Server liquid cooling method

Abstract

The invention provides a server liquid cooling method. The server liquid cooling method comprises the following steps that a sensor detects the temperature T1 of a first pipeline in real time; the control system compares T1 with T, and if T1 is smaller than T, the first pipeline is kept running; if T1 is larger than T, the second pipeline is operated while the first pipeline is operated; when T1 is smaller than TS, operation of the second pipeline is stopped; the sensor detects the fluid pressure P1 of the first pipeline in real time; the control system records a fluid pressure special point P2; the control system maintains normal pipeline fluid pressure; the turbine flow L1 of the first pipeline is detected in real time; the control system compares L1 with L, if L1 is smaller than LS, whether the main pump body in the first pipeline operates normally or not is detected, and if the main pump body is abnormal, the auxiliary pump body operates at the same time; if L1 is larger than L, part of the second pipeline is opened; and when L1 is equal to LS, the second pipeline is closed. According to the invention, the problems of poor cooling efficiency and high energy consumption of liquid cooling equipment in the prior art are solved.

Description

Technical Field

[0001] The present invention relates to the technical field of servers, and in particular to a server liquid cooling method. Background Art

[0002] As the requirements for server performance continue to increase, server heat dissipation has become a key and difficult issue. Due to the complex structure of the server system, conventional air cooling can no longer meet its heat dissipation needs. Liquid cooling solutions have better heat dissipation performance than air cooling solutions.

[0003] In existing liquid cooling, the cooling pipelines often work at full load and cannot be adjusted according to the server status. The cooling efficiency is poor and it also brings a heavy load to the circuit of the computer room, consumes a lot of energy, and there is a risk of circuit overload, which is not conducive to the normal operation of the server. Summary of the invention

[0004] The invention solves the problem of poor cooling efficiency and high energy consumption of liquid cooling equipment in the prior art.

[0005] In order to solve the above problems, the present invention provides a server liquid cooling method, which is applied to a server liquid cooling system. The server liquid cooling system comprises: a first pipeline, the first pipeline comprises at least two pump bodies, and the first pipeline is normally open; a second pipeline, the second pipeline is normally closed, and is used to assist the first pipeline in cooling and to adjust the pipeline fluid pressure and flow. The server liquid cooling method comprises the following steps: Set the cooling temperature threshold T and cooling temperature standard value T S , cooling line fluid pressure threshold value P, cooling line fluid pressure standard value P S And turbine flow threshold L, turbine flow standard value L S ; The sensor detects the first pipe temperature T in real time 1 ; Control System Comparison 1 With T size, if T 1 <T, keep the first pipeline running; if T 1 >T, then keep the first pipeline running while running the second pipeline; When T 1 <T S When the second pipeline is stopped; The sensor detects the first pipeline fluid pressure P in real time 1 ; The control system records the fluid pressure at a specific point P 2 ; The control system maintains normal pipeline fluid pressure; Real-time detection of the first pipeline turbine flow L 1 ; Control System Comparison 1 and L size, if L 1 <L S , then check whether the main pump body in the first pipeline is operating normally. If the main pump body is abnormal, the auxiliary pump body will be operated at the same time; if L 1 >L, then part of the second pipeline is opened; When L 1 =L S When , close the second pipeline; Among them, T>T S , P>P S , L>L S .

[0006] Compared with the prior art, the technical effect achieved by this technical solution is: through at least two pump bodies, one is used as the main pump body and is always running, and the other pump body is used as the auxiliary pump body, the auxiliary pump body is kept normally closed, and the second pipeline assists the first pipeline in liquid cooling, and the second pipeline is always closed to achieve the effect of adjusting the liquid cooling system according to the server status and saving energy. 1 When the cooling temperature threshold T is exceeded, the second pipeline is opened and the auxiliary pump is operated to assist the liquid cooling of the first pipeline. Detect the fluid pressure P of the first pipeline 1 And record the fluid pressure at special point P 2 , as the basis for the control system to open the second pipeline to adjust the fluid pressure, so as to maintain the normal fluid pressure of the entire pipeline. Under normal circumstances, running the main pump body alone can make the turbine flow rate L of the first pipeline 1 Maintain at normal value, i.e. L S <L 1 <L, so when the turbine flow rate of the first pipeline is L 1 Less than the turbine flow standard value L S When the turbine flow rate L of the first pipeline is 1 When it is greater than the turbine flow threshold value L, the control system opens the second pipeline to divert the flow to maintain normal turbine flow.

