Separating and cooling system for gas and particles in transformer oil

Through the combination of oil and gas separation, particulate separation and cooling devices, the problems of gas and particulate separation and cooling in transformer oil are solved, and efficient purification and cooling of oil is achieved to ensure stable operation of the equipment.

CN120261120APending Publication Date: 2025-07-04JIANGSU FRONTIER ELECTRIC TECH
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Patent Information

Application Number
CN202510417701.3
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-04-03
Publication Date
2025-07-04

AI Technical Summary

Technical Problem

The oxygen content and particle doping in the transformer oil will affect the quality and insulation performance of the oil, resulting in unstable equipment operation and it is difficult for the existing technology to effectively separate and cool down.

Method used

The oil and gas separation device, particulate separation device and cooling device are adopted to improve the oil and gas separation efficiency through the inverter and air isolation network, and the air pressure is stabilized using a one-way exhaust mechanism, the breathing component is accelerated separation, and the oil volume is ensured with the oil replenishment device, and the cooling device cools down.

Benefits of technology

Effectively removes gases and particles in transformer oil, prevents oil oxidation, reduces deterioration speed, maintains insulation performance, extends equipment life, and is simple in structure and convenient to operate.

✦ Generated by Eureka AI based on patent content.

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Abstract

The invention discloses a system for separating and cooling gas and particles in transformer oil, which comprises an oil-gas separation device, a particle separation device, a circulating pump, a cooling device and an oil supplementing device, an oil inlet mother pipe of the oil-gas separation device is communicated with a multi-path oil outlet pipe of a power heat source, the oil-gas separation device is connected with the cooling device, and the cooling device is connected with the particle separation device. Finally, an oil outlet main pipe is communicated with a multi-path oil inlet pipe of a power heat source; the oil supplementing device is used for supplementing oil for the circulating system; the oil-gas separation device further comprises a one-way exhaust mechanism and a breathing assembly, and can exhaust gas, stabilize pressure and accelerate oil-gas separation. Smoke and particles in industrial oil can be removed, grease is prevented from being oxidized, particle impurities are prevented from polluting the grease, meanwhile, high-temperature oil can be cooled in time, the degradation speed of the oil is reduced, and the insulation performance of the oil is reduced; the device is simple in structure and convenient to operate, oil in multiple oil ways of the power heat source can be subjected to degassing, impurity removal and cooling treatment, and practicability is high.
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Description

Technical Field:

[0001] The present invention belongs to the technical field of power system equipment, and particularly relates to a gas and particle separation and cooling system for transformer oil. Background Art:

[0002] A transformer is a very important device in the power system, and its normal operation depends on the good condition of each component. Among them, transformer oil, as an important component of the transformer, often contains oxygen and metal dust particles inside, and the temperature of the oil will rise as the equipment operates for a long time. However, when mixed with oxygen and particles, it will have a negative impact on the quality of transformer oil, thus affecting the operation of the equipment.

[0003] When the oxygen content in the transformer oil is too high, on the one hand, it will affect the decomposition of harmful components in the oil, accelerate the aging speed of the oil, and cause too many oxides to be generated in the transformer, damaging the equipment. On the other hand, the too high oxygen content will also cause the dielectric strength of the oil to drop sharply, thus affecting the insulation performance of the transformer. The metal dust particles in the transformer oil are in a suspended state and are difficult to separate from the oil. They are not sensitive to the metal content in the oil during the detection process, and it is also difficult to detect the metal content in the oil during the manufacturing and testing of high-voltage electrical products. Therefore, the metal dust particles in the oil constitute a potential pollution to the oil. In addition, too high an oil temperature will cause the transformer oil to crack into low-molecular hydrocarbons, resulting in a decrease in the flash point of the transformer oil. And the arc of partial discharge will carbonize the oil, deteriorating the insulation performance of the oil. When the average temperature of the transformer oil rises by 10°C, the deterioration speed of the oil increases by 2 times.

