CN117905571A

CN117905571A - Monitoring method applied to cooling system

Info

Publication number: CN117905571A
Application number: CN202410067102.9A
Authority: CN
Inventors: 林承伯; 董春艳; 郭佳倩; 李子清; 何炎迎; 吴广权
Original assignee: Guangzhou Automobile Group Co Ltd
Current assignee: Guangzhou Automobile Group Co Ltd
Priority date: 2024-01-16
Filing date: 2024-01-16
Publication date: 2024-04-19

Abstract

An embodiment of the present application provides a monitoring method applied to a cooling system, the method including: acquiring a new heat increment value and a current gas pressure value corresponding to an expansion water tank in a cooling system; determining the liquid level of the cooling liquid corresponding to the expansion water tank based on the newly increased heat value and the current gas pressure value; and if the liquid level of the cooling liquid does not exceed the liquid level threshold value preset by the expansion water tank, sending an alarm signal for representing the leakage of the cooling liquid in the cooling system. According to the technical scheme provided by the embodiment of the application, whether the cooling liquid in the cooling system leaks or not can be confirmed through the newly increased heat value and the current gas pressure value, and an operator can be timely informed after the cooling liquid in the cooling system leaks, so that the operator can conveniently further process the cooling liquid, and safety accidents caused by the fact that the content of the cooling liquid in the cooling system is too low are avoided.

Description

Monitoring method applied to cooling system

Technical Field

The application relates to the technical field of cooling system monitoring, in particular to a monitoring method applied to a cooling system.

Background

With the continuous development of technology, cooling of heat generating components by using a cooling system containing a cooling liquid has been a cooling method often used by developers. In the related art, the cooling system cools the heat emitted by the heat-generating component in the working state by driving the cooling liquid in the cooling system, so that the heat-generating component maintains a better working state. However, once the coolant in the cooling system leaks, heat emitted by the heat generating component may not be completely transferred to the heat dissipating component for cooling through the coolant, so that the heat generating component works in an overheated state, and thus, an extremely high safety risk is brought to an operator. Therefore, how to monitor whether the coolant in the cooling system leaks or not is a problem to be solved.

Disclosure of Invention

To solve the above technical problems, embodiments of the present application provide a monitoring method and apparatus applied to a cooling system, a computer readable storage medium, and an electronic device.

According to an aspect of an embodiment of the present application, there is provided a monitoring method applied to a cooling system, including: acquiring a new heat increment value and a current gas pressure value corresponding to an expansion water tank in a cooling system; determining the liquid level of the cooling liquid corresponding to the expansion water tank based on the new heat increment value and the current gas pressure value; and if the liquid level of the cooling liquid does not exceed the preset liquid level threshold of the expansion water tank, sending an alarm signal for representing the leakage of the cooling liquid in the cooling system.

According to an aspect of an embodiment of the present application, there is provided a monitoring device applied to a cooling system, including: the acquisition module is configured to acquire a new heat increment value and a current gas pressure value corresponding to the expansion water tank in the cooling system; the calculation module is configured to determine the liquid level of the cooling liquid corresponding to the expansion water tank based on the new heat increment value and the current gas pressure value; and the leakage judging module is configured to send out an alarm signal for representing the leakage of the cooling liquid in the cooling system if the liquid level of the cooling liquid does not exceed the liquid level threshold value preset by the expansion water tank.

In some embodiments of the present application, based on the foregoing aspect, the cooling system includes a heat generating component and a heat dissipating component, the expansion tank includes a first water inlet communicating with a branch port of the heat generating component and a second water inlet communicating with a branch port of the heat dissipating component, and the obtaining module is further configured to: respectively obtaining the flow rate of the cooling liquid branch and the temperature value of the cooling liquid branch, which correspond to the first water inlet and the second water inlet respectively; acquiring a cooling liquid discharge temperature value of the expansion water tank; and calculating the new heat increment value according to the cooling liquid branch flow and the cooling liquid branch temperature value which are respectively corresponding to the first water inlet and the second water inlet and the cooling liquid discharge temperature value.

In some embodiments of the application, based on the foregoing, the cooling system includes an adjusting component for controlling the flow of the cooling liquid, and the acquisition module is further configured to: respectively determining the cooling liquid inflow amount corresponding to each of the heating component and the heat dissipation component based on the cooling liquid flow adjustment parameters of the adjustment component; acquiring the branch discharge flow ratio corresponding to each of the heating component and the heat dissipation component; the bypass discharge flow ratio represents the ratio of the cooling liquid to be discharged to the expansion water tank in the cooling liquid inflow; and calculating the cooling liquid branch flow corresponding to each of the first water inlet and the second water inlet according to the cooling liquid inflow and branch discharge flow ratio corresponding to each of the heating component and the heat radiating component.

In some embodiments of the application, based on the foregoing scheme, the acquisition module is further configured to: determining the theoretical inflow of the cooling liquid corresponding to each of the heating component and the heat dissipation component based on the cooling liquid flow regulation parameters; acquiring a water inlet correction coefficient corresponding to the heating component at the current heating temperature; and calculating the cooling liquid inflow rate corresponding to each of the heating component and the heat dissipation component according to the theoretical inflow rate of the cooling liquid corresponding to each of the heating component and the heat dissipation component and the inflow correction coefficient.

In some embodiments of the application, based on the foregoing, the heat generating component includes a plurality of heat generating units, and the acquisition module is further configured to: acquiring a cooling liquid discharge temperature value and a cooling liquid water inlet proportion corresponding to each heating unit; wherein, the cooling liquid water inlet proportion represents the ratio of the cooling liquid water inlet quantity of the heating unit in the total cooling liquid circulation quantity of the cooling system; calculating the comprehensive heating temperature according to the cooling liquid discharge temperature value and the cooling liquid water inlet proportion corresponding to each heating unit; and determining the water inlet correction coefficient by taking the comprehensive heating temperature as the current heating temperature of the heating component.

In some embodiments of the application, based on the foregoing scheme, the acquisition module is further configured to: the step of respectively obtaining the coolant branch flow and the coolant branch temperature value corresponding to the first water inlet and the second water inlet, includes: respectively acquiring discharge length information, a cooling liquid inlet temperature value and a cooling liquid discharge temperature value corresponding to the heating component and the radiating component; wherein the discharge length information comprises a discharge distance from a water inlet to a branch port and a discharge distance from the water inlet to the discharge port, which are respectively corresponding to the heating component and the heat dissipation component; and calculating the cooling liquid branch temperature values corresponding to the first water inlet and the second water inlet according to the discharge length information, the cooling liquid inlet temperature value and the cooling liquid discharge temperature value corresponding to the heating component and the heat radiating component respectively.

In some embodiments of the application, based on the foregoing, the monitoring device applied to the cooling system further comprises a leakage safety module configured to: after the cooling liquid level corresponding to the expansion water tank is determined based on the new heat increment value and the current gas pressure value, starting timing when the cooling liquid level is between the liquid level threshold and a safety liquid level threshold preset by the expansion water tank, and calculating a liquid level deviation value of the expansion water tank if the timing duration reaches a preset duration; and if the liquid level deviation value exceeds a preset safety threshold, sending out the alarm signal.

In some embodiments of the application, based on the foregoing, the leakage security module is further configured to: circularly executing the steps of responding to a water inlet signal corresponding to the expansion water tank to obtain a current gas pressure value in the expansion water tank and calculating a difference value between the current gas pressure value and a preset gas pressure threshold value until the timing duration reaches the preset duration; and calculating an accumulated value of each difference value calculated in the step of circularly executing, and taking the accumulated value as the liquid level deviation value.

In some embodiments of the application, based on the foregoing, the computing module is further configured to: acquiring the total volume and the cooling liquid temperature value corresponding to the expansion water tank; calculating the gas volume in the expansion water tank according to the total volume, the cooling liquid temperature value, the new heat increment value and the current gas pressure value; and calculating a difference between the total volume and the gas volume, and taking the difference as the liquid level of the cooling liquid.

In some embodiments of the present application, based on the foregoing, the monitoring device applied to the cooling system further includes a self-checking module configured to: before a new heat value corresponding to an expansion water tank in a cooling system is acquired, executing a self-checking program corresponding to an adjusting part in the cooling system; wherein, when the regulating component is a water pump, the self-checking procedure includes: the rotating speed of a water pump in the cooling system is adjusted to be a calibrated rotating speed; when the obtained current rotating speed of the water pump reaches the calibrated rotating speed, obtaining the working current of the water pump, and determining the dry rotating current of the water pump based on the current rotating speed; if the working current does not exceed the dry rotation current, a first fault signal for representing the fault of the water pump is sent out; when the adjusting component is a temperature control module, the self-checking program includes: adjusting the rotation angle of a temperature control module in the cooling system to be a calibration rotation angle; when the acquired real-time rotation angle of the temperature control module reaches the calibration rotation angle, adjusting the current torque of the temperature control module to a preset torque, and calculating the difference between the real-time rotation angle of the temperature control module and the calibration rotation angle; and if the difference value between the real-time rotation angle and the calibration rotation angle exceeds a preset rotation angle deviation value, a second fault signal used for representing the fault of the temperature control module is sent out.

