfer coefficient h and its pre-calibrated system critical heat transfer coefficient Compared with h cr , it is necessary to predict the battery temperature for a certain period of time in the future according to the current working conditions to determine the temperature intervention mode, but this method needs to predict the temperature of the battery, which has the problem of low control accuracy.
在另一种相关技术中,还提出了一种电池热管理控制方法装置介质和设备,该方法根据电池的SOC、当前温度进行产热估算,但该方法未提及进行加热和冷却的功率的具体调节方法,未提及根据换热功率与热管理系统参数如换热介质流量、换热介质与电池温差的关系,也未提及换热功率的概念。In another related art, a battery thermal management control method device medium and device is also proposed. The method estimates heat production according to the SOC and current temperature of the battery, but the method does not mention the power of heating and cooling. The specific adjustment method does not mention the relationship between heat exchange power and thermal management system parameters such as heat exchange medium flow, heat exchange medium and battery temperature difference, nor does it mention the concept of heat exchange power.
在另一种相关技术中,还提出了一种电池热管理的控制方法,该方法利用电池温度、SOH、SOC进行电池预设状态的判断,并提到利用热管理参数调节以调整制冷能力,但该方法只提及用电池温度、SOH、SOC进行电池热管理预设状态的判断,未提及电池产热功率和换热功率的根本关系,因而仍存在调节电池温度周期过长、速度过慢的问题。In another related art, a method for controlling battery thermal management is also proposed. The method uses battery temperature, SOH, and SOC to judge the preset state of the battery, and mentions using thermal management parameter adjustment to adjust the cooling capacity. However, this method only mentions the use of battery temperature, SOH, and SOC to judge the preset state of battery thermal management, and does not mention the fundamental relationship between battery heat production power and heat exchange power. slow problem.
为解决上述问题,本发明实施例提出对电池目标换热功率与实际换热功率的计算,利用实际换热功率调节电池在当前时刻后在充放电过程中的温度,实现了对电池热管理的控制,不需要对电池的温度进行预测,控制更为精准,调整参数为换热介质流量和换热介质温度,是产热的直接影响项,可做到实时快速调节电池温度,提高了控制车辆电池温度的效率。In order to solve the above problem, the embodiment of the present invention proposes the calculation of the target heat exchange power and the actual heat exchange power of the battery, and uses the actual heat exchange power to adjust the temperature of the battery during the charging and discharging process after the current time, so as to realize the thermal management of the battery. Control, does not need to predict the temperature of the battery, the control is more accurate, the adjustment parameters are the heat exchange medium flow and the heat exchange medium temperature, which are the direct influence items of heat production, which can quickly adjust the battery temperature in real time and improve the control of the vehicle. Efficiency over battery temperature.
下面对本发明实施例进行进一步的介绍。The embodiments of the present invention will be further introduced below.
图2是根据本发明实施例的另一种电池温度的调节方法的流程图,如图2所示,另一种电池温度的调节方法包括以下步骤。FIG. 2 is a flowchart of another method for adjusting battery temperature according to an embodiment of the present invention. As shown in FIG. 2 , another method for adjusting battery temperature includes the following steps.
步骤S201,获取电池温度及电池温度阈值并进行比较。In step S201, the battery temperature and the battery temperature threshold are obtained and compared.
在本发明实施例中,获取电池温度与电池温度阈值,并对两者进行比较,其中,电池温度可以用于表征电池的实时温度,可以通过Tbat进行表示,电池温度阈值可以用于表征电池的适宜温度区间,可以为临界温度上限,可以通过Tmax进行表示。In this embodiment of the present invention, the battery temperature and the battery temperature threshold are obtained, and the two are compared, wherein the battery temperature can be used to characterize the real-time temperature of the battery, which can be represented by T bat , and the battery temperature threshold can be used to characterize the battery The suitable temperature range of , can be the upper limit of critical temperature, which can be represented by T max .
可选地,可以通过温度传感器获取电池温度,当电池温度(Tbat)大于等于电池温度阈值(Tmax)时,执行步骤S202,否则继续获取电池温度及电池温度阈值并进行比较,直至满足电池温度大于等于电池温度阈值时,执行步骤S202。Optionally, the battery temperature can be obtained through a temperature sensor, and when the battery temperature (T bat ) is greater than or equal to the battery temperature threshold (T max ), step S202 is performed; otherwise, the battery temperature and the battery temperature threshold are continuously obtained and compared until the battery temperature is satisfied. When the temperature is greater than or equal to the battery temperature threshold, step S202 is executed.
步骤S202,计算电池产热功率。Step S202, calculating the heat generation power of the battery.
在本发明实施例中,当满足电池温度大于等于电池温度阈值时,进行电池产热功率的计算,计算电池产热功率时,获取电池温度、电池荷电状态、电池实时电流以及电池性能状态进行计算,其中,电池实时电流可以用I表示。In the embodiment of the present invention, when the battery temperature is greater than or equal to the battery temperature threshold, the calculation of the battery heat generation power is performed, and when the battery heat generation power is calculated, the battery temperature, the battery state of charge, the battery real-time current and the battery performance state are obtained. Calculation, where the real-time current of the battery can be represented by I.