[0004] Therefore, we should pay attention to controlling the oxygen content and particle doping amount of the transformer oil, keep it within an appropriate range, and cool the oil in time to ensure the normal operation of the equipment. The present invention provides a gas and particle separation and cooling system for transformer oil to solve the above problems. Summary of the Invention:

[0005] The purpose of the present invention is to provide a gas and particle separation and cooling system for transformer oil in view of the deficiencies of the prior art.

[0006] The present invention adopts the following technical solutions:

[0007] The present invention provides a gas and particle separation and cooling system for transformer oil, including an oil-gas separation device, a particle separation device, and a cooling device; an oil inlet main pipe is arranged at the oil inlet end of the oil-gas separation device, and the oil inlet main pipe is communicated with a plurality of oil outlet pipes arranged by a power heat source; the oil outlet end of the oil-gas separation device is connected to the oil inlet end of the cooling device, the oil outlet end of the cooling device is connected to the oil inlet end of the particle separation device, and an oil outlet main pipe is arranged at the oil outlet end of the particle separation device, and the oil outlet main pipe is communicated with a plurality of oil inlet pipes arranged by a power heat source.

[0008] Further, the oil-gas separation device includes an oil-gas separation container, an inverter, and an air separation net; the inverter is a cylindrical structure with an open top and a hollow interior, and is fixedly arranged inside the oil-gas separation container; the air separation net is arranged inside the oil-gas separation container and is fixedly connected to the inner wall of the oil-gas separation container and the outer wall of the inverter respectively, dividing the oil-gas separation container into two spaces, and the oil inlet and the oil outlet of the oil-gas separation container are respectively arranged above and below the air separation net; the oil inlet main pipe is an inverted U-shaped pipe, one branch of the oil inlet main pipe passes through the oil inlet of the oil-gas separation container and extends to the lower part inside the inverter, and the other branch of the oil inlet main pipe is distributed outside the oil-gas separation container and is respectively connected to a plurality of outlet oil pipes of the power heat source.

[0009] Further, the oil-gas separation device further includes a one-way exhaust mechanism for one-way exhaust from inside to outside. The one-way exhaust mechanism is communicated with the oil-gas separation container through a pipeline, and the connection end of the one-way exhaust mechanism and the oil-gas separation container is distributed above the air separation net.

[0010] Further, the oil-gas separation device further includes a breathing component; the breathing component includes a balloon, an air delivery pipe, and an air pump; the balloon is arranged inside the oil-gas separation container, the air pump is arranged outside the oil-gas separation container, and the balloon and the air pump are connected through the air delivery pipe.

[0011] Further, the particle separation device includes a stainless steel pump housing, a first cathode, a second cathode, a U-shaped magnet, and at least one anode cylinder; the first cathode, the second cathode, and the anode cylinder are arranged inside the stainless steel pump housing, the first cathode and the second cathode are parallel to each other, and the anode cylinder is arranged between the first cathode and the second cathode; the U-shaped magnet is arranged outside the stainless steel pump housing, and the stainless steel pump housing is distributed between the two magnetic poles of the U-shaped magnet.

[0012] Further, the cooling device includes a heat exchanger and a refrigeration component; the heat exchanger is provided with a refrigerant circulation pipeline and a heat exchange flow channel, the refrigeration component includes a compressor, a condenser, a liquid storage tank, and an expansion valve, the outlet of the refrigerant circulation pipeline is sequentially connected to the compressor, the condenser, the liquid storage tank, and the expansion valve through pipelines, and the expansion valve is connected to the inlet of the refrigerant circulation pipeline through a pipeline; the circulating refrigerant in the refrigerant circulation pipeline cools the hot oil in the heat exchange flow channel, and the refrigerant after absorbing heat enters the compressor to form high-temperature and high-pressure gas, then enters the condenser to be condensed into liquid, and is stored in the liquid storage tank. The liquid refrigerant in the liquid storage tank enters the expansion valve for pressure reduction and temperature reduction, and then enters the refrigerant circulation pipeline again as a cold source to cool the hot oil in the heat exchange flow channel.