According to an aspect of an embodiment of the present application, there is provided a computer-readable storage medium having stored thereon computer-readable instructions, which when executed by a processor of a computer, cause the computer to perform the monitoring method applied to a cooling system as described in the above embodiment.

According to an aspect of an embodiment of the present application, there is provided an electronic apparatus including: one or more processors; and a storage means for storing one or more programs that, when executed by the one or more processors, cause the electronic device to implement the monitoring method applied to a cooling system as described in the above embodiments.

According to the technical scheme, the new heat increment value and the current gas pressure value corresponding to the expansion water tank in the cooling system are firstly obtained, then the liquid level of the cooling liquid corresponding to the expansion water tank is determined based on the new heat increment value and the current gas pressure value, finally, whether the liquid level of the cooling liquid exceeds the preset liquid level threshold of the expansion water tank is judged, if the liquid level of the cooling liquid exceeds the preset liquid level threshold of the expansion water tank, the situation that the cooling liquid in the cooling system is leaked is indicated, the liquid level of the cooling liquid in the expansion water tank is too low, the probability of causing a safety accident is relatively high, and an alarm signal for representing the leakage of the cooling liquid in the cooling system can be sent out, so that the purpose of confirming the leakage of the cooling liquid in the cooling system is achieved, operators can be timely informed after the leakage of the cooling liquid in the cooling system is confirmed, further processing of the operators is facilitated, and the safety accident caused by the fact that the content of the cooling liquid in the cooling system is too low is avoided.

Drawings

The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate embodiments consistent with the application and together with the description, serve to explain the principles of the application. It is evident that the drawings in the following description are only some embodiments of the present application and that other drawings may be obtained from these drawings without inventive effort for a person of ordinary skill in the art. In the drawings:

Fig. 1 is a schematic view of a cooling system according to the present application.

Fig. 2 is a flow chart illustrating a monitoring method applied to a cooling system according to an exemplary embodiment of the present application.

Fig. 3 is a flowchart of step S210 in an example embodiment in the embodiment shown in fig. 2.

Fig. 4 is a flowchart of step S310 in an example embodiment in the embodiment shown in fig. 3.

Fig. 5 is a flowchart of step S410 in an example embodiment in the embodiment shown in fig. 4.

Fig. 6 is a flowchart of step S520 in the embodiment shown in fig. 5 in an example embodiment.

Fig. 7 is a flowchart of step S310 in the embodiment shown in fig. 3 in yet another example embodiment.

Fig. 8 is a flowchart in another embodiment after step S220 in the embodiment shown in fig. 2.

Fig. 9 is a block diagram illustrating a monitoring apparatus applied to a cooling system according to an exemplary embodiment of the present application.

Fig. 10 is a schematic structural view of an electronic device according to an exemplary embodiment of the present application.

Detailed Description

Example embodiments will now be described more fully with reference to the accompanying drawings. However, the exemplary embodiments may be embodied in many forms and should not be construed as limited to the examples set forth herein; rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the concept of the example embodiments to those skilled in the art.

Furthermore, the described features, structures, or characteristics may be combined in any suitable manner in one or more embodiments. In the following description, numerous specific details are provided to give a thorough understanding of embodiments of the application. One skilled in the relevant art will recognize, however, that the application may be practiced without one or more of the specific details, or with other methods, components, devices, steps, etc. In other instances, well-known methods, devices, implementations, or operations are not shown or described in detail to avoid obscuring aspects of the application.

The block diagrams depicted in the figures are merely functional entities and do not necessarily correspond to physically separate entities. That is, the functional entities may be implemented in software, or in one or more hardware modules or integrated circuits, or in different networks and/or processor devices and/or microcontroller devices.

The flow diagrams depicted in the figures are exemplary only, and do not necessarily include all of the elements and operations/steps, nor must they be performed in the order described. For example, some operations/steps may be decomposed, and some operations/steps may be combined or partially combined, so that the order of actual execution may be changed according to actual situations.

It should be noted that: references herein to "a plurality" means two or more. "and/or" describes an association relationship of an association object, meaning that there may be three relationships, e.g., a and/or B may represent: a exists alone, A and B exist together, and B exists alone. The character "/" generally indicates that the context-dependent object is an "or" relationship.

Fig. 1 is a schematic diagram of an exemplary cooling system 100. As shown in fig. 1, the cooling system 100 includes a cooling liquid circulation line composed of a heat generating part 110, a heat radiating part 120, a regulating part 130, and an expansion tank 140, which are in piping communication.

In the related art, the cooling system 100 is operated by driving the cooling liquid in the cooling system to circulate through the adjusting component 130, so that the heat emitted by the heat generating component 110 is cooled by the heat dissipating component 120, and the heat generating component 110 maintains a better working state. However, once the cooling liquid in the cooling system 100 leaks, heat emitted by the heat generating component 110 may not be completely transferred to the heat dissipating component 120 for cooling through the cooling liquid, so that the heat generating component 110 works in an overheated state, thereby bringing an extremely high safety risk to an operator. Therefore, how to monitor the leakage condition of the cooling liquid in the cooling system 100 becomes a problem to be solved.

In order to monitor whether the cooling liquid in the cooling system leaks, the technical scheme of the embodiment of the application provides a monitoring method applied to the cooling system, and particularly, the monitoring method is shown in fig. 2. The method may be applied to the cooling system shown in fig. 1, and the method may be specifically performed by a controller provided in the cooling system shown in fig. 1, or of course, may be performed by a controller provided in a vehicle provided with the cooling system shown in fig. 1, without limitation. The method at least comprises the steps S210 to S230, and the detailed description is as follows:

In step S210, a new heat increment value and a current gas pressure value corresponding to the expansion tank in the cooling system are acquired.

It should be noted that, after the cooling liquid absorbs the heat emitted by the heat generating component in the cooling system, the volume of the cooling liquid expands correspondingly, and the circulation pipeline in the cooling system cannot accommodate the redundant cooling liquid, the redundant cooling liquid is discharged into the expansion water tank for storing the cooling liquid in the cooling system, and after the temperature of the cooling liquid is reduced, the part of the cooling liquid is returned to the circulation pipeline through the expansion water tank again. Meanwhile, the expansion water tank can absorb the air pressure released after the temperature of the cooling liquid is increased. The redundant cooling liquid entering the expansion water tank absorbs heat radiated by the heating component, the heat is transferred to the expansion water tank, and correspondingly, the newly increased heat value represents the heat radiated to the expansion water tank by the cooling system.

The manner of obtaining the new heat value corresponding to the expansion tank can be flexibly set according to the needs, and in one example, the heat sensor can be arranged in the cooling system, so that the new heat value corresponding to the expansion tank can be obtained through the heat sensor.

In another example, it is contemplated that the newly increased heat value of the expansion tank is related to the current coolant inflow amount, coolant inflow temperature value, and coolant discharge temperature value of the expansion tank. The new heat increment value of the expansion water tank can be calculated through the obtained cooling liquid inflow amount, cooling liquid inflow temperature value and cooling liquid discharge temperature value corresponding to the expansion water tank, so that the corresponding new heat increment value is calculated based on the actual working condition of the expansion water tank, and the accuracy of the obtained new heat increment value is improved.

The new heat increment value in the process can be calculated by adopting the following calculation formula:

Q_Tank_inside＝c×Tank_in×(T_Tank_inlet-T_Tank_outlet)

Wherein Q_tank_inside is the new heat increment value corresponding to the expansion Tank, c is the specific heat capacity corresponding to the cooling liquid in the cooling system, tank_in is the water inflow of the expansion Tank, T_tank_inlet is the water inlet temperature value of the expansion Tank, and T_tank_outlet is the water outlet temperature value of the expansion Tank.

The mode of acquiring the current gas pressure value corresponding to the expansion tank can be realized by arranging a pressure sensor in the expansion tank, so that the gas pressure value in the expansion tank is acquired through the arranged pressure sensor, and the gas pressure value acquired in the expansion tank is taken as the corresponding current gas pressure value.

In step S220, a level of the cooling liquid corresponding to the expansion tank is determined based on the newly increased heat value and the current gas pressure value.

Since the volume in the expansion tank is fixed and only the coolant and the gas generated by the coolant are contained in the expansion tank, that is, the liquid level of the coolant in the expansion tank changes with the change of the gas pressure value, and considering that the volume of the coolant in the expansion tank expands after absorbing heat, the liquid level of the coolant in the expansion tank also changes with the change of the new heat value, in the embodiment of the application, after the new heat value corresponding to the expansion tank is obtained, the liquid level of the coolant corresponding to the expansion tank can be determined based on the new heat value and the current gas pressure value, thereby determining the specific situation that the liquid level of the coolant in the expansion tank changes with the new heat value and the gas pressure value.