可选地,可以通过电流传感器获取电池实时电流;可以通过电池管理系统计算获取当前电池荷电状态、电池性能状态。Optionally, the real-time current of the battery can be obtained through a current sensor; the current state of charge of the battery and the battery performance state can be obtained through calculation by the battery management system.
可选地,电池产热可以为电池放电过程中的产热,可以通过Q产进行表示,可以将电池实时电流(I)的平方值与电池内阻(R)的乘积确定为电池产热功率(Q产),可以用下述公式进行表示:Optionally, the heat production of the battery can be the heat production during the discharge process of the battery, which can be represented by Q production , and the product of the square value of the real-time battery current (I) and the battery internal resistance (R) can be determined as the battery heat production power. (Q production ), can be expressed by the following formula:
Q产=I2RQ production = I 2 R
其中,电池内阻可以通过对电芯的测试得到相应关系,通过输入电池实时电流、电池温度、电池荷电状态、电池性能状态四项数值进行获取,可以用下述公式进行表示:Among them, the internal resistance of the battery can be obtained by testing the battery cell to obtain the corresponding relationship, and can be obtained by entering four values of the battery real-time current, battery temperature, battery state of charge, and battery performance state, which can be expressed by the following formula:
R=f(SOC,Tbat,SOH,I)R=f(SOC, T bat , SOH, I)
步骤S203,计算电池换热功率。Step S203, calculating the heat exchange power of the battery.
在该实施例中,完成对电池产热功率的计算之后,进行对电池换热功率的计算,其中,对电池换热功率进行计算时,可以获取环境温度与换热介质温度。其中,环境温度可以用于表征电池所处环境的温度,可以通过Trt进行表示,换热介质温度可以用于表征电池的换热介质温度值,可以通过Tq进行表示。In this embodiment, after the calculation of the heat production power of the battery is completed, the calculation of the heat exchange power of the battery is performed, wherein, when the heat exchange power of the battery is calculated, the ambient temperature and the temperature of the heat exchange medium can be obtained. Among them, the ambient temperature can be used to characterize the temperature of the environment where the battery is located, which can be represented by T rt , and the temperature of the heat exchange medium can be used to characterize the temperature value of the heat exchange medium of the battery, which can be represented by T q .
可选地,进行对电池换热功率的计算,通过环境温度(Trt)与电池温度的比较,从而确定环境系数(α),响应于电池温度大于等于温度阈值,且电池温度大于环境温度时,则可以确定环境系数为a1;响应于电池温度大于等于温度阈值,且电池温度等于环境温度时,则可以确定环境系数为a2;响应于电池温度大于等于温度阈值,且电池温度小于环境温度时,则可以确定环境系数为a3,其中,温度阈值可以为根据实际情况设定的值,a1<a2<a3,a1、a2、a3可以为根据实际情况或实验数据确定的值,此处不对a1、a2、a3的大小做具体限制。Optionally, calculate the heat exchange power of the battery, and determine the environmental coefficient (α) by comparing the ambient temperature (T rt ) with the battery temperature, in response to the battery temperature being greater than or equal to the temperature threshold, and when the battery temperature is greater than the ambient temperature. , the environmental coefficient can be determined to be a 1 ; in response to the battery temperature being greater than or equal to the temperature threshold, and the battery temperature is equal to the ambient temperature, the environmental coefficient can be determined to be a 2 ; in response to the battery temperature being greater than or equal to the temperature threshold, and the battery temperature is less than the ambient temperature At the temperature, the environmental coefficient can be determined as a 3 , wherein the temperature threshold can be a value set according to the actual situation, a 1 <a 2 <a 3 , a 1 , a 2 , a 3 can be based on the actual situation or experiment The value determined by the data, and there is no specific restriction on the size of a 1 , a 2 , and a 3 here.
可选地,确定热管理系统的热效率,可以用β进行表示,确定热管理系统的热效率时,可以对环境温度(Trt)与换热介质温度(Tq)进行比较,响应于换热介质温度大于环境温度时,则可以确定热效率为b1;响应于换热介质温度等于环境温度时,则可以确定热效率为b2;响应于换热介质温度小于环境温度时,则可以确定热效率为b3,b1<b2<b3,b1、b2、b3可以为根据实际情况或实验数据确定的值,此处不对b1、b2、b3的大小做具体限制。Optionally, to determine the thermal efficiency of the thermal management system, it can be represented by β. When determining the thermal efficiency of the thermal management system, the ambient temperature (T rt ) can be compared with the temperature of the heat exchange medium (T q ), in response to the heat exchange medium. When the temperature is greater than the ambient temperature, the thermal efficiency can be determined as b 1 ; when the temperature of the heat exchange medium is equal to the ambient temperature, the thermal efficiency can be determined as b 2 ; when the temperature of the heat exchange medium is less than the ambient temperature, the thermal efficiency can be determined as b 3 , b 1 <b 2 <b 3 , b 1 , b 2 , and b 3 may be values determined according to actual conditions or experimental data, and the sizes of b 1 , b 2 , and b 3 are not specifically limited here.