[0013] Furthermore, the device is also provided with a circulation pump; the circulation pumps are distributed between the oil-gas separation device and the cooling device, the inlet of the circulation pump is connected to the oil outlet pipe of the oil-gas separation device, and the outlet of the circulation pump is connected to the oil inlet pipe of the cooling device.

[0014] Furthermore, a temperature sensor and a pressure regulator are provided on the oil outlet pipe of the power heat source; a turbine flowmeter is provided on the oil inlet pipe of the power heat source; both the outlet pipe and the inlet pipe are insulating rubber hoses with cloth.

[0015] Furthermore, the device is also provided with an oil replenishing device; the oil replenishing device includes an oil barrel and an auxiliary oil barrel; the oil barrel is connected to the main oil inlet pipe through a first oil pipeline, and a fuel pump and a valve are provided on the first oil pipeline; the auxiliary oil barrel is connected to the oil barrel through a second oil pipeline, and an oil replenishing pump is provided on the second oil pipeline.

[0016] Furthermore, an oil return channel is provided between the auxiliary oil barrel and the oil barrel, both ends of the oil return channel are communicated with the auxiliary oil barrel and the oil barrel respectively, and an oil return valve is provided on the oil return channel.

[0017] Furthermore, the oil-gas separation container includes a detachable upper pipe body and a lower pipe body; both the gas separation net and the inverter are fixedly connected to the upper pipe body.

[0018] Advantages of the present invention:

[0019] (1) By providing an oil-gas separation device, a particle separation device and a cooling device, the present invention can effectively remove the flue gas and particles in industrial oil, avoid the oxidation of grease and reduce the service life of oil or equipment, and also avoid the pollution of grease by particulate impurities. At the same time, the high-temperature oil can be cooled in time, the deterioration rate of the oil can be reduced, and the insulation performance of the oil can be avoided from being reduced;

[0020] (3) In the oil-gas separation device of the present invention, by providing an inverter and a gas separation net, the separation speed of oil and gas can be improved, and the oil-gas separation efficiency can be improved; by providing a one-way exhaust mechanism, the gas can be exhausted in time, so that the air pressure in the oil-gas separation container is kept stable, and the pipeline components are prevented from bursting due to excessive pressure; by providing a breathing component, the oil-gas separation can be accelerated;

[0021] (2) The present invention is also provided with an oil replenishing device, which can timely replenish the oil in the circulation system, is flexible and convenient to operate, and has strong safety.

[0022] (4) The present invention has a simple structure and is convenient to operate, and can degas, remove impurities and cool the oil in multiple oil circuits of the power heat source, and has strong practicability. Description of the drawings:

[0023] Figure 1 is a schematic diagram of the structure of the present invention;

[0024] Figure 2 is a schematic structural diagram of the oil-gas separation device of the present invention;

[0025] Figure 3 is the oil replenishing device of the particulate separation device of the present invention;

[0026] Figure 4 is a distribution diagram of the temperature sensor and pressure regulator in the oil discharge pipe of the present invention;

[0027] Figure 5 is the oil replenishing device of the present invention's oil replenishing device

[0028] The reference numerals in the drawings are:

[0029] 1. Power heat source; 2. Oil-gas separation device; 2-1. Oil-gas separation container; 2-2. Inverter; 2-3. Gas separation net; 2-4. Unidirectional exhaust mechanism; 2-5. Balloon; 2-6. Gas transmission pipe; 3. Particulate separation device; 3-1. Stainless steel pump housing; 3-2. First cathode; 3-3. Second cathode; 3-4. U-shaped magnet; 3-5. Anode cylinder; 4. Cooling device; 4-1. Heat exchanger; 5. Inlet oil main pipe; 6. Outlet pipe; 7. Outlet oil main pipe; 8. Inlet pipe; 9. Circulation pump; 10. Temperature sensor; 10-1. Thermistor; 10-2. Heat conduction cylinder; 10-3. Anti-air interference cover; 11. Pressure regulator; 12. Oil replenishing device; 12-1. Oil cylinder; 12-2. Attached oil cylinder; 12-3. First oil transmission pipeline; 12-4. Oil transmission pump; 12-5. Valve; 12-6. Second oil transmission pipeline; 12-7. Oil replenishing pump; 12-8. Oil return channel; 12-9. Oil return valve; 13. Turbine flowmeter; 14. Support frame; 15. Flange. Specific embodiments:

