Circulation driving structure of thermosyphon cooler

Abstract

The utility model relates to the technical field of thermosyphon coolers, in particular to a circulation driving structure of a thermosyphon cooler, which comprises an evaporator, a gas-liquid separation tank arranged above the evaporator, an air cooler arranged above the gas-liquid separation tank, and a gas conveying pipe connected with the top of one end of the evaporator and connected with the top of the other end of the gas-liquid separation tank. The top of one end of the gas-liquid separation tank is connected with the top of one end of the air cooler through a gas separation pipe, and the bottom of the other end of the evaporator is connected with the bottom of the other end of the gas-liquid separation tank through a liquid return pipe. According to the circulation driving structure of the thermosyphon cooler, the gas-liquid separation tank is arranged above the evaporator, and the top and the bottom of the evaporator and the top and the bottom of the gas-liquid separation tank are connected through the gas conveying pipe and the liquid return pipe respectively, so that effective separation of gas and liquid is achieved. By means of the design, the flow resistance of the gas and liquid mixture in the pipeline is reduced, the problems of blockage and unsmooth flow are avoided, and therefore the overall performance of the cooler is improved.

Description

TECHNICAL FIELD

[0001] The utility model relates to heat siphon cooler technical field, concretely relates to a circulating drive structure of heat siphon cooler. BACKGROUND

[0002] In the heat siphon cooler technical field, the design of circulating drive structure is crucial for the operation efficiency and stability of the whole system. The traditional heat siphon cooler circulating drive structure usually includes an evaporator, a condenser (which may appear in the form of an air cooler in some designs) and a pipeline system connecting the two. However, these traditional structures often have some problems and deficiencies in practical application.

[0003] On the one hand, the gas-liquid separation effect in the traditional structure is not ideal, which leads to problems such as blockage and poor flow during the circulation of gas and liquid mixture in the pipeline, affecting the overall performance of the cooler. This problem is particularly prominent in high-temperature and high-pressure working environments.

[0004] On the other hand, the traditional circulating drive structure has deficiencies in impurity removal and sedimentation. During the circulation process, various impurities and particulate matter may be mixed into the coolant, which not only affects the flowability and heat transfer performance of the coolant, but also may cause wear and corrosion to the internal components of the cooler, shortening the service life of the equipment.

[0005] In addition, the layout and pipeline design of the traditional structure may not be optimized, resulting in significant energy loss during the circulation process and reducing the cooling efficiency. This problem is more pronounced in cases where the coolant needs to be transported over long distances. SUMMARY

[0006] The purpose of the utility model is to provide a circulating drive structure of heat siphon cooler to solve the problem of poor gas-liquid separation effect in the traditional structure, which leads to problems such as blockage and poor flow during the circulation of gas and liquid mixture in the pipeline, affecting the overall performance of the cooler. This problem is particularly prominent in high-temperature and high-pressure working environments.

[0007] In order to achieve the above object, the utility model provides a kind of circulation drive structure of thermosyphon cooler, including evaporator, the top of the evaporator is provided with gas-liquid separation tank, the top of the gas-liquid separation tank is provided with air cooler, the top of one end of the evaporator is connected with the top of one end of gas-liquid separation tank by gas pipe, the top of one end of the gas-liquid separation tank is connected with the top of one end of air cooler by gas separation pipe, the bottom of the other end of the evaporator is connected with the bottom of the other end of gas-liquid separation tank by liquid return pipe, the top of the other end of the gas-liquid separation tank is connected with the bottom of the other end of air cooler by liquid path pipe.

[0008] As preferred, the bottom end of the gas separation pipe is provided with a sediment tank, and a plurality of baffles are vertically arranged on the top of the sediment tank.

[0009] As preferred, the sediment tank is provided with a decontamination port on one side, and a cover plate is arranged on the outside of the decontamination port.

[0010] As preferred, the middle section of the liquid return pipe is provided with a decontamination tank.

[0011] As preferred, a filter screen is arranged in the decontamination tank, a high-pressure gas pump is connected to the lower part of one side of the decontamination tank, an exhaust pipe is connected to the upper part of one side of the decontamination tank, and an exhaust valve is arranged on the exhaust pipe.

[0012] As preferred, a liquid inlet is arranged on the upper part of the decontamination tank, a liquid outlet is arranged on the lower part of the decontamination tank, an upper valve is arranged on the liquid inlet of the decontamination tank, and a lower valve is arranged on the liquid outlet of the decontamination tank.