The manner of determining the liquid level of the cooling liquid corresponding to the expansion tank based on the new heat value and the current gas pressure value can be flexibly adjusted according to needs, in one example, the liquid level of the cooling liquid having a mapping relationship with the new heat value and the current gas pressure value can be determined in a preset liquid level table, that is, the mapping relationship between different liquid levels and corresponding new heat value and current gas pressure value can be prestored in the preset liquid level table. In addition, the generation mode of the preset liquid level meter can be generated through input after the test by a tester or according to the development experience input of a developer.

In another example, considering that the volumes of the cooling liquid and the gas in the expansion tank are both related to the temperature value of the cooling liquid in the expansion tank, the total volume and the cooling liquid temperature value corresponding to the expansion tank can be obtained first, then the gas volume in the expansion tank is calculated according to the total volume, the cooling liquid temperature value, the new heat increment value and the current gas pressure value, finally the difference between the total volume and the gas volume is calculated, and the difference is used as the cooling liquid level corresponding to the expansion tank, so that the corresponding cooling liquid level is determined according to the actual working condition of the expansion tank, and the accuracy of the determined cooling liquid level is improved.

The liquid level of the cooling liquid in the process can be calculated by adopting the following calculation formula:

V_Tank_gas＝V_Tank-V_Tank_liq

P1*V_Tank_gas＝c×f(Q_Tank_inside)×T_Tank_inside(n)

T_Tank_inside(n)＝T_Tank_insid(n-1)+[Q_Tank_inside÷(c×V_Tank_liq×ρ)]

Wherein v_tank_gas is the gas volume of the expansion Tank, v_tank is the total volume of the expansion Tank, v_tank_liq is the liquid level of the cooling liquid in the expansion Tank, P1 is the current gas pressure value in the expansion Tank, f (q_tank_inside) is a coefficient set based on the newly increased heat value, t_tank_inside (n) is the temperature value after the temperature value of the expansion Tank in the volume corresponding to the liquid level threshold is changed by the newly increased heat value, t_tank_ insid (n-1) is the temperature value before the temperature value of the expansion Tank in the volume corresponding to the liquid level threshold is changed by the newly increased heat value, ρ is the density corresponding to the cooling liquid in the cooling system.

In step S230, if the coolant level does not exceed the preset level threshold of the expansion tank, an alarm signal is sent to indicate a coolant leak in the cooling system.

It should be noted that, in order to determine whether the coolant in the cooling system leaks, a liquid level threshold corresponding to the cooling system may be preset based on an actual working condition of the cooling system and a volume of the expansion tank, so as to determine that the coolant in the cooling system leaks when a liquid level of the coolant in the expansion tank is lower than the liquid level threshold.

In the embodiment of the application, after the liquid level of the cooling liquid corresponding to the expansion water tank is calculated, if the liquid level of the cooling liquid does not exceed the liquid level threshold preset by the expansion water tank, the cooling liquid in the cooling system is leaked, and the liquid level of the cooling liquid in the expansion water tank is too low, so that the probability of causing a safety accident is relatively high, an alarm signal for representing the leakage of the cooling liquid in the cooling system is sent out, thereby timely informing an operator after the leakage of the cooling liquid in the cooling system is confirmed, facilitating the further processing of the operator and avoiding the safety accident caused by the too low content of the cooling liquid in the cooling system.

In the present application, considering that the cooling system 100 shown in fig. 1 circulates the cooling liquid in the cooling system 100 through the heat generating component 110 and the heat dissipating component 120 in the cooling system 100 during operation, so as to transfer and cool the heat emitted by the heat generating component 110, and the volume of the cooling liquid is further expanded while the temperature of the cooling liquid is gradually increased, in order to avoid the expansion of the cooling liquid after the heat generating component 110 or the heat dissipating component 120 is expanded, branch ports are provided on the heat generating component 110 and the heat dissipating component 120, so that when the volume of the cooling liquid expands, the redundant cooling liquid is discharged through the corresponding branch ports of the heat generating component 110 and the heat dissipating component 120. Meanwhile, the expansion tank 140 includes a first water inlet communicating with the branch port of the heat generating part 110 and a second water inlet communicating with the branch port of the heat radiating part 120, so that the surplus coolant discharged from the branch ports of the heat generating part 110 and the heat radiating part 120 is recovered through the first water inlet and the second water inlet.

Based on the above and the technical solution of the embodiment shown in fig. 2, in an embodiment of the present application, the process of obtaining the new heat increment value and the current gas pressure value corresponding to the expansion tank in the cooling system may include steps S310 to S330. Referring specifically to fig. 3, the following is described in detail:

In step S310, the coolant branch flow and the coolant branch temperature value corresponding to the first water inlet and the second water inlet are obtained, respectively.

Since the newly increased heat value of the expansion tank is correlated with the inflow amount of the cooling liquid discharged into the expansion tank and the temperature value of the cooling liquid discharged into the expansion tank, the expansion tank receives the cooling liquid supplied by the heat radiating member and the heat generating member at the same time, that is, the newly increased heat value of the expansion tank is correlated with the inflow amount and the temperature value of the cooling liquid supplied by the heat radiating member and the heat generating member. In addition, the heat emitted by the heat radiating component and the heat emitted by the heat generating component are different, so that the temperature values corresponding to the cooling liquid conveyed by the heat radiating component and the heat generating component are different. Therefore, in the embodiment of the application, in the process of acquiring the newly-increased heat value corresponding to the expansion water tank, the flow rate of the cooling liquid branch and the temperature value of the cooling liquid branch corresponding to the first water inlet and the second water inlet respectively can be acquired first.

The flow rate values of the cooling liquid flowing through the first water inlet and the second water inlet can be acquired based on the set flow rates by arranging the flow meters in the first water inlet and the second water inlet, so that the flow rate values acquired at the first water inlet and the second water inlet are respectively used as the flow rates of the cooling liquid branches respectively corresponding to the first water inlet and the second water inlet. And the temperature sensors can be respectively arranged at the first water inlet and the second water inlet in a mode of respectively acquiring the temperature values of the cooling liquid branches corresponding to the first water inlet and the second water inlet, so that the temperature values of the cooling liquid flowing through the first water inlet and the second water inlet are acquired through the arranged temperature sensors, and the temperature values acquired at the first water inlet and the second water inlet are used as the temperature values of the cooling liquid branches corresponding to the first water inlet and the second water inlet.

In step S320, a coolant discharge temperature value of the expansion tank is acquired.

The method for acquiring the cooling liquid discharge temperature value of the expansion water tank can also acquire the cooling liquid discharge temperature value of the expansion water tank by adopting a mode of setting a temperature sensor, namely, setting the temperature sensor at the discharge port of the expansion water tank, so that the temperature value corresponding to the cooling liquid flowing through the discharge port of the expansion water tank is acquired by the set temperature sensor, and the acquired temperature value is used as the cooling liquid discharge temperature value.

In step S330, a new heat increment value is calculated according to the coolant branch flow and the coolant branch temperature values and the coolant discharge temperature values corresponding to the first water inlet and the second water inlet, respectively.

In the embodiment of the application, the new heat increment value can be calculated according to the cooling liquid branch flow and the cooling liquid branch temperature value which are respectively corresponding to the first water inlet and the second water inlet and the cooling liquid discharge temperature value of the expansion water tank, so as to determine the new heat increment value of the expansion water tank based on the actual heat radiation of the heating component and the heat radiation component in the cooling system, thereby improving the accuracy of the obtained new heat increment value.

Q_Tank_inside＝c×mf_Tank_Eng_in_Act×(T_CylHed_gas-T_Tank_outlet)

+c×mf_Tank_Rad_in_Act×(T_Rad_gas-T_Tank_outlet)

wherein mf_tank_eng_in_act is the cooling liquid branch flow corresponding to the first water inlet, t_ CylHed _gas is the cooling liquid branch temperature value corresponding to the first water inlet, mf_tank_rad_in_act is the cooling liquid branch flow corresponding to the second water inlet, and t_rad_gas is the cooling liquid branch temperature value corresponding to the second water inlet.

In order to avoid wasting resources of the cooling system while ensuring that the cooling speed is not easily reduced, the present application considers that the heat emitted by the heat generating component 110 in the cooling system 100 shown in fig. 1 is continuously changed, and an adjusting component 130 for controlling the flow of the cooling liquid is provided in the cooling system 100 to adjust the flow rate of the cooling liquid according to the change of the heat emitted by the heat generating component 110, thereby avoiding wasting resources.

Based on the foregoing and the technical solutions of the embodiments shown in fig. 3, in an embodiment of the present application, the process of obtaining the flow rate and the temperature value of the cooling liquid branch corresponding to each of the first water inlet and the second water inlet respectively may include steps S410 to S430. Referring specifically to fig. 4, the following is described in detail:

in step S410, the coolant inflow amounts of the heat generating component and the heat radiating component, respectively, are determined based on the coolant flow adjustment parameters of the adjustment component.