[0030] To make the objectives, technical solutions, and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Obviously, the described embodiments are some, but not all, of the embodiments of the present invention. All other embodiments obtained by those of ordinary skill in the art based on the embodiments of the present invention without creative efforts fall within the scope of protection of the present invention.

[0031] As Figure 1 shown, the embodiments of the present invention provide a gas and particulate separation and cooling system for transformer oil, including an oil-gas separation device 2, a particulate separation device 3, a cooling device 4, and a circulation pump 9.

[0032] Among them, an oil inlet main pipe 5 is provided at the oil inlet end of the oil-gas separation device 2. The oil inlet main pipe 5 is communicated with seven oil outlet pipes 6 provided by the power heat source 1, and the oil temperatures in the seven oil outlet pipes 6 are the same or different. The oil outlet end of the oil-gas separation device 2 is connected to the oil inlet end of the circulation pump 9, the oil outlet end of the circulation pump 9 is connected to the oil inlet end of the cooling device 4, the oil outlet end of the cooling device 4 is connected to the oil inlet end of the particle separation device 3, and an oil outlet main pipe 7 is provided at the oil outlet end of the particle separation device 3. The oil outlet main pipe 7 is communicated with seven oil inlet pipes 8 provided by the power heat source 1. Both the oil outlet pipe 6 and the oil inlet pipe 8 are insulating cloth-covered silica gel pipes.

[0033] During application, under the action of the circulation pump 9, the oil discharged from the power heat source 1 sequentially enters the oil-gas separation device 2 through the oil outlet pipe 6 and the oil inlet main pipe 5. After removing the gas in the oil-gas separation device 2, it enters the cooling device 4 for cooling. The cooled oil enters the particle separation device 3 to remove metal dust particles. The oil after removing the gas and metal dust particles finally returns to the power heat source 1 through the oil outlet main pipe 7 and the oil inlet pipe 8 provided by the power heat source 1 for cyclic application.

[0034] As Figure 2 As shown, the oil-gas separation device 2 includes an oil-gas separation container 2-1, an inverter 2-2, and an air separation net 2-3. The oil-gas separation container 2-1 includes an upper pipe body and a lower pipe body that are detachably installed through a flange. The inverter 2-2 is a long cylindrical structure with an open top and a hollow interior. It is fixedly arranged inside the oil-gas separation container 2-1, fixedly connected to the upper pipe body, and the lower end of the inverter 2-2 extends to the lower part of the oil-gas separation container 2-1. The air separation net 2-3 is arranged inside the oil-gas separation container 2-1, and is fixedly connected to the inner wall of the upper pipe body of the oil-gas separation container 2-1 and the outer wall of the inverter 2-2 respectively, dividing the oil-gas separation container 2-1 into upper and lower spaces. The gas in the oil cannot pass through the air separation net 2-3. The oil inlet and outlet of the oil-gas separation container 2-1 are respectively arranged above and below the air separation net 2-3. The oil inlet main pipe 5 is a reverse U-shaped pipe. One branch pipe of the oil inlet main pipe 5 passes through the oil inlet of the oil-gas separation container 2-1 and extends to the lower inner part of the inverter 2-2, and the other branch pipe of the oil inlet main pipe 5 is distributed outside the oil-gas separation container 2-1 and is communicated with seven oil outlet pipes 6 of the power heat source 1 respectively.