可选地,确定环境系数与热效率之后,电池的换热功率可以用于表征电池换热功率的目标值,可以通过Q目换进行表示,可以为环境系数与热效率的比值与电池产热功率的乘积,可以通过下述公式进行表示:Optionally, after determining the environmental coefficient and thermal efficiency, the heat exchange power of the battery can be used to characterize the target value of the heat exchange power of the battery, which can be expressed by Q -exchange , which can be the ratio of the ratio of the environmental coefficient to the thermal efficiency and the heat production power of the battery. The product can be expressed by the following formula:
Q目换=Q产·α/βQ eye change = Q production · α/β
步骤S204,使用换热功率进行冷却。Step S204, use heat exchange power for cooling.
在该实施例中,完成对电池产热功率的计算之后,使用换热功率对电池进行冷却,其中,冷却过程可以通过电池热管理系统完成。In this embodiment, after the calculation of the heat generation power of the battery is completed, the heat exchange power is used to cool the battery, wherein the cooling process can be completed by the battery thermal management system.
可选地,将热管理系统对电池的换热功率调节至步骤S203中计算得出的换热功率,可以根据牛顿冷却公式计算电池的实际换热功率,可通过Q实换=h·A·ΔT进行计算,其中,Q实换可以为电池当前的实际换热功率,h可以为对流换热系数,A可以为换热面积,ΔT可以为换热介质和换热面的温差,其中,对于特定结构的电池只需考虑对流换热系数与换热介质和换热面的温差。Optionally, the heat exchange power of the thermal management system to the battery is adjusted to the heat exchange power calculated in step S203, and the actual heat exchange power of the battery can be calculated according to the Newton cooling formula, which can be calculated by Q actual exchange = h·A· ΔT is calculated, where Q actual exchange can be the current actual heat exchange power of the battery, h can be the convective heat transfer coefficient, A can be the heat exchange area, ΔT can be the temperature difference between the heat exchange medium and the heat exchange surface, where, for The specific structure of the battery only needs to consider the convective heat transfer coefficient and the temperature difference between the heat transfer medium and the heat transfer surface.
可选地,由于电池换热过程无论是在风冷或液冷的情况下均为单相强制对流换热,因此h=f(v,l,ρ,η,λ,Cp),其中,h可以为对流换热系数,v可以为换热介质速度,l可以为特征长度,ρ可以为流体密度,η可以为流体动力粘度,λ可以为导热系数,Cp可以为定压比热容,由于特定结构通道特征长度不变,以及同一工作温度范围内特定流体的流体密度、流体动力粘度、导热系数以及定压比热容的变化不大,因此上述公式可以进一步简化,可以通过下述公式进行表示:Optionally, since the heat exchange process of the battery is single-phase forced convection heat exchange whether it is air-cooled or liquid-cooled, h=f(v, l, ρ, η, λ, C p ), where, h can be the convective heat transfer coefficient, v can be the heat transfer medium velocity, l can be the characteristic length, ρ can be the fluid density, η can be the hydrodynamic viscosity, λ can be the thermal conductivity, and C p can be the constant pressure specific heat capacity, since The characteristic length of the channel of a specific structure is unchanged, and the fluid density, hydrodynamic viscosity, thermal conductivity and constant pressure specific heat capacity of a specific fluid within the same working temperature range do not change much. Therefore, the above formula can be further simplified and can be expressed by the following formula:
h=f(v)h=f(v)
因此,实际换热功率可通过Q实换=f(v,ΔT)进行表示。Therefore, the actual heat exchange power can be expressed by Q real exchange = f(v, ΔT).
可选地,对电池实际换热功率的调节过程可以通过热管理系统进行,比如,在热管理系统将电池的实际换热功率调节至目标换热功率的过程中,可以通过调整热管理系统的参数实现。Optionally, the process of adjusting the actual heat exchange power of the battery can be performed through the thermal management system. parameter implementation.
可选地,通过对电池热管理系统的标定工作,得到通过调整热管理系统的参数,从而确定如何调节电池实际换热功率,其中,通过确认换热介质流量(q)、换热介质温度(Tq)、电池温度(Tbat)三个变量与实际换热功率(Q实换)之间的关系,来完成热管理系统的标定工作。Optionally, by calibrating the battery thermal management system, the parameters of the thermal management system can be adjusted to determine how to adjust the actual heat exchange power of the battery. The relationship between the three variables of T q ), battery temperature (T bat ) and the actual heat exchange power (Q actual exchange ) is used to complete the calibration of the thermal management system.
可选地,进行电池热管理系统的标定工作可以先搭建电池热管理参数标定台架,其中,标定台架至少可以包括:含有热管理系统的电池包、换热介质回路、制冷单元、换热介质驱动单元、温度监控测试装置、电池包充放电装置以及恒温环境仓等,其中,温度监控测试装置可以包括测试电池温度与换热介质温度。Optionally, to perform the calibration of the battery thermal management system, a battery thermal management parameter calibration bench may be built first, wherein the calibration bench may at least include: a battery pack containing a thermal management system, a heat exchange medium circuit, a refrigeration unit, a heat exchange A medium drive unit, a temperature monitoring and testing device, a battery pack charging and discharging device, a constant temperature environment chamber, etc., wherein the temperature monitoring and testing device may include testing the temperature of the battery and the temperature of the heat exchange medium.