[0007] Furthermore, the control system is compared with L 1 and L size, specifically including: if L 1 =0, the main pump body is stopped and the auxiliary pump body is started.

[0008] Compared with the prior art, the technical effect achieved by this technical solution is: when L 1 =0, the main pump body is judged to be completely damaged, and the control system shuts down the main pump body in time to avoid unnecessary energy consumption.

[0009] Furthermore, the control system maintains the normal pressure of the pipeline fluid, specifically including: the control system records the fluid pressure at the special point P 2The time of occurrence, at the special point P of fluid pressure 2 Open the second pipeline during the concentrated period of time; compare the fluid pressure P of the first pipeline 1 The standard value of the cooling pipeline fluid pressure P S size.

[0010] Compared with the prior art, the technical effect achieved by this technical solution is: in order to avoid high-frequency opening and closing of the valve related to the second pipeline when maintaining the pipeline fluid pressure, the second pipeline is set to have a large fluctuation in the pipeline fluid pressure, that is, the fluid pressure special point P 2 The first pipeline fluid pressure P 1 The standard value of the cooling pipeline fluid pressure P S The size of the first pipeline fluid pressure P 1 of the changing situation.

[0011] Furthermore, the server liquid cooling system further includes: a heat exchanger; a liquid storage tank connected to the heat exchanger by a pipeline; a first pipeline connecting the pump body and the heat exchanger; a second pipeline including an auxiliary pipeline, and the starting end and the end of the second pipeline are both connected to the heat exchanger; if T 1 >T, then the first pipeline is kept running while the second pipeline is running, specifically including: at least two pump bodies in the first pipeline work simultaneously, the second pipeline is partially opened, and the auxiliary pipeline valve remains closed.

[0012] Compared with the prior art, the technical effect achieved by the present technical solution is as follows: when the temperature of the first pipeline is higher than the cooling temperature threshold, the auxiliary pump body is started, the main pump body and the auxiliary pump body run at the same time, and the second pipeline is opened to enhance the liquid cooling effect on the server, and the auxiliary pipeline valve remains closed to keep the fluid pressure in the pipeline and the pipeline turbine flow stable.

[0013] Furthermore, the first pipeline includes: a first liquid supply pipe and a first liquid return pipe. One end of the first liquid supply pipe is connected to the pump body; one end of the first liquid return pipe is connected to the heat exchanger; the sensor detects the fluid pressure P of the first pipeline in real time 1 Including: The sensor detects the fluid pressure P of the first return pipe in real time 1 ; The control system records the fluid pressure at a special point P 2 Includes: Control System Comparison P 1 and the size of P, if P 1 >P, then it is judged to be a special point of fluid pressure P 2 And record the fluid pressure at special point P 2 Appearance time; if P 1 <P, it is judged as a normal point.

[0014] Compared with the prior art, the technical effect achieved by this technical solution is: to achieve the special point P of fluid pressure2 judgment and record.

[0015] Furthermore, the second pipeline includes: a second liquid supply pipe and a second liquid return pipe. One end of the second liquid supply pipe is connected to the heat exchanger; one end of the second liquid return pipe is connected to the heat exchanger; an auxiliary pipeline connects the second liquid supply pipe and the second liquid return pipe; the control system maintains the normal pressure of the pipeline fluid including: the control system controls the fluid pressure according to the recorded special point P 2 The time of occurrence, at the special point P of fluid pressure 2 The second liquid supply pipe, the second liquid return pipe and the auxiliary pipeline are opened during the concentrated time period.