[0035] During application, the oil discharged from the power heat source 1 sequentially enters the inverter 2-2 through the oil outlet pipe 6 and the oil inlet main pipe 5. The oil in the inverter 2-2 flows upward. The rising speed of the gas is greater than that of the oil, which can achieve the purpose of automatic separation. The bubbles formed when the gas flows upward are blocked by the air separation net 2-3. The gas is blocked above the air separation net 2-3, and the transformer oil enters the upper part of the air separation net 2-3 from bottom to top and moves to the lower inner part of the oil-gas separation container 2-1 through the air separation net 2-3, and finally flows out through the oil outlet for the next treatment.

[0036] AsFigure 2 As shown, the oil-gas separation device 2 further includes a one-way exhaust mechanism 2-4. The one-way exhaust mechanism 2-4 is connected to the oil-gas separation container 2-1 through a pipeline, and the connection end of the one-way exhaust mechanism 2-4 and the oil-gas separation container 2-1 is distributed above the gas separation net 2-3. A pressure sensor can be arranged inside the oil-gas separation container 2-1 to detect the internal pressure of the oil-gas separation container 2-1. When it is detected that the internal pressure of the oil-gas separation container 2-1 is higher than the set value, the one-way exhaust mechanism 2-4 is controlled by the control system to open, and the internal gas of the oil-gas separation container 2-1 is discharged through the one-way exhaust mechanism 2-4, avoiding excessive internal pressure of the oil-gas separation container 2-1 and achieving the function of stabilizing the pressure.

[0037] As Figure 2 shown, as a further preference of the present invention, the oil-gas separation device 2 further includes a breathing component. The breathing component includes a balloon 2-5, an air delivery pipe 2-6 and an air pump. Among them, the balloon 2-5 is arranged inside the oil-gas separation container 2-1, the air pump is arranged outside the oil-gas separation container 2-1, the air delivery pipe 2-6 passes through the air hole arranged on the oil-gas separation container 2-1, and the outer edge of the air delivery pipe 2-6 is sealed with the air hole of the oil-gas separation container 2-1. The two ends of the air delivery pipe 2-6 are respectively connected to the balloon 2-5 and the air pump. The air pump is used for inflating and deflating the balloon 2-5. When inflating, the balloon 2-5 expands and its volume becomes larger, and when deflating, the balloon 2-5 contracts and its volume becomes smaller. By controlling the inflation and deflation of the air pump, the internal pressure of the oil-gas separation container 2-1 can be adjusted, so as to achieve accelerated oil-gas separation.

[0038] As Figure 1 shown, the cooling device 4 includes a heat exchanger 4-1 and a refrigeration component. Among them, the heat exchanger 4-1 is provided with a refrigerant circulation pipeline and a heat exchange flow channel. The refrigerant circulation pipeline is used for the circulation of refrigerant (such as Freon), and the heat exchange flow channel is used for the circulation of transformer oil. The refrigeration component includes a compressor, a condenser, a liquid storage tank and an expansion valve. The outlet of the refrigerant circulation pipeline is connected to the compressor, the condenser, the liquid storage tank and the expansion valve in sequence through pipelines, and the expansion valve is connected to the inlet of the refrigerant circulation pipeline through a pipeline; the circulating refrigerant in the refrigerant circulation pipeline cools the hot oil in the heat exchange flow channel. The refrigerant after absorbing heat enters the compressor to form high-temperature and high-pressure gas, then enters the condenser to condense into liquid, and is stored in the liquid storage tank. The liquid refrigerant in the liquid storage tank enters the expansion valve for pressure reduction and temperature reduction, and then enters the refrigerant circulation pipeline again as a cold source to cool the hot oil in the heat exchange flow channel. Through such cyclic processing, the cooling and temperature reduction of the high-temperature oil are realized.