可选地,热管理系统的标定方法可以为:首先将电池荷电状态调整至50%,并将电池放置于特定温度环境仓进行浸湿,完成条件后电池的平均温度处于环境温度上下浮动0.5℃范围内,其中,特定温度可以用Trt1进行表示;将电池荷电状态调整至50%后,使用恒定倍率电流将电池荷电状态由50%充电至60%,再放电至50%,并持续此循环,同时持续通入特定流量与特定温度的换热介质,并记录每个放电循环过程结束时的电池温度,其中,恒定倍率电流可以用I1进行表示,换热介质的特定流量可以用q1进行表示,换热介质的特定温度可以用Tq1进行表示,每个放电循环结束时的电池温度可以分别用Tbat1、Tbat2、Tbat3……Tbatn进行表示,需要说明的是此处符号表示仅为举例说明,只要可以表示出指定量的符号都可以为本发明实施例可以保护的范围。Optionally, the calibration method of the thermal management system can be as follows: firstly, adjust the state of charge of the battery to 50%, and place the battery in a specific temperature environment chamber for soaking. Within the range of ℃, the specific temperature can be represented by Trt1; after adjusting the battery state of charge to 50%, use a constant rate current to charge the battery state of charge from 50% to 60%, and then discharge it to 50%, and continue During this cycle, a heat exchange medium with a specific flow rate and a specific temperature is continuously fed, and the battery temperature at the end of each discharge cycle process is recorded. The constant rate current can be represented by I 1 , and the specific flow rate of the heat exchange medium can be expressed by q 1 , the specific temperature of the heat exchange medium can be represented by T q1 , and the battery temperature at the end of each discharge cycle can be represented by T bat1 , T bat2 , T bat3 ...... T batn respectively, it should be noted that this The symbols indicated here are only for illustration, and as long as the symbols that can represent the specified quantity can be within the protection scope of the embodiments of the present invention.
可选地,记录出每个放电循环过程结束时的电池温度后,将某一放电过程结束后的电池温度与上一放电过程结束后的电池温度相比较,当某一放电过程结束后的电池温度与上一放电过程结束后的电池温度的差值小于等于0.2℃时,可以通过Tbatn-Tbat(n-1)≤0.2℃进行表示,此时电池达到热平衡状态,其中,热平衡状态可以为电池的产热功率与换热功率相等,达到热平衡状态后停止充放电循环,记录此时的换热值、换热介质流量、换热介质温度与电池温度。Optionally, after recording the battery temperature at the end of each discharge cycle, compare the battery temperature after a certain discharge process with the battery temperature after the previous discharge process. When the difference between the temperature and the battery temperature after the last discharge process is less than or equal to 0.2°C, it can be represented by T batn -T bat(n-1) ≤ 0.2°C. At this time, the battery reaches a thermal equilibrium state, where the thermal equilibrium state can be The heat generation power of the battery is equal to the heat exchange power. After reaching the thermal equilibrium state, the charge and discharge cycle is stopped, and the heat exchange value, heat exchange medium flow rate, heat exchange medium temperature and battery temperature are recorded at this time.
可选地,得到换热值、换热介质流量、换热介质温度与电池温度之后,保持充放电倍率保持不变,改变换热介质流量与换热介质温度,重复电池充放电的循环过程以及放电过程结束后的电池温度与上一放点过程结束后的电池温度的比较,得出新的换热功率;改变充放电倍率,重复上述操作,最终完成对热管理系统的标定工作,得出换热介质流量(q)、换热介质温度(Tq)、电池温度(Tbat)三个变量与实际换热功率(Q实换)之间的关系,可以通过下述公式进行表示:Optionally, after obtaining the heat exchange value, heat exchange medium flow rate, heat exchange medium temperature and battery temperature, keep the charge and discharge rate unchanged, change the heat exchange medium flow rate and heat exchange medium temperature, repeat the cycle process of battery charge and discharge, and Compare the battery temperature after the discharge process with the battery temperature after the last discharge process to obtain the new heat exchange power; change the charge and discharge rate, repeat the above operations, and finally complete the calibration of the thermal management system, get The relationship between the three variables of heat exchange medium flow (q), heat exchange medium temperature (T q ), battery temperature (T bat ) and the actual heat exchange power (Q actual exchange ) can be expressed by the following formula:
Q实换=f(q,Tq,,Tbat)Q real conversion =f(q, T q ,, T bat )
可选地,由于电池热管理系统中的换热介质温度(Tq)变化较小,因此上述公式可以通过Q实换=f(q,ΔT)进行表示,其中,ΔT可以为电池温度(Tbat)与换热介质温度(Tq)的差值,可以通过Q实换=f[q,(Tq-Tbat)]进行表示,因此,在电池温度(Tbat)保持不变的情况下,可以通过调节换热介质流量(q)与换热介质温度(Tq)控制实际换热功率。Optionally, since the temperature of the heat exchange medium (T q ) in the battery thermal management system changes little, the above formula can be expressed by Q = f(q, ΔT), where ΔT can be the battery temperature (T bat ) and the temperature of the heat exchange medium (T q ), can be expressed by Q real exchange =f[q, (T q -T bat )], therefore, when the battery temperature (T bat ) remains unchanged The actual heat exchange power can be controlled by adjusting the heat exchange medium flow rate (q) and the heat exchange medium temperature (T q ).