It should be noted that, since the adjusting module is used to control the flow of the cooling liquid, that is, the water inflow corresponding to each component in the cooling system will change with the change of the flow adjusting parameter of the cooling liquid corresponding to the adjusting module.

The manner of determining the respective coolant inflow amounts of the heat generating component and the heat dissipating component based on the coolant inflow adjustment parameters of the adjusting component may be flexibly adjusted according to needs, and in one example, the respective coolant inflow amounts of the heat generating component and the heat dissipating component having a mapping relationship with the coolant inflow adjustment parameters of the adjusting component may be determined in a preset flow meter, that is, the mapping relationship between the coolant inflow amounts of the different coolant inflow adjustment parameters and the heat generating component and the coolant inflow amount of the heat dissipating component may be prestored in the preset flow meter. In addition, the generation mode of the preset flow meter can be input and generated after the test by a tester or according to the development experience input of a developer.

In another example, considering that the heat generating component generates different heat rates under different working conditions, and the higher the heat absorbed by the cooling liquid is, the interaction force between molecules is reduced, so that the adjusting module more easily pushes the cooling liquid to flow, that is, under the same cooling liquid flow adjusting parameter, the higher the cooling liquid temperature is, the larger the flow of the cooling liquid is, the current working condition of the heating component can be obtained, a corresponding target preset flow meter is determined according to the current working condition, and then the cooling liquid inflow amounts respectively corresponding to the heating component and the cooling component which have mapping relation with the cooling liquid flow adjusting parameter of the adjusting component are respectively determined in the target preset flow meter, so that the accuracy of the determined cooling liquid inflow amounts respectively corresponding to the heating component and the cooling component is improved.

In step S420, the bypass discharge flow ratio corresponding to each of the heat generating part and the heat radiating part is obtained.

In the embodiment of the application, after the respective corresponding cooling liquid inflow rates of the heating component and the heat dissipation component are determined, the respective corresponding branch discharge flow rates of the heating component and the heat dissipation component can be obtained, wherein the branch discharge flow rate represents the ratio of the cooling liquid to be discharged to the expansion water tank in the cooling liquid inflow rate, that is, the respective corresponding branch discharge flow rates of the heating component and the heat dissipation component are obtained to respectively determine the ratio of the cooling liquid to be discharged to the expansion water tank in the respective corresponding cooling liquid inflow rates of the heating component and the heat dissipation component.

In step S430, the coolant bypass flow rates corresponding to the first water inlet and the second water inlet are calculated according to the coolant inflow rate and the bypass discharge flow rate ratios corresponding to the heat generating component and the heat radiating component, respectively.

In the embodiment of the application, after the branch discharge flow rate ratio of each corresponding heat generating component and heat radiating component is obtained, the branch flow rate of the cooling liquid corresponding to each first water inlet and second water inlet can be calculated according to the cooling liquid inflow rate and branch discharge flow rate ratio of each corresponding heat generating component and heat radiating component, so that the cooling liquid flow rate of each first water inlet and second water inlet entering the expansion water tank is determined based on the current cooling liquid inflow rate of each corresponding heat generating component and heat radiating component in the cooling system, and the accuracy of the obtained branch flow rate of the cooling liquid corresponding to each first water inlet and second water inlet is improved.

The flow of the cooling liquid branch corresponding to the first water inlet and the second water inlet in the process can be calculated by adopting the following calculation formula:

mf_Tank_Eng_in_Act＝mf_Eng_Act×mf_CylHed_gas_coef

mf_Tank_Rad_in_Act＝mf_Rad_Act×mf_Rad_gas_coef

Wherein mf_eng_act is the cooling liquid water inflow corresponding to the heating element, mf_ CylHed _gas_coef is the branch discharge flow rate corresponding to the heating element, mf_rad_act is the cooling liquid water inflow corresponding to the heat dissipation element, and mf_rad_gas_coef is the branch discharge flow rate corresponding to the heat dissipation element.

In addition, it is considered that the cooling system is a closed constant pressure system, that is, the coolant outlet amount of the expansion tank is equal to the coolant inlet amount of the expansion tank. Therefore, in the embodiment of the present application, the target component may be determined from the heat generating component and the heat dissipating component, the target component is one of the heat generating component and the heat dissipating component, the coolant inflow amount and the branch discharge flow rate ratio corresponding to the target component are determined based on the coolant flow rate adjustment parameter of the adjusting component, the coolant branch flow rate corresponding to the target component may be calculated based on the coolant inflow amount and the branch discharge flow rate ratio, and then the coolant branch flow rate corresponding to the other component except the target component is calculated based on the obtained coolant inflow amount of the expansion tank and the coolant branch flow rate corresponding to the target component, so that the coolant branch flow rates corresponding to the first water inlet and the second water inlet are respectively obtained.

Referring to fig. 5, fig. 5 is a flow chart of step S410 in an exemplary embodiment in the embodiment shown in fig. 4. As shown in fig. 4, the process of determining the inflow amounts of the cooling liquid corresponding to the heat generating component and the heat dissipating component, respectively, based on the cooling liquid inflow amount adjustment parameters of the adjustment component may include steps S510 to S530, which are described in detail as follows:

In step S510, the theoretical inflow amounts of the coolant for each of the heat generating component and the heat radiating component are determined based on the coolant flow adjustment parameters.

The method of determining the theoretical inflow of the cooling liquid corresponding to each of the heat generating component and the heat dissipating component based on the cooling liquid flow adjusting parameter of the adjusting component may refer to the method described in step S410, that is, by setting a preset theoretical flow table in which mapping relationships between the theoretical inflow of the cooling liquid of different cooling liquid flow adjusting parameters and heat generating components and the theoretical inflow of the cooling liquid of the heat dissipating component are prestored, so as to determine the theoretical inflow of the cooling liquid corresponding to each of the heat generating component and the heat dissipating component based on the preset theoretical flow table, or obtain the current working condition of the heat generating component first, determine the corresponding target preset theoretical flow table according to the current working condition, and determine the theoretical inflow of the cooling liquid corresponding to each of the heat generating component and the heat dissipating component based on the target preset theoretical flow table, thereby improving the accuracy of the determined theoretical inflow of the cooling liquid corresponding to each of the heat generating component and the heat dissipating component.

In step S520, a water inflow correction factor corresponding to the heat generating component at the current heat generating temperature is acquired.

Because the higher the heat absorbed by the cooling liquid is, the faster the flowing speed of the cooling liquid is, in the embodiment of the application, after the theoretical water inflow of the cooling liquid corresponding to each of the heating component and the heat dissipation component is determined, the corresponding water inflow correction coefficient of the heating component at the current heating temperature can be obtained.

The method for acquiring the current heating temperature of the heating component can be flexibly adjusted according to the requirement, and in one example, a temperature sensor can be arranged in the heating component to acquire the temperature value of the heating component through the arranged temperature sensor, so that the acquired temperature value is used as the current heating temperature of the heating component.

In another example, considering that the cooling liquid is used to absorb heat emitted from the heat generating component, that is, that the temperature of the cooling liquid discharged from the heat generating component is correlated with the current heat generating temperature of the heat generating component, the collected cooling liquid discharge temperature value of the heat generating component may be taken as the current heat generating temperature of the heat generating component by disposing a temperature sensor at the cooling liquid discharge port of the heat generating component to collect the cooling liquid discharge temperature value of the heat generating component by the disposed temperature sensor.

In step S530, the coolant inflow amounts of the heat generating component and the heat radiating component are calculated based on the coolant theoretical inflow amounts and the inflow correction factors of the heat generating component and the heat radiating component, respectively.

In the embodiment of the application, based on the theoretical water inflow of the cooling liquid of the heating component and the water inflow correction coefficient corresponding to the current heating temperature, the water inflow of the cooling liquid corresponding to the heating component and the cooling component can be calculated according to the theoretical water inflow of the cooling liquid corresponding to the heating component and the cooling component and the water inflow correction coefficient.

The cooling liquid inflow amounts respectively corresponding to the heating component and the heat dissipation component in the process can be calculated by adopting the following calculation formula:

mf_Eng_Act＝mf_Eng×mf_mod

mf_Rad_Act＝mf_Rad×mf_mod

Wherein mf_eng is the theoretical inflow of the cooling liquid corresponding to the heating element, mf_mod is the corresponding inflow correction coefficient of the heating element at the current heating temperature, and mf_rad is the theoretical inflow of the cooling liquid corresponding to the heat dissipation element.