[0039] As Figure 3As shown in the figure, the particulate separation device 3 includes a stainless-steel pump housing 3-1, a first cathode 3-2, a second cathode 3-3, a U-shaped magnet 3-4, and seven anode cylinders 3-5. The first cathode 3-2, the second cathode 3-3, and the anode cylinders 3-5 are arranged inside the stainless-steel pump housing 3-1. The first cathode 3-2 and the second cathode 3-3 are parallel to each other, and the anode cylinders 3-5 are connected in series with each other and arranged between the first cathode 3-2 and the second cathode 3-3. The U-shaped magnet 3-4 is arranged outside the stainless-steel pump housing 3-1. The stainless-steel pump housing 3-1 is distributed between the two magnetic poles of the U-shaped magnet 3-4, and the U-shaped magnet 3-4 is used to provide a magnetic field. The oil processed by the oil-gas separation device 2 and the cooling device 4 enters the interior of the particulate separation device 3 through the oil inlet. The positive-ion particles fly towards the cathode plate, and the negative-ion particles fly towards the anode cylinders, so that the positive and negative charged particles in the oil are adsorbed inside the oil-gas separation device 2, and the oil after removing the particles is exported through the oil outlet.

[0040] As Figure 1 and Figure 4 shown, as a preferred embodiment of the present invention, a temperature sensor 10 and a pressure regulator 11 are arranged on the oil outlet pipe 6 of the power heat source 1 for detecting the oil temperature and the oil pressure. Among them, the structure or model of the temperature sensor 10 can be selected according to needs. Specifically, in this embodiment, the temperature sensor 10 includes a thermistor 10-1, a heat conduction cylinder 10-2, and an air interference prevention cover 10-3. The thermistor 10-1 is fixed inside the heat conduction cylinder 10-2 and sealed by the air interference prevention cover 10-3. The heat conduction cylinder 10-2 is fixed on the oil outlet pipe 6. The heat conduction cylinder 10-2 can immediately transfer the heat of the oil in the oil outlet pipe 6, and the thermistor 10-1 can sense the temperature of the oil in real time and feedback the temperature information to the main control system.

[0041] As Figure 1 shown, as a preferred embodiment of the present invention, a turbine flowmeter 13 is arranged on the oil inlet pipe 8 of the power heat source 1, which can monitor the oil flow in the seven oil outlet pipes 6 in real time.

[0042] As Figure 1 and Figure 5 shown, as a preferred embodiment of the present invention, the device is further provided with an oil replenishing device 12. When the amount of oil circulating in the system becomes less, the oil replenishing device 12 can replenish oil into the system to meet the oil quantity requirement.

[0043] Specifically, as Figure 5 shown, the oil replenishing device 12 includes an oil cylinder 12-1 and an attached oil cylinder 12-2. An oil cylinder cover is detachably installed on the oil cylinder 12-1. The oil cylinder 12-1 and the oil cylinder cover are sealed. An oil outlet hole and an oil inlet hole are arranged on the oil cylinder cover.

[0044] Among them, the oil barrel 12-1 is connected to the oil inlet main pipe 5 through the first oil pipeline 12-3. One end of the first oil pipeline 12-3 is connected to the lower end of the branch pipe of the oil inlet main pipe 5 of the inverted U-shaped pipe. The other end of the first oil pipeline 12-3 extends into the lower part of the oil barrel 12-1 through the oil outlet hole. The outer edge of the first oil pipeline 12-3 is sealingly connected to the inner edge of the oil outlet hole. An oil transfer pump 12-4 for providing oil transfer power and a valve 12-5 for opening and closing the oil pipeline are arranged on the first oil pipeline 12-3. The auxiliary oil barrel 12-2 is arranged on one side of the oil barrel 12-1 and is connected to the oil barrel 12-1 through the second oil pipeline 12-6. One end of the second oil pipeline 12-6 is communicated with the auxiliary oil barrel 12-2. The other end of the second oil pipeline 12-6 passes through the oil inlet hole arranged on the oil barrel cover and is communicated with the oil barrel 12-1. And the outer edge of the second oil pipeline 12-6 is sealingly connected to the inner edge of the oil inlet hole. A makeup oil pump 12-7 is arranged on the second oil pipeline 12-6 for transferring the oil in the auxiliary oil barrel 12-2 into the oil barrel 12-1. When the oil quantity inside the circulation system is insufficient, start the oil transfer pump 12-4 and open the valve 12-5 of the oil pipeline. The oil in the oil barrel 12-1 enters the oil inlet main pipe 5 through the first oil pipeline 12-3. When the oil quantity in the oil barrel 12-1 is insufficient, start the makeup oil pump 12-7. The oil in the auxiliary oil barrel 12-2 enters the oil barrel 12-1 through the second oil pipeline 12-6.