举例而言,图3是根据本发明实施例的一种电池热管理系统的标定结果的示意图,如图3所示,换热功率(Q换)与温差(ΔT)呈线性关系,ΔT随着Q换的增加而增加,同时,Q换随着换热介质流量(q)的增大变化趋缓,当换热介质流量(q)达到一定数值后,继续增加换热介质流量(q)对Q换的增加影响减小。For example, FIG. 3 is a schematic diagram of a calibration result of a battery thermal management system according to an embodiment of the present invention. As shown in FIG. 3 , the heat exchange power (Q exchange ) has a linear relationship with the temperature difference (ΔT), and ΔT increases with the The Q exchange increases with the increase of the heat exchange medium. At the same time, the Q exchange changes slowly with the increase of the heat exchange medium flow rate (q). When the heat exchange medium flow rate (q) reaches a certain value, continue to increase the heat exchange medium flow rate (q). The increased effect of Q- swap decreases.
可选地,通过调节换热介质流量与换热介质温度响应调节复杂度与响应速度时,优先考虑调整换热介质流量,当调节换热介质流量不能达到要求时,再通过调节控温装置对换热介质温度进行调整,进而调节电池温度(Tbat)与换热介质温度(Tq)的温差ΔT。Optionally, when adjusting the complexity and response speed by adjusting the heat exchange medium flow rate and the heat exchange medium temperature, priority is given to adjusting the heat exchange medium flow rate. The temperature of the heat exchange medium is adjusted, thereby adjusting the temperature difference ΔT between the battery temperature (T bat ) and the temperature of the heat exchange medium (T q ).
可选地,图4是根据本发明实施例的一种电池热管理系统的装置示意图,如图4所示,实现控制冷却方法的必要系统可以包括:与电池401进行直接热量交换的换热装置402,其中,换热装置402可以为将一种流体的热量传给另一种流体的装置,可以为液冷系统的水冷板、风冷系统的风道、直冷系统的直冷板等;换热介质驱动单元403,其中,换热介质驱动单元403可以为液冷系统冷却液、风冷系统的空气、直冷系统的冷媒等;给换热介质调节温度的换热装置404,其中,换热装置404可以为液冷系统的Chiller、风冷系统的蒸发器、直冷系统的冷凝器、液冷系统的WPTC加热器、风冷系统的APTC加热器、模组加热膜、模组加热板等;能够采集必要数据的采样分析模块405,其中,采样分析模块405可以为芯片;能够执行控制逻辑的控制模块406,其中,控制模块406可以为芯片,可以包括电池产热模块407、换热功率计算模块408以及换热参数调节模块409。Optionally, FIG. 4 is a schematic device diagram of a battery thermal management system according to an embodiment of the present invention. As shown in FIG. 4 , a necessary system for implementing the control cooling method may include: a heat exchange device for direct heat exchange with the battery 401 402, wherein, the heat exchange device 402 can be a device that transfers the heat of one fluid to another fluid, and can be a water cooling plate of a liquid cooling system, an air duct of an air cooling system, a direct cooling plate of a direct cooling system, etc.; The heat exchange medium drive unit 403, wherein the heat exchange medium drive unit 403 can be the cooling liquid of the liquid cooling system, the air of the air cooling system, the refrigerant of the direct cooling system, etc.; the heat exchange device 404 for adjusting the temperature of the heat exchange medium, wherein, The heat exchange device 404 can be the Chiller of the liquid cooling system, the evaporator of the air cooling system, the condenser of the direct cooling system, the WPTC heater of the liquid cooling system, the APTC heater of the air cooling system, the module heating film, the module heating A sampling and analysis module 405 capable of collecting necessary data, wherein the sampling and analysis module 405 may be a chip; a control module 406 capable of executing control logic, wherein the control module 406 may be a chip, and may include a battery heat generating module 407, a heat exchanger Thermal power calculation module 408 and heat exchange parameter adjustment module 409 .
可选地,热量通过热传导从电池传递到换热装置402,再通过换热介质热对流从换热装置传递到换热装置404。Optionally, heat is transferred from the battery to the
可选地,系统通过采样分析模块405采集电池数据(可以包括温度、电流、SOC、SOH)、换热介质数据(可以包括温度、流速)、环境温度,导入控制模块406计算电池产热功率、换热功率、换热参数(可以包括换热介质流量、换热介质和电池温差),最终确认需求控制参数(可以包括流量、制冷单元功率)并控制制冷单元、换热介质驱动单元403实现冷却控制。Optionally, the system collects battery data (may include temperature, current, SOC, SOH), heat exchange medium data (may include temperature, flow rate), and ambient temperature through the sampling analysis module 405, and import the
该实施例通过实时获取车辆中电池在当前时刻的状态数据,确定出电池的目标换热功率,基于目标换热功率,调节电池的实际换热功率,利用实际换热功率调节电池在当前时刻后在充放电过程中的温度,从而实现了提高控制车辆的电池温度的效率的技术效果,解决了控制车辆的电池温度的效率低的技术问题。In this embodiment, the state data of the battery in the vehicle at the current moment is acquired in real time, the target heat exchange power of the battery is determined, the actual heat exchange power of the battery is adjusted based on the target heat exchange power, and the actual heat exchange power is used to adjust the battery after the current moment. The temperature in the process of charging and discharging, thereby achieving the technical effect of improving the efficiency of controlling the temperature of the battery of the vehicle, and solving the technical problem of low efficiency of controlling the temperature of the battery of the vehicle.