[0016] Compared with the prior art, the technical effect achieved by the present technical solution is as follows: the second liquid supply pipe, the auxiliary pipeline and the second liquid return pipe form a pipeline loop, so that the coolant is diverted through the auxiliary pipeline to achieve the purpose of regulating the pipeline fluid pressure.

[0017] Further, comparing the first pipeline fluid pressure P 1 The standard value of the cooling pipeline fluid pressure P S The size of P 1 =P S When the control system closes the second liquid supply pipe, the second liquid return pipe and the auxiliary pipeline.

[0018] Compared with the prior art, the technical effect achieved by the present technical solution is as follows: when the fluid pressure in the first pipeline returns to the standard value, the second liquid supply pipe, the auxiliary pipeline and the second liquid return pipe are closed to form a pipeline loop, thereby preventing the fluid pressure in the first pipeline from being too low or the pump body from overloading to maintain the fluid pressure in the pipeline.

[0019] Furthermore, the server liquid cooling system further includes: a first outer tube and a second outer tube. The first outer tube connects the first liquid supply tube and the first liquid return tube; the second outer tube connects the second liquid supply tube and the second liquid return tube; and the turbine flow rate L of the first pipeline is detected in real time. 1 Including: detecting the first outer pipe turbine flow L 1 ; If L 1 >L, then opening part of the second pipeline includes: opening the auxiliary pipeline valve and detecting the turbine flow rate L of the first outer pipe 1 Change, if L 1 If there is no change or increase, open the second outer tube valve.

[0020] Compared with the prior art, the technical effects achieved by the technical solution are as follows: the first outer tube and the second outer tube pass through the server components to achieve liquid cooling effect on the server, the turbine flow at the first outer tube is relatively stable and accurate, and the auxiliary pipeline is opened when the turbine flow of the first outer tube is too large to divert flow. If the turbine flow of the first outer tube does not show a downward trend after the auxiliary pipeline is opened, it is determined that the auxiliary pipeline is faulty, and the second outer tube is opened to achieve the diversion effect.

[0021] Furthermore, the sensor detects the first pipe temperature T in real time. 1 , specifically including: the sensor detects the first return liquid pipe temperature T in real time 1 .

[0022] Compared with the prior art, the technical effect achieved by the technical solution is as follows: the cooling liquid passes through the first liquid supply pipe and the first outer pipe. After cooling the server, the cooling liquid temperature rises and flows back into the first liquid return pipe. The cooling liquid temperature at the first liquid return pipe can accurately reflect the temperature conditions of the components in the server.

[0023] Furthermore, the server liquid cooling method also includes: fault alarm, when the main pump body and the auxiliary pump body both fail to work, the control system alarms.

[0024] Compared with the prior art, the technical effect achieved by this technical solution is that it is convenient for manual maintenance to be carried out in a timely manner. BRIEF DESCRIPTION OF THE DRAWINGS

[0025] Figure 1 A flow chart of the server liquid cooling method provided by the present invention; Figure 2 A structural diagram of a server liquid cooling system used in the server liquid cooling method provided by the present invention; Figure 3 is a schematic diagram of the first pipeline structure; Figure 4 Schematic diagram of the second pipeline structure.

[0026] Description of reference numerals: 1-first pipeline; 11-first liquid supply pipe; 12-first liquid return pipe; 2-second pipeline; 21-auxiliary pipeline; 22-second liquid supply pipe; 23-second liquid return pipe; 3-heat exchanger; 4-liquid storage tank. DETAILED DESCRIPTION

[0027] The object of the present invention is to provide a server liquid cooling method for improving the cooling efficiency of a cooling system and achieving energy-saving effects.

[0028] In order to make the above-mentioned objects, features and advantages of the present invention more obvious and easy to understand, specific embodiments of the present invention are described in detail below with reference to the accompanying drawings.