[0045] As Figure 5 shown, as an alternative embodiment of the present invention, an oil return channel 12-8 is further arranged between the auxiliary oil barrel 12-2 and the oil barrel 12-1. Both ends of the oil return channel 12-8 are communicated with the auxiliary oil barrel 12-2 and the oil barrel 12-1 respectively. And an oil return valve 12-9 is arranged on the oil return channel 12-8. The oil inside the oil barrel 12-1 can also enter the auxiliary oil barrel 12-2 through the oil return channel 12-8.

[0046] The present invention can slow down the oxidation process of the oil, timely remove the particles in the oil to improve the impedance, dissipate heat efficiently, and increase the service life of the oil. The system adopts a building block structure design with high integration, is suitable for on-site mobile installation, and is convenient to use.

[0047] The above is only the preferred embodiment of the present invention. The protection scope of the present invention is not limited to the above embodiments. All technical solutions falling within the idea of the present invention belong to the protection scope of the present invention. It should be pointed out that for those of ordinary skill in the art, several improvements and refinements made without departing from the principle of the present invention should be regarded as the protection scope of the present invention.

Claims

1. A gas and particle separation and cooling system for transformer oil, characterized in that it includes an oil-gas separation device (2), a particle separation device (3) and a cooling device (4); An oil inlet header pipe (5) is arranged at the oil inlet end of the oil-gas separation device (2), and the oil inlet header pipe (5) is communicated with a plurality of outlet oil pipes (6) arranged by the power heat source (1); the oil outlet end of the oil-gas separation device (2) is connected to the oil inlet end of the cooling device (4), the oil outlet end of the cooling device (4) is connected to the oil inlet end of the particle separation device (3), and an outlet oil header pipe (7) is arranged at the oil outlet end of the particle separation device (3), and the outlet oil header pipe (7) is communicated with a plurality of inlet oil pipes (8) arranged by the power heat source (1).

2. The gas and particle separation and cooling system for transformer oil according to claim 1, characterized in that the oil-gas separation device (2) includes an oil-gas separation container (2-1), an inverter (2-2) and a gas separation net (2-3); The inverter (2-2) is a cylindrical structure with an open top and a hollow interior, and is fixedly arranged inside the oil-gas separation container (2-1); the gas separation net (2-3) is arranged inside the oil-gas separation container (2-1), and is fixedly connected to the inner wall of the oil-gas separation container (2-1) and the outer wall of the inverter (2-2) respectively, dividing the oil-gas separation container (2-1) into two spaces, and the oil inlet and outlet of the oil-gas separation container (2-1) are respectively arranged above and below the gas separation net (2-3); The oil inlet header pipe (5) is an inverted U-shaped pipe, and one branch of the oil inlet header pipe (5) passes through the oil inlet of the oil-gas separation container (2-1) and extends to the lower part inside the inverter (2-2), and the other branch of the oil inlet header pipe (5) is distributed outside the oil-gas separation container (2-1) and is respectively communicated with a plurality of outlet oil pipes (6) of the power heat source (1).

3. The gas and particle separation and cooling system for transformer oil according to claim 2, characterized in that the oil-gas separation device (2) further includes a one-way exhaust mechanism (2-4), and the one-way exhaust mechanism (2-4) is communicated with the oil-gas separation container (2-1) through a pipeline, and the connection end of the one-way exhaust mechanism (2-4) and the oil-gas separation container (2-1) is distributed above the gas separation net (2-3).