实施例3Example 3
根据本发明实施例,还提供了一种电池温度的调节装置。需要说明的是,该电池温度的调节装置可以用于执行实施例1中的电池温度的调节方法。According to an embodiment of the present invention, a battery temperature adjustment device is also provided. It should be noted that the device for adjusting battery temperature can be used to implement the method for adjusting battery temperature in Embodiment 1.
图5是根据本发明实施例的一种电池温度的调节装置的示意图。如图5所示,该电池温度的调节装置500可以包括:获取单元502、确定单元504、第一调节单元506和第二调节单元508。FIG. 5 is a schematic diagram of an apparatus for adjusting the temperature of a battery according to an embodiment of the present invention. As shown in FIG. 5 , the battery temperature adjustment device 500 may include: an acquisition unit 502 , a determination unit 504 , a first adjustment unit 506 and a second adjustment unit 508 .
获取单元502,用于获取车辆中电池在当前时刻的状态数据,其中,状态数据用于表征电池在当前时刻充放电过程中的状态;The obtaining unit 502 is configured to obtain the state data of the battery in the vehicle at the current moment, wherein the state data is used to represent the state of the battery during the charging and discharging process at the current moment;
确定单元504,用于基于状态数据,确定电池的目标换热功率;a determining unit 504, configured to determine the target heat exchange power of the battery based on the state data;
第一调节单元506,用于基于目标换热功率,调节电池的实际换热功率;a first adjustment unit 506, configured to adjust the actual heat exchange power of the battery based on the target heat exchange power;
第二调节单元508,用于利用实际换热功率调节电池在当前时刻后在充放电过程中的温度。The second adjusting unit 508 is configured to use the actual heat exchange power to adjust the temperature of the battery during the charging and discharging process after the current time.
可选地,确定单元504包括:第一确定模块,用于基于状态数据中的电池温度和状态数据中的电池电流,确定电池的产热功率;第二确定模块,用于基于电池温度、电池所处的环境温度和车辆中的换热介质温度,确定目标系数,其中,目标系数用于表征环境温度和换热介质温度对电池的换热功率影响的程度;第三确定模块,用于基于目标系数和产热功率,确定目标换热功率。Optionally, the determining unit 504 includes: a first determining module for determining the heat production power of the battery based on the battery temperature in the state data and the battery current in the state data; a second determining module for determining the heat-producing power of the battery based on the battery temperature, The ambient temperature and the temperature of the heat exchange medium in the vehicle are used to determine the target coefficient, wherein the target coefficient is used to characterize the degree of the influence of the ambient temperature and the temperature of the heat exchange medium on the heat exchange power of the battery; the third determination module is used based on The target coefficient and heat production power determine the target heat exchange power.
可选地,第二确定模块包括:第一确定子模块,用于基于电池温度和环境温度,确定第一系数,其中,第一系数用于表征环境温度对电池的换热功率影响的程度;第二确定子模块,用于基于环境温度和换热介质温度,确定第二系数,其中,第二系数用于表征换热介质温度对电池的换热功率影响的程度;第三确定子模块,用于将第一系数和第二系数二者之间的比值,确定为目标系数。Optionally, the second determination module includes: a first determination sub-module, configured to determine a first coefficient based on the battery temperature and the ambient temperature, where the first coefficient is used to represent the degree of influence of the ambient temperature on the heat exchange power of the battery; The second determination submodule is used for determining a second coefficient based on the ambient temperature and the temperature of the heat exchange medium, wherein the second coefficient is used to represent the degree of influence of the temperature of the heat exchange medium on the heat exchange power of the battery; the third determination submodule, Used to determine the ratio between the first coefficient and the second coefficient as the target coefficient.
可选地,第三确定模块包括:第四确定子模块,用于将目标系数和产热功率二者之间的乘积,确定为目标换热功率。Optionally, the third determination module includes: a fourth determination sub-module, configured to determine the product between the target coefficient and the heat generation power as the target heat exchange power.
可选地,第一确定子模块包括以下之一:用于响应电池温度不小于温度阈值,且电池温度大于环境温度;或响应电池温度不小于温度阈值,且电池温度等于环境温度;或响应电池温度不小于温度阈值,且电池温度小于环境温度,对第一系数进行确定。Optionally, the first determination sub-module includes one of the following: for responding that the battery temperature is not less than the temperature threshold, and the battery temperature is greater than the ambient temperature; or responding that the battery temperature is not less than the temperature threshold, and the battery temperature is equal to the ambient temperature; or responding to the battery temperature When the temperature is not less than the temperature threshold, and the battery temperature is less than the ambient temperature, the first coefficient is determined.
可选地,第二确定子模块包括以下之一:用于响应换热介质温度大于环境温度;或响应换热介质温度等于环境温度;或响应换热介质温度小于环境温度,对第二系数进行确定。Optionally, the second determination sub-module includes one of the following: in response to the temperature of the heat exchange medium being greater than the ambient temperature; or in response to the temperature of the heat exchange medium being equal to the ambient temperature; or in response to the temperature of the heat exchange medium being smaller than the ambient temperature, performing the second coefficient calculation. Sure.