[0029] like Figure 1 , Figure 2 As shown, the present invention provides a server liquid cooling method, which is applied to a server liquid cooling system. The server liquid cooling system includes: a first pipeline 1, the first pipeline 1 includes at least two pump bodies, and the first pipeline 1 is normally open; a second pipeline 2, the second pipeline 2 is normally closed, and is used to assist the first pipeline 1 in cooling and to adjust the pipeline fluid pressure and flow. The server liquid cooling method includes the following steps: Set the cooling temperature threshold T and cooling temperature standard value T S , cooling line fluid pressure threshold value P, cooling line fluid pressure standard value P S And turbine flow threshold L, turbine flow standard value L S ; The sensor detects the temperature T of the first pipeline 1 in real time 1 ; Control System Comparison 1 With T size, if T 1 <T, keep the first pipeline 1 running; if T 1 >T, then keep the first pipeline 1 running while running the second pipeline 2; When T 1 <T S When the second pipeline 2 is stopped; The sensor detects the fluid pressure P of the first pipeline 1 in real time 1 ; The control system records the fluid pressure at a specific point P 2 ; The control system maintains normal pipeline fluid pressure; Real-time detection of the turbine flow rate L of the first pipeline 1 1 ; Control System Comparison 1 and L size, if L 1 <L S , then check whether the main pump body in the first pipeline 1 is operating normally. If the main pump body is abnormal, the auxiliary pump body will be operated at the same time; if L 1 >L, then part of the second pipeline 2 is opened; When L 1 =L S When , close the second pipeline 2; Among them, T>T S , P>P S , L>L S .

[0030] At least two pump bodies are used, one of which is used as the main pump body and is always running, and the other pump bodies are used as auxiliary pump bodies. The auxiliary pump bodies are kept normally closed. The second pipeline 2 assists the first pipeline 1 in liquid cooling. The second pipeline 2 is normally closed to achieve the effect of adjusting the liquid cooling system according to the server status and saving energy. When the temperature of the first pipeline 1 is T 1 When the cooling temperature threshold T is exceeded, the second pipeline 2 is opened and the auxiliary pump is operated to assist the liquid cooling of the first pipeline 1. Detect the fluid pressure P of the first pipeline 1 1 And record the fluid pressure at special point P 2, as the basis for the control system to open the second pipeline 2 to adjust the fluid pressure, so as to maintain the normal fluid pressure of the entire pipeline. Under normal circumstances, running the main pump body alone can make the turbine flow L of the first pipeline 1 1 Maintain at normal value, i.e. L S <L 1 <L, so when the turbine flow rate of the first pipeline 1 is L 1 Less than the turbine flow standard value L S When the turbine flow rate L in the first pipeline 1 is 1 When it is greater than the turbine flow threshold value L, the control system opens the second pipeline 2 to divert the flow to maintain normal turbine flow.

[0031] Control System Comparison 1 and L size, specifically including: if L 1 =0, the main pump body is stopped and the auxiliary pump body is started.

[0032] Optionally, there may be one or more auxiliary pump bodies, and the auxiliary pump bodies are connected in parallel with the main pump body.

[0033] When L 1 =0, the main pump body is judged to be completely damaged, and the control system shuts down the main pump body in time to avoid unnecessary energy consumption.

[0034] The control system maintains the normal fluid pressure in the pipeline, specifically including: the control system records the fluid pressure at the special point P 2 The time of occurrence, at the special point P of fluid pressure 2 Open the second pipeline 2 during the concentrated period; compare the fluid pressure P of the first pipeline 1 1 The standard value of the cooling pipeline fluid pressure P S size.

[0035] Specifically, the fluid pressure at a special point P 2 The concentrated time period can be calculated by counting the special points P of fluid pressure in hours. 2 The number of occurrences, select the special point P of fluid pressure 2 The time period with the largest number of occurrences is used.