[0013] As preferred, the evaporator, the gas-liquid separation tank and the air cooler are arranged at equal intervals from top to bottom.

[0014] As preferred, the baffles are arranged at equal intervals.

[0015] Compared with the prior art, the utility model has the beneficial effects that:

[0016] In the circulation drive structure of the thermosyphon cooler, the gas-liquid separation tank is arranged above the evaporator, and the gas pipe and the liquid return pipe are respectively connected to the top and the bottom of the evaporator and the gas-liquid separation tank, which realizes the effective separation of gas and liquid. This design reduces the flow resistance of the gas and liquid mixture in the pipeline, avoids the problems of blockage and poor flow, and improves the overall performance of the cooler. Especially in high-temperature and high-pressure working environment, the optimized gas-liquid separation effect is particularly significant.

[0017] A sedimentation bin is installed at the bottom end of the gas separation tube, and a plurality of baffles are arranged inside the sedimentation bin, which can slow down the flow rate of the gas, so that impurities and particles are more easily deposited. At the same time, the impurity removal port arranged on one side of the sedimentation bin facilitates the cleaning of the deposits. In addition, a sediment removal bin is installed in the middle section of the liquid return pipe, and a filter screen is arranged in the bin to further filter out impurities in the coolant. The design of the high-pressure gas pump and the exhaust pipe helps to exhaust the gas in the bin when cleaning impurities, maintaining the pressure balance in the bin. These designs collectively improve the purity and flowability of the coolant and extend the service life of the equipment.

[0018] The evaporator, the gas-liquid separation tank and the air cooler are arranged in an equal interval from top to bottom, which not only saves space, but also facilitates the smooth flow of the coolant and the effective transfer of heat. At the same time, the valves and connecting pieces in the pipeline system are carefully designed to reduce energy loss and the risk of leakage, and to improve the cooling efficiency. Especially in the case of long-distance transmission of the coolant, the optimized layout and pipeline design can significantly reduce energy loss and improve overall performance. BRIEF DESCRIPTION OF DRAWINGS

[0019] Fig. 1 It is a schematic diagram of the overall structure of the utility model;

[0020] Fig. 2 It is a schematic diagram of the structure of the sediment removal bin in the utility model;

[0021] Fig. 3 It is a schematic diagram of the structure of the sedimentation bin in the utility model;

[0022] The meanings of the various reference numerals in the drawings are as follows:

[0023] 1, evaporator; 11, gas pipeline; 12, liquid return pipe; 121, lower valve; 122, upper valve; 2, gas-liquid separation tank; 21, gas separation tube; 3, air cooler; 31, liquid path pipe; 4, sediment removal bin; 41, filter screen; 42, high-pressure gas pump; 43, exhaust pipe; 431, exhaust valve; 5, sedimentation bin; 51, baffle; 52, impurity removal port. DETAILED DESCRIPTION

[0024] The technical solutions in the embodiments of the utility model will be clearly and completely described below with reference to the drawings in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, rather than all the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by those skilled in the art without creative labor fall within the scope of protection of the utility model.

[0025] The utility model provides a circulating drive structure of thermosyphon cooler, like Figs. 1-3As shown, it includes an evaporator 1, an air-liquid separation tank 2 is arranged above the evaporator 1, an air cooler 3 is arranged above the air-liquid separation tank 2, one end of the top of the evaporator 1 is connected with one end of the top of the air-liquid separation tank 2 through a gas conveying pipe 11, one end of the top of the air-liquid separation tank 2 is connected with one end of the top of the air cooler 3 through a gas separation pipe 21, the other end of the bottom of the evaporator 1 is connected with the other end of the bottom of the air-liquid separation tank 2 through a liquid return pipe 12, and the other end of the top of the air-liquid separation tank 2 is connected with the other end of the bottom of the air cooler 3 through a liquid path pipe 31. Through the careful design of the component layout and the pipeline connection, the efficient and stable circulation driving effect is realized. Specifically, the evaporator 1, the air-liquid separation tank 2 and the air cooler 3 are arranged in sequence from top to bottom, and are tightly connected through the pipeline system such as the gas conveying pipe 11, the gas separation pipe 21, the liquid return pipe 12 and the liquid path pipe 31, forming a complete and closed circulation driving structure.