可选地,第一调节单元506包括:第一调节模块,用于基于数据库中目标换热功率对应的换热介质流量或换热介质温度,对车辆中换热介质流量或车辆中换热介质温度进行调节;第二调节模块,用于基于调节后的车辆中换热介质流量或车辆中换热介质温度,调节电池的实际换热功率。Optionally, the first adjustment unit 506 includes: a first adjustment module, configured to adjust the flow rate of the heat exchange medium in the vehicle or the heat exchange medium in the vehicle based on the flow rate of the heat exchange medium or the temperature of the heat exchange medium corresponding to the target heat exchange power in the database. The temperature is adjusted; the second adjustment module is used to adjust the actual heat exchange power of the battery based on the adjusted flow rate of the heat exchange medium in the vehicle or the temperature of the heat exchange medium in the vehicle.
在本发明实施例中,通过获取单元,获取车辆中电池在当前时刻的状态数据;通过确定单元,基于状态数据,确定电池的目标换热功率;通过第一调节单元,基于目标换热功率,调节电池的实际换热功率;通过第二调节单元,利用实际换热功率调节电池在当前时刻后在充放电过程中的温度。也就是说,本发明通过实时获取车辆中电池在当前时刻的状态数据,确定出电池的目标换热功率,基于目标换热功率,调节电池的实际换热功率,利用实际换热功率调节电池在当前时刻后在充放电过程中的温度,从而实现了提高控制车辆的电池温度的效率的技术效果,解决了控制车辆的电池温度的效率低的技术问题。In the embodiment of the present invention, the state data of the battery in the vehicle at the current moment is obtained by the obtaining unit; the target heat exchange power of the battery is determined based on the state data by the determining unit; Adjust the actual heat exchange power of the battery; through the second adjustment unit, use the actual heat exchange power to adjust the temperature of the battery during the charging and discharging process after the current moment. That is to say, the present invention determines the target heat exchange power of the battery by acquiring the state data of the battery in the vehicle at the current moment in real time, adjusts the actual heat exchange power of the battery based on the target heat exchange power, and uses the actual heat exchange power to adjust the The temperature during the charging and discharging process after the current time, thereby achieving the technical effect of improving the efficiency of controlling the battery temperature of the vehicle, and solving the technical problem of low efficiency in controlling the battery temperature of the vehicle.
实施例4Example 4
根据本发明实施例,还提供了一种计算机可读存储介质,该存储介质包括存储的程序,其中,所述程序执行实施例1中的电池温度的调节方法。According to an embodiment of the present invention, a computer-readable storage medium is further provided, and the storage medium includes a stored program, wherein the program executes the method for adjusting the battery temperature in the first embodiment.
实施例5Example 5
根据本发明实施例,还提供了一种处理器,该处理器用于运行程序,其中,所述程序运行时执行实施例1中的电池温度的调节方法。According to an embodiment of the present invention, there is also provided a processor for running a program, wherein the method for adjusting the battery temperature in Embodiment 1 is executed when the program is running.
实施例6Example 6
根据本发明实施例,还提供了一种车辆,该车辆用于执行实施例1中的电池温度的调节方法。According to an embodiment of the present invention, there is also provided a vehicle for implementing the method for adjusting the battery temperature in the first embodiment.
上述本发明实施例序号仅仅为了描述,不代表实施例的优劣。The above-mentioned serial numbers of the embodiments of the present invention are only for description, and do not represent the advantages or disadvantages of the embodiments.
在本发明的上述实施例中,对各个实施例的描述都各有侧重,某个实施例中没有详述的部分,可以参见其他实施例的相关描述。In the above-mentioned embodiments of the present invention, the description of each embodiment has its own emphasis. For parts that are not described in detail in a certain embodiment, reference may be made to related descriptions of other embodiments.
在本申请所提供的几个实施例中,应该理解到,所揭露的技术内容,可通过其它的方式实现。其中,以上所描述的装置实施例仅仅是示意性的,例如所述单元的划分,可以为一种逻辑功能划分,实际实现时可以有另外的划分方式,例如多个单元或组件可以结合或者可以集成到另一个系统,或一些特征可以忽略,或不执行。另一点,所显示或讨论的相互之间的耦合或直接耦合或通信连接可以是通过一些接口,单元或模块的间接耦合或通信连接,可以是电性或其它的形式。In the several embodiments provided in this application, it should be understood that the disclosed technical content can be implemented in other ways. The device embodiments described above are only illustrative, for example, the division of the units may be a logical function division, and there may be other division methods in actual implementation, for example, multiple units or components may be combined or Integration into another system, or some features can be ignored, or not implemented. On the other hand, the shown or discussed mutual coupling or direct coupling or communication connection may be through some interfaces, indirect coupling or communication connection of units or modules, and may be in electrical or other forms.
所述作为分离部件说明的单元可以是或者也可以不是物理上分开的,作为单元显示的部件可以是或者也可以不是物理单元,即可以位于一个地方,或者也可以分布到多个单元上。可以根据实际的需要选择其中的部分或者全部单元来实现本实施例方案的目的。The units described as separate components may or may not be physically separated, and components shown as units may or may not be physical units, that is, may be located in one place, or may be distributed to multiple units. Some or all of the units may be selected according to actual needs to achieve the purpose of the solution in this embodiment.