[0036] In order to avoid high-frequency opening and closing of the valves related to the second pipeline 2 when maintaining the pipeline fluid pressure, the second pipeline 2 is set to have a large fluctuation in the pipeline fluid pressure, that is, the fluid pressure special point P 2 The first pipeline 1 fluid pressure P 1 The standard value of the cooling pipeline fluid pressure P S The size of the first pipeline 1 is used to detect the fluid pressure P 1of the changing situation.

[0037] The server liquid cooling system also includes: a heat exchanger 3; a liquid storage tank 4, which is connected to the heat exchanger 3 by a pipeline; a first pipeline 1 connecting the pump body and the heat exchanger 3; a second pipeline 2 including an auxiliary pipeline 21, and the starting end and the end of the second pipeline 2 are both connected to the heat exchanger 3; if T 1 >T, then the first pipeline 1 is kept running while the second pipeline 2 is running, specifically including: at least two pump bodies in the first pipeline 1 work simultaneously, the second pipeline 2 is partially opened, and the valve of the auxiliary pipeline 21 remains closed.

[0038] When the temperature of the first pipeline 1 is higher than the cooling temperature threshold, the auxiliary pump body is started, the main pump body and the auxiliary pump body run at the same time, and the second pipeline 2 is opened to enhance the liquid cooling effect on the server. The valve of the auxiliary pipeline 21 remains closed to keep the fluid pressure in the pipeline and the pipeline turbine flow stable.

[0039] like Figure 3 As shown, the first pipeline 1 includes: a first liquid supply pipe 11 and a first liquid return pipe 12. One end of the first liquid supply pipe 11 is connected to the pump body; one end of the first liquid return pipe 12 is connected to the heat exchanger 3; the sensor detects the fluid pressure P of the first pipeline 1 in real time 1 Including: the sensor detects the pipeline fluid pressure P at the first return pipe 12 in real time 1 ; The control system records the fluid pressure at a special point P 2 Includes: Control System Comparison P 1 and the size of P, if P 1 >P, then it is judged to be a special point of fluid pressure P 2 And record the fluid pressure at special point P 2 Appearance time; if P 1 <P, it is judged as a normal point.

[0040] Realize the special point P of fluid pressure 2 judgment and record.

[0041] like Figure 4 As shown, the second pipeline 2 includes: a second liquid supply pipe 22 and a second liquid return pipe 23. One end of the second liquid supply pipe 22 is connected to the heat exchanger 3; one end of the second liquid return pipe 23 is connected to the heat exchanger 3; the auxiliary pipeline 21 connects the second liquid supply pipe 22 and the second liquid return pipe 23; the control system maintains the normal pressure of the pipeline fluid including: the control system according to the recorded fluid pressure special point P 2 The time of occurrence, at the special point P of fluid pressure 2 The second liquid supply pipe 22, the second liquid return pipe 23 and the auxiliary pipeline 21 are opened during the concentrated time period.

[0042] Among them, a valve is provided on the auxiliary pipeline 21, and the control system can control the opening and closing angle of the valve.

[0043] The second liquid supply pipe 22, the auxiliary pipeline 21 and the second liquid return pipe 23 form a pipeline loop, so that the coolant is diverted through the auxiliary pipeline 21 to achieve the purpose of regulating the pipeline fluid pressure.

[0044] Compare the first pipeline 1 fluid pressure P 1 The standard value of the cooling pipeline fluid pressure P S The size of P 1 =P S When the control system closes the second liquid supply pipe 22, the second liquid return pipe 23 and the auxiliary pipeline 21.

[0045] If P 1 =P S When the server liquid cooling system is still at the special fluid pressure point P 2 During the concentrated period of time, the control system will not reopen the pipeline loop composed of the second liquid supply pipe 22, the auxiliary pipeline 21 and the second liquid return pipe 23.