[0026] In this structure, the gas-liquid mixture generated by the evaporator 1 first enters the air-liquid separation tank 2 through the gas conveying pipe 11 for gas-liquid separation. The design of the air-liquid separation tank 2 can effectively separate the gas and the liquid, avoiding the problems such as blockage and poor flow that easily occur when the gas-liquid mixture flows in the pipeline in the traditional structure. The separated gas enters the air cooler 3 through the gas separation pipe 21 for cooling treatment, and the liquid returns to the evaporator 1 through the liquid return pipe 12 for recycling. At the same time, the other end of the top of the air-liquid separation tank 2 is also connected with the other end of the bottom of the air cooler 3 through the liquid path pipe 31, ensuring that the cooled liquid can flow back to the evaporator 1 smoothly, forming a continuous circulation process.

[0027] The design of this circulation driving structure not only improves the overall performance of the cooler, but also enhances the stability and reliability of the system. By optimizing the pipeline layout and connection method, the energy loss and leakage risk are reduced, and the cooling efficiency is improved. At the same time, the arrangement of the air-liquid separation tank 2 and the air cooler 3 also helps to prolong the service life of the equipment and reduce the maintenance cost.

[0028] In this embodiment, the bottom end of the gas separation pipe 21 is provided with a sedimentation bin 5, and a plurality of baffles 51 are vertically arranged inside the top of the sedimentation bin 5. This design effectively improves the sedimentation efficiency of impurities in the gas. The presence of the baffles 51 slows down the flow rate of the gas, allowing heavier impurity particles to have more opportunities to deposit in the sedimentation bin 5, thereby avoiding these impurities from entering the subsequent air cooler 3, ensuring the cleanliness and operating efficiency of the cooling system.

[0029] Specifically, one side of the sedimentation bin 5 is provided with a impurity removal port 52, and a cover plate is installed outside the impurity removal port 52. This provides a convenient way for users to clean impurities. When a certain amount of impurities accumulates in the sedimentation bin, users can easily remove the impurities from the impurity removal port 52 by opening the cover plate, which not only maintains the cleanliness of the system, but also prolongs the service life of the equipment.

[0030] Further, the middle section of the liquid return pipe 12 is provided with a impurity removal bin 4. This design further strengthens the purification process of the coolant. As a barrier in the liquid return path, the impurity removal bin 4 can effectively intercept and remove impurities carried in the coolant, ensuring high purity of the coolant returned to the evaporator, thereby improving the performance and stability of the entire cooling system.

[0031] Further, the inside of the impurity removal bin 4 is provided with a filter screen 41, one side of the impurity removal bin 4 is connected with a high-pressure gas pump 42 at the lower part, and one side of the impurity removal bin 4 is connected with an exhaust pipe 43 at the upper part, and an exhaust valve 431 is installed on the exhaust pipe 43. The above-mentioned structure jointly constitutes a high-efficiency impurity removal system. The filter screen 41 can finely filter the impurities in the coolant, and the high-pressure gas pump 42 provides necessary power support when cleaning impurities. Through the cooperation of the exhaust pipe 43 and the exhaust valve 431, the gas in the bin can be easily discharged, the pressure balance in the bin is maintained, and the smooth progress of the impurity removal process is ensured.

[0032] Further, the upper part of the impurity removal bin 4 is provided with a liquid inlet, the lower part of the impurity removal bin 4 is provided with a liquid outlet, the upper valve 122 is installed on the liquid inlet of the impurity removal bin 4, and the lower valve 121 is installed on the liquid outlet of the impurity removal bin 4. This provides users with flexible control options. By adjusting the opening and closing states of the two valves, users can accurately control the flow of liquid in the impurity removal bin 4.

[0033] Further, the evaporator 1, the gas-liquid separation tank 2 and the air cooler 3 are arranged in equal intervals from top to bottom. This layout not only looks beautiful and compact, but also facilitates the smooth flow of coolant and the effective transfer of heat. The equal-interval arrangement ensures that the lengths of the connecting pipes between the components are equal, reducing energy loss and flow resistance caused by differences in pipe length, and improving the performance of the entire cooling system.

[0034] Further, the baffles 51 are arranged in equal intervals. This design ensures that the gas can uniformly decelerate when passing through the sedimentation bin, allowing impurity particles to have more uniform opportunities to settle down. The equal-interval arrangement also optimizes the space utilization of the sedimentation bin and improves the sedimentation efficiency of impurities.

[0035] The circulating driving structure of the thermosiphon cooler in use firstly in the evaporator 1, the coolant is heated and evaporated, and a mixture of gas and liquid is formed.

[0036] The gas and liquid mixture generated by evaporation enters the gas-liquid separation tank 2 through the gas conveying pipe 11. In the gas-liquid separation tank 2, the gas and liquid are naturally separated due to the change of gravity and flow rate. The gas continues to flow upward through the gas separation pipe 21, and the liquid returns to the evaporator 1 through the liquid return pipe 12.