4. The gas and particle separation and cooling system for transformer oil according to claim 2, characterized in that the oil-gas separation device (2) further includes a breathing component; The breathing component includes a balloon (2-5), an air delivery pipe (2-6) and an air pump; The balloon (2-5) is arranged inside the oil-gas separation container (2-1), the air pump is arranged outside the oil-gas separation container (2-1), and the balloon (2-5) and the air pump are connected through the air delivery pipe (2-6).

5. The gas and particle separation and cooling system for transformer oil according to claim 1, characterized in that the particle separation device (3) includes a stainless steel pump housing (3-1), a first cathode (3-2), a second cathode (3-3), a U-shaped magnet (3-4) and at least one anode cylinder (3-5); The first cathode (3-2), the second cathode (3-3) and the anode cylinder (3-5) are arranged inside the stainless steel pump housing (3-1). The first cathode (3-2) and the second cathode (3-3) are parallel to each other, and the anode cylinder (3-5) is arranged between the first cathode (3-2) and the second cathode (3-3); The U-shaped magnet (3-4) is arranged outside the stainless steel pump housing (3-1), and the stainless steel pump housing (3-1) is distributed between the two magnetic poles of the U-shaped magnet (3-4).

6. The gas and particle separation and cooling system in transformer oil according to claim 1, characterized in that The cooling device (4) includes a heat exchanger (4-1) and a refrigeration component; The heat exchanger (4-1) is provided with a refrigerant circulation pipeline and a heat exchange flow channel, The refrigeration component includes a compressor, a condenser, a liquid storage tank and an expansion valve. The outlet of the refrigerant circulation pipeline is connected to the compressor, the condenser, the liquid storage tank and the expansion valve in sequence through pipelines, and the expansion valve is connected to the inlet of the refrigerant circulation pipeline through a pipeline; the circulating refrigerant in the refrigerant circulation pipeline cools the hot oil in the heat exchange flow channel. The refrigerant after absorbing heat enters the compressor to form high-temperature and high-pressure gas, then enters the condenser to be condensed into liquid, and is stored in the liquid storage tank. The liquid refrigerant in the liquid storage tank enters the expansion valve for pressure reduction and temperature reduction, and then enters the refrigerant circulation pipeline again as a cold source to cool the hot oil in the heat exchange flow channel.

7. The gas and particle separation and cooling system in transformer oil according to claim 1, characterized in that A circulation pump (9) is further provided; The circulation pump (9) is distributed between the oil-gas separation device (2) and the cooling device (4). The inlet of the circulation pump (9) is connected to the oil outlet pipeline of the oil-gas separation device (2), and the outlet of the circulation pump (9) is connected to the oil inlet pipeline of the cooling device (4).

8. The gas and particle separation and cooling system in transformer oil according to claim 1, characterized in that A temperature sensor (10) and a pressure regulator (11) are provided on the oil outlet pipe (6) of the power heat source (1); A turbine flowmeter (13) is provided on the oil inlet pipe (8) of the power heat source (1); Both the oil outlet pipe (6) and the oil inlet pipe (8) are insulating rubber hoses with fabric.

9. The gas and particle separation and cooling system in transformer oil according to claim 1, characterized in that A oil replenishing device (12) is further provided; The oil replenishing device (12) includes an oil cylinder (12-1) and an attached oil cylinder (12-2); The oil cylinder (12-1) is connected to the main oil inlet pipe (5) through a first oil pipeline (12-3), and a oil transfer pump (12-4) and a valve (12-5) are provided on the first oil pipeline (12-3); The attached oil cylinder (12-2) is connected to the oil cylinder (12-1) through a second oil pipeline (12-6), and a oil replenishing pump (12-7) is provided on the second oil pipeline (12-6).

10. The gas and particle separation and cooling system in transformer oil according to claim 9, characterized in that An oil return passage (12-8) is further provided between the additional oil cylinder (12-2) and the oil cylinder (12-1). Both ends of the oil return passage (12-8) are respectively communicated with the additional oil cylinder (12-2) and the oil cylinder (12-1), and an oil return valve (12-9) is provided on the oil return passage (12-8).