According to the embodiment, on the basis of considering the influence of the cooling fluid flow rate adjusting parameter of the adjusting component on the cooling fluid inflow rate corresponding to each of the heating component and the radiating component, the influence of the current heating temperature of the heating component on the cooling fluid inflow rate corresponding to each of the heating component and the radiating component is also considered, so that the cooling fluid inflow rate corresponding to each of the heating component and the radiating component is calculated according to the theoretical cooling fluid inflow rate corresponding to each of the heating component and the radiating component and the water inflow correction coefficient corresponding to each of the heating component at the current heating temperature, and the accuracy of the obtained cooling fluid inflow rate corresponding to each of the heating component and the radiating component is improved.

Referring to fig. 6, fig. 6 is a flow chart of step S520 in an exemplary embodiment in the embodiment shown in fig. 5. As shown in fig. 6, when the heat generating component includes a plurality of heat generating units, the process of acquiring the inflow correction coefficient corresponding to the heat generating component at the current heat generating temperature may include steps S610 to S630, which are described in detail as follows:

In step S610, a coolant discharge temperature value and a coolant water intake ratio corresponding to each heating unit are acquired.

When the heat generating component in the cooling system includes a plurality of heat generating units, in order to ensure that the plurality of heat generating units can be cooled in time, the cooling system generally simultaneously conveys the cooled coolant to each heat generating unit, for example, an engine cylinder cover, an engine cylinder block or an oil cooler in the vehicle, and in order to ensure that each heat generating unit in the vehicle is not easy to overheat, the cooling system simultaneously conveys the cooled coolant to the engine cylinder cover, the engine cylinder block or the oil cooler.

Since the heat generating component includes a plurality of heat generating units, the heat generating temperatures corresponding to the heat generating units are different, and the cooling system simultaneously transmits the cooling liquid to the heat generating units, that is, the flow rates of the cooling liquid received by the heat generating units are also different. In the embodiment of the application, in order to obtain the current heating temperature of the heating component, a cooling liquid discharge temperature value and a cooling liquid water inlet ratio corresponding to each heating component can be obtained, wherein the cooling liquid water inlet ratio represents the ratio of the cooling liquid water inlet amount of the heating unit in the total cooling liquid circulation amount of the cooling system.

The method of obtaining the cooling liquid water inlet ratio corresponding to each heating component can firstly determine the cooling liquid water inlet amount corresponding to each heating unit through the cooling liquid flow rate adjusting parameter, then calculate the total cooling liquid circulation amount based on the cooling liquid water inlet amount corresponding to each heating unit, that is, calculate the accumulated value of the cooling liquid water inlet amount corresponding to each heating unit, and take the calculated accumulated value as the total cooling liquid circulation amount. The ratio of the coolant inlet of each heating component is the ratio of the determined coolant inlet amount to the total coolant circulation amount.

In step S620, the integrated heat generation temperature is calculated according to the coolant discharge temperature value and the coolant water intake ratio corresponding to each heat generation unit.

In the embodiment of the application, after the cooling liquid discharge temperature value and the cooling liquid water inlet ratio corresponding to each heating unit are obtained, the comprehensive heating temperature can be calculated according to the cooling liquid discharge temperature value and the cooling liquid water inlet ratio corresponding to each heating unit so as to determine the comprehensive heating state of the heating component.

When the plurality of heating units contained in the heating component are the engine cylinder cover, the engine cylinder body and the oil cooler respectively, the comprehensive heating temperature in the process can be calculated by adopting the following calculation formula:

T_overall＝T1×mf_CylHed_prop+T2×mf_CylBlk_prop+T3*mf_OC_prop

Wherein, T_overlap is the comprehensive heating temperature, T1 is the coolant discharge temperature value of the engine cylinder cover, mf_ CylHed _prop is the coolant water inlet proportion of the engine cylinder cover, T2 is the coolant discharge temperature value of the engine cylinder body, mf_ CylBlk _prop is the coolant water inlet proportion of the engine cylinder body, T3 is the coolant discharge temperature value of the oil cooler, and mf_OC_prop is the coolant water inlet proportion of the oil cooler.

In step S630, the water intake correction coefficient is determined using the integrated heat generation temperature as the current heat generation temperature of the heat generation component.

In the embodiment of the application, after the comprehensive heating temperature is calculated, the comprehensive heating temperature can be used as the current heating temperature of the heating component to determine the water inlet correction coefficient so as to determine the current heating temperature of the heating component with a plurality of heating units based on the heating state of each heating unit, thereby improving the accuracy of the determined water inlet correction coefficient.

In addition, the difference in the heating rate of the heating component when the heating component operates at different ambient temperatures is considered, that is, the heating rates corresponding to the heating component in the cold environment and the heating component in the hot environment are different. Therefore, in the embodiment of the application, after the current heating temperature of the heating component is obtained, the current environment temperature can also be obtained, so that the water inlet correction coefficient is determined based on the current heating temperature of the heating component and the current environment temperature, and the accuracy of the determined water inlet correction coefficient is further improved.

Referring to fig. 7, fig. 7 is a flowchart of step S310 in an exemplary embodiment in the embodiment shown in fig. 3. As shown in fig. 7, the process of obtaining the flow rate and the temperature value of the cooling liquid branch corresponding to the first water inlet and the second water inlet, respectively, may include steps S710 to S720, which are described in detail below:

in step S710, discharge length information, a coolant inflow temperature value, and a coolant discharge temperature value, respectively, corresponding to the heat generating part and the heat radiating part are acquired, respectively.

The cooling liquid flowing through the first water inlet and the second water inlet flows out from the heat generating component and the heat dissipating component, that is, the cooling liquid branch temperature values of the first water inlet and the second water inlet are related to the cooling liquid inlet temperature value and the cooling liquid discharge temperature value of the heat generating component and the heat dissipating component, and are also related to the corresponding structural parameters of the heat generating component and the heat dissipating component.

In the embodiment of the application, in order to obtain the respective coolant branch temperature values of the first water inlet and the second water inlet, the respective discharge length information, the respective coolant inlet temperature value and the respective coolant discharge temperature value of the heat generating component and the heat dissipating component may be obtained first, where the discharge length information includes the respective discharge distances from the respective water inlet to the branch port and from the water inlet to the discharge port in the heat generating component and the heat dissipating component.

Since the emission length information is one of the structural parameters of the heat generating component and the heat dissipating component, the emission length information corresponding to each of the heat generating component and the heat dissipating component can be obtained by directly inquiring the product structural information of the heat generating component and the heat dissipating component.

In step S720, a coolant branch temperature value corresponding to each of the first water inlet and the second water inlet is calculated according to the discharge length information, the coolant inlet temperature value, and the coolant discharge temperature value corresponding to each of the heat generating component and the heat radiating component.

In the embodiment of the application, after the discharge length information, the cooling liquid inlet temperature value and the cooling liquid discharge temperature value which are respectively corresponding to the heating component and the cooling component are obtained, the cooling liquid branch temperature value which is respectively corresponding to the first water inlet and the second water inlet can be calculated according to the discharge length information, the cooling liquid inlet temperature value and the cooling liquid discharge temperature value which are respectively corresponding to the heating component and the cooling component, so that the cooling liquid branch temperature value which is respectively corresponding to the first water inlet and the second water inlet can be determined only by collecting the cooling liquid inlet temperature value and the cooling liquid discharge temperature value which are respectively corresponding to the heating component and the cooling component, and further, the temperature sensors are not required to be arranged on the first water inlet and the second water inlet, thereby saving the production cost.

The temperature values of the cooling liquid branches corresponding to the first water inlet and the second water inlet in the process can be calculated by adopting the following calculation formula:

T_CylHed_gas＝[(T1-T3)÷Len_CylHed]×Len_CylHed_gas+T3

T_Rad_gas＝[(T4-T5)÷Len_Rad]*Len_Rad_gas+T5

Wherein len_ CylHed is the discharge distance from the water inlet to the discharge outlet of the heat generating component, len_ CylHed _gas is the discharge distance from the water inlet to the branch outlet of the heat generating component, T4 is the coolant discharge temperature value of the heat dissipating component, T5 is the coolant inlet temperature value of the heat dissipating component, len_rad is the discharge distance from the water inlet to the discharge outlet of the heat dissipating component, and len_rad_gas is the discharge distance from the water inlet to the branch outlet of the heat dissipating component.

In addition, considering that the structural parameters of the heat generating component and the heat dissipating component can also affect the branch flow of the cooling liquid corresponding to each of the first water inlet and the second water inlet, that is, in the embodiment of the application, after the discharge length information corresponding to each of the heat generating component and the heat dissipating component is obtained, the branch discharge flow ratio corresponding to each of the heat generating component and the heat dissipating component can be determined through the discharge length information corresponding to each of the heat generating component and the heat dissipating component, so as to improve the accuracy of the obtained branch discharge flow ratio.

Referring to fig. 8, fig. 8 is a flowchart illustrating a monitoring method applied to a cooling system according to another exemplary embodiment. As shown in fig. 8, after step S220 in the embodiment shown in fig. 2, the method may further include steps S810 to S820, which are described in detail below:

In step S810, when the liquid level of the cooling liquid is between the liquid level threshold and the preset safe liquid level threshold of the expansion tank, timing is started, and if the timing duration reaches the preset duration, the liquid level deviation value of the expansion tank is calculated.