[0037] The separated gas enters the air cooler 3 through the gas separation pipe 21. In the air cooler 3, the gas exchanges heat with the external environment and is cooled to change into liquid or gas-liquid mixture.

[0038] Before the gas enters the air cooler 3, it will first pass through the sedimentation bin 5. The baffle 51 inside the sedimentation bin 5 slows down the flow rate of the gas, so that heavier impurity particles are deposited. The user can periodically open the cover of the impurity removal port 52 to clean the impurities in the sedimentation bin 5

[0039] The liquid returned from the evaporator 1 enters the impurity removal bin 4 through the liquid return pipe 12. In the impurity removal bin 4, the filter screen 41 intercepts and removes the impurities in the liquid. When cleaning the impurities, the high-pressure gas pump 42 provides power support, and the gas in the bin is discharged through the exhaust pipe 43 and the exhaust valve 431 to maintain pressure balance. The pure liquid continues to return to the evaporator 1 through the liquid return pipe 12 to complete the circulation.

[0040] Through the liquid path pipe 31, the cooled liquid or gas-liquid mixture in the air cooler 3 smoothly flows back to the evaporator 1. The evaporator 1, the gas-liquid separation tank 2 and the air cooler 3 are arranged at equal intervals from top to bottom, which ensures smooth flow of the coolant and effective transfer of heat. This continuous and stable circulation process improves the overall performance of the cooler and enhances the stability and reliability of the system.

[0041] The above shows and describes the basic principles, main features and advantages of the present application. Those skilled in the art should understand that the present application is not limited to the above embodiments, and the above embodiments and descriptions in the specification are only preferred examples of the present application and do not limit the present application. Without departing from the spirit and scope of the present application, various changes and improvements can be made to the present application, and these changes and improvements all fall within the scope of the claimed present application. The scope of protection of the present application is defined by the appended claims and their equivalents.

Claims

1. A circulation drive structure of a thermosyphon cooler, comprising an evaporator (1), characterized in that: The upper portion of the evaporator (1) is provided with a gas-liquid separation tank (2), the upper portion of the gas-liquid separation tank (2) is provided with an air cooler (3), one end of the top of the evaporator (1) is connected with one end of the top of the gas-liquid separation tank (2) through a gas conveying pipe (11), one end of the top of the gas-liquid separation tank (2) is connected with one end of the top of the air cooler (3) through a gas separation pipe (21), the other end of the bottom of the evaporator (1) is connected with the other end of the bottom of the gas-liquid separation tank (2) through a liquid return pipe (12), and the other end of the top of the gas-liquid separation tank (2) is connected with the other end of the bottom of the air cooler (3) through a liquid path pipe (31).

2. The thermosiphon cooler circulation drive structure of claim 1, wherein: The bottom end of the gas separation pipe (21) is provided with a sedimentation bin (5), and a plurality of baffles (51) are vertically arranged on the upper portion of the inside of the sedimentation bin (5).

3. The thermosiphon cooler circulation drive structure of claim 2, wherein: One side of the sedimentation bin (5) is provided with a foreign matter removal opening (52), and a cover plate is arranged on the outside of the foreign matter removal opening (52).

4. The thermosiphon cooler of claim 1, wherein: The middle section of the liquid return pipe (12) is provided with a foreign matter removal bin (4).

5. The thermosiphon cooler circulation drive structure of claim 4, wherein: The inside of the foreign matter removal bin (4) is provided with a filter screen (41), one side of the lower portion of the foreign matter removal bin (4) is connected with a high-pressure gas pump (42), one side of the upper portion of the foreign matter removal bin (4) is connected with an exhaust pipe (43), and the exhaust pipe (43) is provided with an exhaust valve (431).

6. The thermosiphon cooler of claim 5, wherein: The upper portion of the foreign matter removal bin (4) is provided with a liquid inlet, the lower portion of the foreign matter removal bin (4) is provided with a liquid outlet, the liquid return pipe (12) is provided with an upper valve (122) near the liquid inlet of the foreign matter removal bin (4), and the liquid return pipe (12) is provided with a lower valve (121) near the liquid outlet of the foreign matter removal bin (4).

7. The thermosiphon cooler of claim 1, wherein: The evaporator (1), the gas-liquid separation tank (2) and the air cooler (3) are arranged in equal intervals from top to bottom.

8. The thermosiphon cooler of claim 2, wherein: The baffles (51) are arranged in equal intervals.

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