另外,在本发明各个实施例中的各功能单元可以集成在一个处理单元中,也可以是各个单元单独物理存在,也可以两个或两个以上单元集成在一个单元中。上述集成的单元既可以采用硬件的形式实现,也可以采用软件功能单元的形式实现。In addition, each functional unit in each embodiment of the present invention may be integrated into one processing unit, or each unit may exist physically alone, or two or more units may be integrated into one unit. The above-mentioned integrated units may be implemented in the form of hardware, or may be implemented in the form of software functional units.
所述集成的单元如果以软件功能单元的形式实现并作为独立的产品销售或使用时,可以存储在一个计算机可读取存储介质中。基于这样的理解,本发明的技术方案本质上或者说对现有技术做出贡献的部分或者该技术方案的全部或部分可以以软件产品的形式体现出来,该计算机软件产品存储在一个存储介质中,包括若干指令用以使得一台计算机设备(可为个人计算机、服务器或者网络设备等)执行本发明各个实施例所述方法的全部或部分步骤。而前述的存储介质包括:U盘、只读存储器(ROM,Read-Only Memory)、随机存取存储器(RAM,Random Access Memory)、移动硬盘、磁碟或者光盘等各种可以存储程序代码的介质。The integrated unit, if implemented in the form of a software functional unit and sold or used as an independent product, may be stored in a computer-readable storage medium. Based on this understanding, the technical solution of the present invention is essentially or the part that contributes to the prior art, or all or part of the technical solution can be embodied in the form of a software product, and the computer software product is stored in a storage medium , including several instructions for causing a computer device (which may be a personal computer, a server, or a network device, etc.) to execute all or part of the steps of the methods described in the various embodiments of the present invention. The aforementioned storage medium includes: U disk, read-only memory (ROM, Read-Only Memory), random access memory (RAM, Random Access Memory), mobile hard disk, magnetic disk or optical disk and other media that can store program codes .
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above are only the preferred embodiments of the present invention. It should be pointed out that for those skilled in the art, without departing from the principles of the present invention, several improvements and modifications can be made. It should be regarded as the protection scope of the present invention.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116087798A (en) * | 2023-04-03 | 2023-05-09 | 中北润良新能源(济宁)股份有限公司 | Power battery detection method |
GB2626128A (en) * | 2023-01-03 | 2024-07-17 | Perkins Engines Co Ltd | A method of thermal management of a battery |
CN119104919A (en) * | 2024-11-06 | 2024-12-10 | 浙江晶科储能有限公司 | Temperature prediction method, electronic device, storage medium and energy storage system |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120176082A1 (en) * | 2010-01-28 | 2012-07-12 | Lg Chem, Ltd. | Battery pack system of improving operating performance using internal resistance of cell |
CN108172930A (en) * | 2017-12-26 | 2018-06-15 | 智车优行科技(上海)有限公司 | battery pack cooling control method, device and battery pack |
CN109599606A (en) * | 2017-09-30 | 2019-04-09 | 比亚迪股份有限公司 | The temperature control method and humidity control system of on-vehicle battery |
CN112060976A (en) * | 2020-09-16 | 2020-12-11 | 广州小鹏汽车科技有限公司 | Heating method and device for vehicle power battery and vehicle |
CN113859049A (en) * | 2021-09-07 | 2021-12-31 | 恒大新能源汽车投资控股集团有限公司 | Battery thermal management method and device, electronic equipment and computer readable storage medium |
-
2022
- 2022-05-27 CN CN202210590758.XA patent/CN114927803A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120176082A1 (en) * | 2010-01-28 | 2012-07-12 | Lg Chem, Ltd. | Battery pack system of improving operating performance using internal resistance of cell |
CN109599606A (en) * | 2017-09-30 | 2019-04-09 | 比亚迪股份有限公司 | The temperature control method and humidity control system of on-vehicle battery |
CN108172930A (en) * | 2017-12-26 | 2018-06-15 | 智车优行科技(上海)有限公司 | battery pack cooling control method, device and battery pack |
CN112060976A (en) * | 2020-09-16 | 2020-12-11 | 广州小鹏汽车科技有限公司 | Heating method and device for vehicle power battery and vehicle |
CN113859049A (en) * | 2021-09-07 | 2021-12-31 | 恒大新能源汽车投资控股集团有限公司 | Battery thermal management method and device, electronic equipment and computer readable storage medium |
Non-Patent Citations (1)
Title |
---|
张浩;罗志民;宋韩龙;张福增;: "电动车动力锂离子电池水冷系统研究", 汽车实用技术, no. 06, 30 March 2017 (2017-03-30) * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2626128A (en) * | 2023-01-03 | 2024-07-17 | Perkins Engines Co Ltd | A method of thermal management of a battery |
CN116087798A (en) * | 2023-04-03 | 2023-05-09 | 中北润良新能源(济宁)股份有限公司 | Power battery detection method |
CN116087798B (en) * | 2023-04-03 | 2023-07-18 | 中北润良新能源(济宁)股份有限公司 | A kind of detection method of power battery |
CN119104919A (en) * | 2024-11-06 | 2024-12-10 | 浙江晶科储能有限公司 | Temperature prediction method, electronic device, storage medium and energy storage system |
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