It should be noted that, considering that the working conditions of the heat generating components in the cooling system are generally transient, so that the temperature value of the cooling liquid is suddenly high and suddenly low, and the fluctuation range is relatively large, the safe liquid level threshold used for representing the possible leakage risk of the cooling liquid in the cooling system can be preset based on the actual working condition of the cooling system and the volume of the expansion tank.

In the embodiment of the application, after the liquid level of the cooling liquid corresponding to the expansion water tank is determined based on the newly increased heat value and the current gas pressure value, when the liquid level of the cooling liquid is between the liquid level threshold value and the preset safety liquid level threshold value of the expansion water tank, the expansion water tank under the current liquid level is indicated to represent that the cooling liquid in the cooling system possibly has leakage risk, in order to further confirm whether the cooling system has leakage or not, timing is started when the temperature value of the cooling liquid is between the cooling liquid temperature threshold value and the cooling liquid temperature safety threshold value, and if the timing duration reaches the preset duration, the liquid level deviation value of the expansion water tank is calculated.

The liquid level deviation value of the expansion tank can be flexibly adjusted according to the requirement, and the fact that the liquid level of the cooling liquid in the expansion tank is related to the pressure in the expansion tank, namely the liquid level of the cooling liquid in the expansion tank changes along with the change of the pressure in the expansion tank, is considered. In one example, the current pressure value of the expansion tank may be obtained when the timed duration reaches a preset duration, and a difference between the current pressure value and a preset pressure threshold value may be calculated to determine a liquid level deviation value from the calculated difference.

In another example, the steps of acquiring a current gas pressure value in the expansion tank in response to a corresponding inflow signal of the expansion tank, and calculating a difference between the current gas pressure value and a preset gas pressure threshold value may be performed in a cyclic manner until a time period reaches the preset time period, and finally calculating an accumulated value of each difference calculated in the step of performing in the cyclic manner, taking the accumulated value as a liquid level deviation value, so as to determine the liquid level deviation value each time based on a fluctuation change of the gas pressure in the expansion tank during the time period when the cooling liquid temperature value is between the cooling liquid temperature threshold value and the cooling liquid temperature safety threshold value, thereby improving the accuracy of the determined liquid level deviation value.

In step S820, if the liquid level deviation exceeds the preset safety threshold, an alarm signal is sent.

If the heating component works in a tiny leakage state for a long time, the temperature difference between the cooling liquid and the heating component is larger than expected, so that the internal part of the heating component exceeds the thermal stress born by the original design value, and the risk of deformation possibly occurs. In the embodiment of the application, after the liquid level deviation value of the expansion water tank is calculated, if the liquid level deviation value exceeds the preset safety threshold, the condition that continuous tiny leakage exists in the expansion water tank is represented, an alarm signal is sent out, an operator is timely informed, the operator can conveniently further process the liquid level deviation value, and the situation that the safety accident is caused due to deformation of a heating component is avoided.

In another exemplary embodiment, the application provides a monitoring method applied to a cooling system, and the method executes a self-checking program corresponding to an adjusting component in the cooling system before a new heat value corresponding to an expansion tank in the cooling system is acquired, so as to determine whether the adjusting component fails or not through the self-checking program, thereby being convenient for limiting the operation power of a heating component when the adjusting component is confirmed to fail, and avoiding that cooling liquid flowing through the heating component cannot completely absorb heat emitted by the heating component.

Wherein, when the adjusting part is a water pump for controlling the flow rate of the cooling liquid, the self-checking program comprises the following steps:

the rotating speed of a water pump in the cooling system is adjusted to be a calibrated rotating speed;

When the obtained current rotating speed of the water pump reaches the calibrated rotating speed, obtaining the working current of the water pump, and determining the dry rotating current of the water pump based on the current rotating speed;

And if the working current does not exceed the dry rotation current, a first fault signal for representing the fault of the water pump is sent out.

In the process, when the regulating component is the water pump, the rotating speed of the water pump in the cooling system is regulated to the calibrated rotating speed, when the obtained current rotating speed of the water pump reaches the calibrated rotating speed, the working current of the water pump is obtained, and the dry rotating current of the water pump is determined based on the current rotating speed, wherein the dry rotating current represents the current required by the water pump to reach the current rotating speed when the water pump is not connected with cooling liquid, if the working current does not exceed the dry rotating current, the current value of the water pump connected with cooling liquid at the current rotating speed is indicated, even the current value of the water pump not connected with cooling liquid at the current rotating speed is lower than the current value of the water pump connected with cooling liquid, the current failure of the water pump in the cooling system is determined, so that a first failure signal used for representing the failure of the water pump can be sent out, and an operator can conveniently process the failure in time, or the operation power of the heating component is regulated based on the first failure signal in the process of working of the subsequent control of the heating component.

When the adjusting component is a temperature control module for controlling the flow of the cooling liquid corresponding to the heating component and the heat dissipation component in the cooling system, the self-checking program comprises:

adjusting the rotation angle of a temperature control module in the cooling system to be a calibration rotation angle;

When the acquired real-time rotation angle of the temperature control module reaches the calibration rotation angle, adjusting the current torque of the temperature control module to a preset torque, and calculating the difference between the real-time rotation angle of the temperature control module and the calibration rotation angle;

and if the difference value between the real-time rotation angle and the calibration rotation angle exceeds the preset rotation angle deviation value, a second fault signal for representing the fault of the temperature control module is sent.

In the process, when the adjusting component is the temperature control module, the rotating angle of the temperature control module in the cooling system is adjusted to be the calibration rotating angle, and when the acquired real-time rotating angle of the temperature control module reaches the calibration rotating angle, the current torque of the temperature control module is adjusted to be the preset torque so as to ensure that the rotating angle of the temperature control module reaches the mechanical dead center for clamping the ball valve in the temperature control module, the difference value between the real-time rotating angle of the temperature control module and the calibration rotating angle is calculated, if the difference value between the real-time rotating angle and the calibration rotating angle exceeds the preset rotating angle deviation value, the real-time rotating angle of the temperature control module is still continuously rotated after the calibration rotating angle is reached, and the rotating angle is larger than the preset rotating angle deviation value, so that the temperature control module is determined to have faults, and further, a second fault signal for representing the faults of the temperature control module can be sent out, so that operators can timely process the faults, or in the process of working of the subsequent control heating components, and the running power of the heating component is adjusted based on the second fault signal.

In addition, before the current torque of the temperature control module is adjusted to the preset torque, whether the current torque of the temperature control module is not 0 can be judged first, if yes, an indication signal for representing that the rotation angle of the temperature control module reaches a mechanical dead point for clamping the ball valve in the temperature control module is sent out and timing is started, when the timing time reaches the preset detection time, whether the rotation angle variation of the temperature control module is larger than the preset rotation angle variation is judged, if no, it is determined that the ball valve in the temperature control module is clamped by the mechanical dead point and cannot continue to rotate, and therefore the current torque of the temperature control module is adjusted to the preset torque, and damage caused by collision with the mechanical dead point inside the temperature control module due to the fact that the rotation speed of the ball valve in the temperature control module is fast is avoided.

The following describes an embodiment of the apparatus of the present application that may be used to perform the monitoring method of the above-described embodiment of the present application applied to a cooling system. For details not disclosed in the embodiments of the apparatus of the present application, please refer to the embodiments of the monitoring method applied to the cooling system.

Fig. 9 shows a block diagram of a monitoring device 900 applied to a cooling system according to an embodiment of the present application.

Referring to fig. 9, a monitoring apparatus 900 applied to a cooling system according to an embodiment of the present application includes: an acquisition module 910 configured to acquire a new heat increment value and a current gas pressure value corresponding to an expansion tank in the cooling system; a calculation module 920 configured to determine a coolant level corresponding to the expansion tank based on the new heat value and the current gas pressure value; the leakage determination module 930 is configured to issue an alarm signal for indicating a leakage of the cooling fluid in the cooling system if the level of the cooling fluid does not exceed a predetermined level threshold of the expansion tank.

In some embodiments of the present application, based on the foregoing aspect, the cooling system includes a heat generating component and a heat dissipating component, the expansion tank includes a first water inlet communicating with a branch port of the heat generating component and a second water inlet communicating with a branch port of the heat dissipating component, and the obtaining module 910 is further configured to: respectively obtaining the flow of the cooling liquid branch and the temperature value of the cooling liquid branch, which correspond to the first water inlet and the second water inlet respectively; acquiring a cooling liquid discharge temperature value of an expansion water tank; and calculating a new heat increment value according to the cooling liquid branch flow and the cooling liquid branch temperature value which correspond to the first water inlet and the second water inlet respectively and the cooling liquid discharge temperature value.