[0046] When the fluid pressure P in the first pipeline 1 1 When returning to the standard value, the second liquid supply pipe 22, the auxiliary pipeline 21 and the second liquid return pipe 23 are closed to form a pipeline loop to prevent the fluid pressure in the first pipeline 1 from being too low or the pump body from overloading to maintain the pipeline fluid pressure.

[0047] The server liquid cooling system also includes: a first outer tube and a second outer tube. The first outer tube connects the first liquid supply tube 11 and the first liquid return tube 12; the second outer tube connects the second liquid supply tube 22 and the second liquid return tube 23; real-time detection of the turbine flow rate L of the first pipeline 1 Including: detecting the first outer pipe turbine flow L 1 ; If L 1 >L, then opening part of the second pipeline 2 includes: opening the valve of the auxiliary pipeline 21 and detecting the turbine flow rate L of the first outer pipe 1 Change, if L 1 If there is no change or increase, open the second outer tube valve.

[0048] The second outer pipe has a longer stroke than the auxiliary pipe 21 .

[0049] The first outer tube and the second outer tube pass through the server components to achieve a liquid cooling effect on the server. The turbine flow at the first outer tube is relatively stable and accurate. The auxiliary pipeline 21 is opened when the turbine flow of the first outer tube is too large to divert the flow. If the turbine flow of the first outer tube does not show a downward trend after the auxiliary pipeline 21 is opened, it is determined that the auxiliary pipeline 21 is faulty, and the second outer tube is opened to achieve a diversion effect.

[0050] The sensor detects the temperature T of the first pipeline 1 in real time 1 Specifically, the sensor detects the temperature T of the first liquid return pipe 12 in real time.1 .

[0051] The cooling liquid passes through the first liquid supply pipe 11 and the first outer pipe. After cooling the server, the cooling liquid temperature increases and flows back into the first liquid return pipe 12. The cooling liquid temperature at the first liquid return pipe 12 can accurately reflect the temperature status of the components in the server.

[0052] The server liquid cooling method also includes: a fault alarm, when both the main pump body and the auxiliary pump body fail to work, the control system alarms.

[0053] Specifically, when the auxiliary pump is running, the turbine flow rate L of the first pipeline 1 is 1 Less than the turbine flow standard value L S When the auxiliary pump fails, the control system determines that the auxiliary pump is faulty.

[0054] After determining that the auxiliary pump body is faulty, the control system should promptly shut down the auxiliary pump body, close the second outer pipe valve and the auxiliary pipeline 21 valve to prevent the second pipeline 2 liquid from reflux and leaking during the maintenance process, and alarm to facilitate manual maintenance in a timely manner.

[0055] Although the present invention is disclosed as above, the present invention is not limited thereto. Any person skilled in the art can make various changes and modifications without departing from the spirit and scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the scope defined by the claims.

Claims

1. A server liquid cooling method, characterized in that: Applied to a server liquid cooling system, the server liquid cooling system comprises: a first pipeline, the first pipeline comprises at least two pump bodies, the first pipeline is normally open; a second pipeline, the second pipeline is normally closed, and is used to assist the first pipeline in cooling and to adjust the pipeline fluid pressure and flow rate. The server liquid cooling method comprises the following steps: Set the cooling temperature threshold T and cooling temperature standard value T S , cooling line fluid pressure threshold value P, cooling line fluid pressure standard value P S And turbine flow threshold L, turbine flow standard value L S ; The sensor detects the first pipeline temperature T1 in real time; The control system compares T1 with T. If T1 < T, the first pipeline is kept running; if T1 > T, the first pipeline is kept running while the second pipeline is run. When T1<T S When the second pipeline is stopped; The sensor detects the first pipeline fluid pressure P1 in real time; The control system records the special point P2 of fluid pressure; The control system maintains normal fluid pressure in the pipeline; Real-time detection of the turbine flow rate L1 of the first pipeline; The control system compares L1 and L. If L1 < L S , then check whether the main pump body in the first pipeline is operating normally. If the main pump body is abnormal, the auxiliary pump body will be operated at the same time; if L1>L, part of the second pipeline will be opened; When L1=L S When , close the second pipeline; Among them, T>T S , P>P S , L>L S .