In some embodiments of the application, based on the foregoing, the cooling system includes an adjustment component for controlling the flow of the cooling fluid, and the acquisition module 910 is further configured to: respectively determining the cooling liquid inflow amount corresponding to each of the heating component and the heat dissipation component based on the cooling liquid inflow amount adjusting parameter of the adjusting component; acquiring the branch discharge flow ratio corresponding to each of the heating component and the heat dissipation component; the bypass discharge flow ratio represents the ratio of the cooling liquid to be discharged to the expansion water tank in the cooling liquid water inflow; and calculating the cooling liquid branch flow corresponding to each of the first water inlet and the second water inlet according to the cooling liquid inflow and branch discharge flow ratio corresponding to each of the heating component and the heat radiating component.

In some embodiments of the present application, based on the foregoing scheme, the acquisition module 910 is further configured to: determining theoretical inflow of the cooling liquid corresponding to each of the heating component and the heat radiating component based on the cooling liquid flow regulating parameter; acquiring a water inlet correction coefficient corresponding to the heating component at the current heating temperature; and calculating the cooling liquid inflow rate corresponding to the heating component and the heat dissipation component according to the cooling liquid theoretical inflow rate corresponding to the heating component and the heat dissipation component respectively and the inflow correction coefficient.

In some embodiments of the present application, based on the foregoing, the heat generating component includes a plurality of heat generating units, and the acquisition module 910 is further configured to: acquiring a cooling liquid discharge temperature value and a cooling liquid water inlet proportion corresponding to each heating unit; the cooling liquid water inlet proportion represents the ratio of the cooling liquid water inlet quantity of the heating unit in the total cooling liquid circulation quantity of the cooling system; calculating the comprehensive heating temperature according to the cooling liquid discharge temperature value and the cooling liquid water inlet proportion corresponding to each heating unit; and determining a water inlet correction coefficient by taking the comprehensive heating temperature as the current heating temperature of the heating component.

In some embodiments of the present application, based on the foregoing scheme, the acquisition module 910 is further configured to: the method for respectively obtaining the flow and the temperature value of the cooling liquid branch corresponding to the first water inlet and the second water inlet comprises the following steps: respectively acquiring discharge length information, a cooling liquid inlet temperature value and a cooling liquid discharge temperature value corresponding to the heating component and the radiating component; the discharge length information comprises the discharge distance from the water inlet to the branch port and the discharge distance from the water inlet to the discharge port, which are respectively corresponding to the heating component and the heat dissipation component; and calculating the temperature value of the cooling liquid branch corresponding to each of the first water inlet and the second water inlet according to the discharge length information, the cooling liquid inlet temperature value and the cooling liquid discharge temperature value corresponding to each of the heating component and the heat radiating component.

In some embodiments of the present application, based on the foregoing, the monitoring device 900 applied to the cooling system further includes a leakage safety module configured to: after determining the liquid level of the cooling liquid corresponding to the expansion water tank based on the newly increased heat value and the current gas pressure value, starting timing when the liquid level of the cooling liquid is between a liquid level threshold value and a preset safe liquid level threshold value of the expansion water tank, and calculating a liquid level deviation value of the expansion water tank if the timing time length reaches a preset time length; and if the liquid level deviation value exceeds a preset safety threshold, sending out an alarm signal.

In some embodiments of the application, based on the foregoing, the leakage security module is further configured to: circularly executing the steps of responding to a water inlet signal corresponding to the expansion water tank to obtain a current gas pressure value in the expansion water tank, and calculating a difference value between the current gas pressure value and a preset gas pressure threshold value until the timing duration reaches the preset duration; and calculating the accumulated value of each difference value calculated in the step of circularly executing, and taking the accumulated value as a liquid level deviation value.

In some embodiments of the application, based on the foregoing, the computing module 920 is further configured to: acquiring the total volume and the cooling liquid temperature value corresponding to the expansion water tank; calculating the gas volume in the expansion water tank according to the total volume, the cooling liquid temperature value, the newly-increased heat value and the current gas pressure value; the difference between the total volume and the gas volume is calculated and taken as the cooling liquid level.

In some embodiments of the present application, based on the foregoing, the monitoring device 900 applied to the cooling system further includes a self-checking module configured to: before a new heat value corresponding to the expansion water tank is obtained, executing a self-checking program corresponding to an adjusting part in the cooling system; wherein, when the regulating part is the water pump, the self-checking procedure includes: the rotating speed of a water pump in the cooling system is adjusted to be a calibrated rotating speed; when the obtained current rotating speed of the water pump reaches the calibrated rotating speed, obtaining the working current of the water pump, and determining the dry rotating current of the water pump based on the current rotating speed; if the working current does not exceed the dry rotation current, a first fault signal for representing the fault of the water pump is sent out; when the adjusting component is a temperature control module, the self-checking program comprises: adjusting the rotation angle of a temperature control module in the cooling system to be a calibration rotation angle; when the acquired real-time rotation angle of the temperature control module reaches the calibration rotation angle, adjusting the current torque of the temperature control module to a preset torque, and calculating the difference between the real-time rotation angle of the temperature control module and the calibration rotation angle; and if the difference value between the real-time rotation angle and the calibration rotation angle exceeds the preset rotation angle deviation value, a second fault signal for representing the fault of the temperature control module is sent.

It should be noted that, the monitoring device 900 applied to the cooling system provided in the foregoing embodiment and the monitoring method applied to the cooling system provided in the foregoing embodiment belong to the same concept, and the specific manner in which each module and unit perform the operation has been described in detail in the method embodiment, which is not repeated herein.

Embodiments of the present application also provide an electronic device comprising a processor and a memory, wherein the memory has stored thereon computer readable instructions which, when executed by the processor, implement a monitoring method as described above for a cooling system.

Fig. 10 shows a schematic diagram of a computer system suitable for use in implementing an embodiment of the application.

It should be noted that, the computer system 1000 of the electronic device shown in fig. 10 is only an example, and should not impose any limitation on the functions and the application scope of the embodiments of the present application.

As shown in fig. 10, the computer system 1000 includes a central processing unit (Centra lProcessing Unit, CPU) 1001 that can perform various appropriate actions and processes, such as performing the method described in the above embodiment, according to a program stored in a read-only memory (ROM) 1002 or a program loaded from a storage portion 1008 into a random access memory (Random Access Memory, RAM) 1003. In the RAM 1003, various programs and data required for system operation are also stored. The CPU 1001, ROM 1002, and RAM 1003 are connected to each other by a bus 1004. An Input/Output (I/O) interface 1005 is also connected to bus 1004.

The following components are connected to the I/O interface 1005: an input section 1006 including a keyboard, a mouse, and the like; an output portion 1007 including a Cathode Ray Tube (CRT), a Liquid crystal display (Liquid CRYSTA LDISPLAY, LCD), and a speaker, etc.; a storage portion 1008 including a hard disk or the like; and a communication section 1009 including a network interface card such as a LAN (Loca lArea Network ) card, a modem, or the like. The communication section 1009 performs communication processing via a network such as the internet. The drive 1010 is also connected to the I/O interface 1005 as needed. A removable medium 1011, such as a magnetic disk, an optical disk, a magneto-optical disk, a semiconductor memory, or the like, is installed as needed in the drive 1010, so that a computer program read out therefrom is installed as needed in the storage section 1008.

In particular, according to embodiments of the present application, the processes described above with reference to flowcharts may be implemented as computer software programs. For example, embodiments of the present application include a computer program product comprising a computer program embodied on a computer readable medium, the computer program comprising a computer program for performing the method shown in the flowchart. In such an embodiment, the computer program may be downloaded and installed from a network via the communication portion 1009, and/or installed from the removable medium 1011. When executed by a Central Processing Unit (CPU) 1001, the computer program performs various functions defined in the system of the present application.

It should be noted that, the computer readable medium shown in the embodiments of the present application may be a computer readable signal medium or a computer readable storage medium, or any combination of the two. The computer readable storage medium can be, for example, but not limited to, an electronic, magnetic, optical, electromagnetic, infrared, or semiconductor system, apparatus, or device, or a combination of any of the foregoing. More specific examples of the computer-readable storage medium may include, but are not limited to: an electrical connection having one or more wires, a portable computer diskette, a hard disk, a Random Access Memory (RAM), a read-only memory (ROM), an erasable programmable read-only memory (Erasable Programmable Read Only Memory, EPROM), a flash memory, an optical fiber, a portable compact disc read-only memory (CD-ROM), an optical storage device, a magnetic storage device, or any suitable combination of the foregoing. In the context of this document, a computer readable storage medium may be any tangible medium that can contain, or store a program for use by or in connection with an instruction execution system, apparatus, or device. In the present application, however, a computer-readable signal medium may include a data signal propagated in baseband or as part of a carrier wave, with a computer-readable computer program embodied therein. Such a propagated data signal may take any of a variety of forms, including, but not limited to, electro-magnetic, optical, or any suitable combination of the foregoing. A computer readable signal medium may also be any computer readable medium that is not a computer readable storage medium and that can communicate, propagate, or transport a program for use by or in connection with an instruction execution system, apparatus, or device. A computer program embodied on a computer readable medium may be transmitted using any appropriate medium, including but not limited to: wireless, wired, etc., or any suitable combination of the foregoing.