2. The server liquid cooling method according to claim 1, characterized in that: The control system compares L1 with L, and specifically includes: if L1=0, the main pump body is stopped and the auxiliary pump body is operated.

3. The server liquid cooling method according to claim 2, characterized in that: The control system maintains normal pipeline fluid pressure, specifically including: The control system opens the second pipeline in a time period when the special fluid pressure point P2 appears according to the recorded time when the special fluid pressure point P2 appears; Compare the first pipeline fluid pressure P1 with the cooling pipeline fluid pressure standard value P S size.

4. The server liquid cooling method according to claim 3, characterized in that: Applicable to a server liquid cooling system, the server liquid cooling system further comprises: a heat exchanger; a liquid storage tank connected to the heat exchanger by a pipeline; the first pipeline connects the pump body and the heat exchanger; the second pipeline comprises an auxiliary pipeline, and the starting end and the end of the second pipeline are both connected to the heat exchanger; If T1>T, the first pipeline is kept running while the second pipeline is running, which specifically includes: at least two pump bodies in the first pipeline work simultaneously, the second pipeline is partially opened, and the auxiliary pipeline valve remains closed.

5. The server liquid cooling method according to claim 4, characterized in that: Applied to a server liquid cooling system, the first pipeline includes: a first liquid supply pipe, one end of which is connected to the pump body; a first liquid return pipe, one end of which is connected to the heat exchanger; The sensor detecting the first pipeline fluid pressure P1 in real time comprises: the sensor detecting the pipeline fluid pressure P1 at the first liquid return pipe in real time; The control system records the special fluid pressure point P2, including: the control system compares the sizes of P1 and P, if P1>P, it is judged as the special fluid pressure point P2 and records the appearance time of the special fluid pressure point P2; if P1<P, it is judged as a normal point.

6. The server liquid cooling method according to claim 5, characterized in that: Applied to the server liquid cooling system, the second pipeline includes: a second liquid supply pipe, one end of which is connected to the heat exchanger; a second liquid return pipe, one end of which is connected to the heat exchanger; the auxiliary pipeline connects the second liquid supply pipe and the second liquid return pipe; The control system maintains normal pipeline fluid pressure including: the control system opens the second liquid supply pipe, the second liquid return pipe and the auxiliary pipeline during the time period when the special fluid pressure point P2 appears according to the recorded time when the special fluid pressure point P2 appears.

7. The server liquid cooling method according to claim 6, characterized in that: The comparison of the first pipeline fluid pressure P1 with the cooling pipeline fluid pressure standard value P S The size of the When P1=P S When the control system closes the second liquid supply pipe, the second liquid return pipe and the auxiliary pipeline.

8. The server liquid cooling method according to claim 7, characterized in that: Applicable to a server liquid cooling system, the server liquid cooling system further comprises: a first outer tube, the first outer tube connecting the first liquid supply tube and the first liquid return tube; a second outer tube, the second outer tube connecting the second liquid supply tube and the second liquid return tube; The real-time detection of the first pipeline turbine flow rate L1 comprises: detecting the first outer pipe turbine flow rate L1; If L1>L, opening part of the second pipeline includes: opening the auxiliary pipeline valve and detecting the change of the first outer pipe turbine flow L1, and if L1 does not change or increases, opening the second outer pipe valve.

9. The server liquid cooling method according to claim 8, characterized in that: The sensor detects the first pipeline temperature T1 in real time, specifically including: the sensor detects the first liquid return pipe pipeline temperature T1 in real time.

10. The server liquid cooling method according to any one of claims 1 to 9, characterized in that: Also includes: Fault alarm: when both the main pump body and the auxiliary pump body fail to work, the control system alarms.

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