The flowcharts and block diagrams in the figures illustrate the architecture, functionality, and operation of possible implementations of systems, methods and computer program products according to various embodiments of the present application. Where each block in the flowchart or block diagrams may represent a module, segment, or portion of code, which comprises one or more executable instructions for implementing the specified logical function(s). It should also be noted that, in some alternative implementations, the functions noted in the block may occur out of the order noted in the figures. For example, two blocks shown in succession may, in fact, be executed substantially concurrently, or the blocks may sometimes be executed in the reverse order, depending upon the functionality involved. It will also be noted that each block of the block diagrams or flowchart illustration, and combinations of blocks in the block diagrams or flowchart illustration, can be implemented by special purpose hardware-based systems which perform the specified functions or acts, or combinations of special purpose hardware and computer instructions.

The units involved in the embodiments of the present application may be implemented by software, or may be implemented by hardware, and the described units may also be provided in a processor. Wherein the names of the units do not constitute a limitation of the units themselves in some cases.

As another aspect, the present application also provides a computer-readable storage medium that may be contained in the electronic device described in the above embodiment; or may exist alone without being incorporated into the electronic device. The computer-readable storage medium carries one or more programs which, when executed by the electronic device, cause the electronic device to implement the methods described in the above embodiments.

It should be noted that although in the above detailed description several modules or units of a device for action execution are mentioned, such a division is not mandatory. Indeed, the features and functions of two or more modules or units described above may be embodied in one module or unit in accordance with embodiments of the application. Conversely, the features and functions of one module or unit described above may be further divided into a plurality of modules or units to be embodied.

From the above description of embodiments, those skilled in the art will readily appreciate that the example embodiments described herein may be implemented in software, or may be implemented in software in combination with the necessary hardware. Thus, the technical solution according to the embodiments of the present application may be embodied in the form of a software product, which may be stored in a non-volatile storage medium (may be a CD-ROM, a U-disk, a mobile hard disk, etc.) or on a network, and includes several instructions to cause a computing device (may be a personal computer, a server, a touch terminal, or a network device, etc.) to perform the method according to the embodiments of the present application.

Other embodiments of the application will be apparent to those skilled in the art from consideration of the specification and practice of the embodiments disclosed herein. This application is intended to cover any variations, uses, or adaptations of the application following, in general, the principles of the application and including such departures from the present disclosure as come within known or customary practice within the art to which the application pertains.

It is to be understood that the application is not limited to the precise arrangements and instrumentalities shown in the drawings, which have been described above, and that various modifications and changes may be effected without departing from the scope thereof. The scope of the application is limited only by the appended claims.

Claims

1. A monitoring method applied to a cooling system, comprising:

acquiring a new heat increment value and a current gas pressure value corresponding to an expansion water tank in a cooling system;

Determining the liquid level of the cooling liquid corresponding to the expansion water tank based on the new heat increment value and the current gas pressure value;

and if the liquid level of the cooling liquid does not exceed the preset liquid level threshold of the expansion water tank, sending an alarm signal for representing the leakage of the cooling liquid in the cooling system.

2. The method of claim 1, wherein the cooling system includes a heat generating component and a heat dissipating component, the expansion tank includes a first water inlet in communication with a bypass port of the heat generating component and a second water inlet in communication with a bypass port of the heat dissipating component, and the obtaining the new heat increment value and the current gas pressure value corresponding to the expansion tank in the cooling system includes:

respectively obtaining the flow rate of the cooling liquid branch and the temperature value of the cooling liquid branch, which correspond to the first water inlet and the second water inlet respectively;

Acquiring a cooling liquid discharge temperature value of the expansion water tank;

And calculating the new heat increment value according to the cooling liquid branch flow and the cooling liquid branch temperature value which are respectively corresponding to the first water inlet and the second water inlet and the cooling liquid discharge temperature value.

3. The method of claim 2, wherein the cooling system includes an adjustment component for controlling the flow of the cooling fluid, and wherein the obtaining the respective coolant branch flow and coolant branch temperature values of the first water inlet and the second water inlet includes:

Respectively determining the cooling liquid inflow amount corresponding to each of the heating component and the heat dissipation component based on the cooling liquid flow adjustment parameters of the adjustment component;

Acquiring the branch discharge flow ratio corresponding to each of the heating component and the heat dissipation component; the bypass discharge flow ratio represents the ratio of the cooling liquid to be discharged to the expansion water tank in the cooling liquid inflow;

And calculating the cooling liquid branch flow corresponding to each of the first water inlet and the second water inlet according to the cooling liquid inflow and branch discharge flow ratio corresponding to each of the heating component and the heat radiating component.

4. A method according to claim 3, wherein the determining the respective amounts of coolant inflow of the heat generating component and the heat radiating component based on the coolant flow adjustment parameters of the adjustment component, respectively, includes:

Determining the theoretical inflow of the cooling liquid corresponding to each of the heating component and the heat dissipation component based on the cooling liquid flow regulation parameters;

Acquiring a water inlet correction coefficient corresponding to the heating component at the current heating temperature;

And calculating the cooling liquid inflow rate corresponding to each of the heating component and the heat dissipation component according to the theoretical inflow rate of the cooling liquid corresponding to each of the heating component and the heat dissipation component and the inflow correction coefficient.

5. The method of claim 4, wherein the heat generating component comprises a plurality of heat generating cells, the obtaining a corresponding water inflow correction factor for the heat generating component at a current heat generating temperature comprising:

acquiring a cooling liquid discharge temperature value and a cooling liquid water inlet proportion corresponding to each heating unit; wherein, the cooling liquid water inlet proportion represents the ratio of the cooling liquid water inlet quantity of the heating unit in the total cooling liquid circulation quantity of the cooling system;

Calculating the comprehensive heating temperature according to the cooling liquid discharge temperature value and the cooling liquid water inlet proportion corresponding to each heating unit;

and determining the water inlet correction coefficient by taking the comprehensive heating temperature as the current heating temperature of the heating component.

6. The method of claim 2, wherein the obtaining the respective coolant branch flow and coolant branch temperature values for the first water inlet and the second water inlet, respectively, comprises:

respectively acquiring discharge length information, a cooling liquid inlet temperature value and a cooling liquid discharge temperature value corresponding to the heating component and the radiating component; wherein the discharge length information comprises a discharge distance from a water inlet to a branch port and a discharge distance from the water inlet to the discharge port, which are respectively corresponding to the heating component and the heat dissipation component;

And calculating the cooling liquid branch temperature values corresponding to the first water inlet and the second water inlet according to the discharge length information, the cooling liquid inlet temperature value and the cooling liquid discharge temperature value corresponding to the heating component and the heat radiating component respectively.

7. The method of claim 1, wherein after the determining the corresponding coolant level of the expansion tank based on the new heat increment value and the current gas pressure value, the method further comprises:

Starting timing when the liquid level of the cooling liquid is between the liquid level threshold and a safety liquid level threshold preset by the expansion water tank, and calculating a liquid level deviation value of the expansion water tank if the timing duration reaches a preset duration;

And if the liquid level deviation value exceeds a preset safety threshold, sending out the alarm signal.

8. The method of claim 7, wherein the calculating a liquid level deviation value of the expansion tank comprises:

Circularly executing the steps of responding to a water inlet signal corresponding to the expansion water tank to obtain a current gas pressure value in the expansion water tank and calculating a difference value between the current gas pressure value and a preset gas pressure threshold value until the timing duration reaches the preset duration;

And calculating an accumulated value of each difference value calculated in the step of circularly executing, and taking the accumulated value as the liquid level deviation value.

9. The method of claim 1, wherein the determining a corresponding coolant level of the expansion tank based on the new heat increment value and the current gas pressure value comprises:

acquiring the total volume and the cooling liquid temperature value corresponding to the expansion water tank;

Calculating the gas volume in the expansion water tank according to the total volume, the cooling liquid temperature value, the new heat increment value and the current gas pressure value;

and calculating a difference between the total volume and the gas volume, and taking the difference as the liquid level of the cooling liquid.

10. The method according to claim 1, wherein the method further comprises:

Before a new heat value corresponding to an expansion water tank in a cooling system is acquired, executing a self-checking program corresponding to an adjusting part in the cooling system;

Wherein, when the regulating component is a water pump, the self-checking procedure includes:

if the working current does not exceed the dry rotation current, a first fault signal for representing the fault of the water pump is sent out;

When the adjusting component is a temperature control module, the self-checking program includes:

And if the difference value between the real-time rotation angle and the calibration rotation angle exceeds a preset rotation angle deviation value, a second fault signal used for representing the fault of the temperature control module is sent out.