Steam heat exchange device and method for formation of high-temperature-resistant electrode foil for AI server

Abstract

The invention relates to the technical field of production equipment, in particular to a steam heat exchange device and method based on high-temperature-resistant electrode foil formation for an AI server, the steam heat exchange device comprises a heat exchange tank and further comprises a plurality of vortex-shaped pipes, the vortex-shaped pipes are uniformly and concentrically arranged along the center axis of the heat exchange tank, and the bottom of the heat exchange tank communicates with a steam inlet pipe for inputting high-temperature steam into the vortex-shaped pipes; a centrifugal assembly for driving the multiple vortex-shaped pipes to rotate synchronously is arranged in the heat exchange tank. The spiral scraping pipe is spirally arranged in the vortex-shaped pipe and attached to the inner wall of the vortex-shaped pipe, the interior of the vortex-shaped pipe is rotationally connected with a sealed rotating shell, the interior of the sealed rotating shell is fixedly connected with a positioning piece used for clamping the spiral scraping pipe, and the outer surface of the sealed rotating shell is provided with a cleaning assembly for driving the positioning piece to rotate intermittently and a lifting seat; the lifting base is arranged above the multiple vortex-shaped pipes, the lifting base can apply pressure to the vortex-shaped pipes to enable the vortex-shaped pipes to deform, and a trigger assembly which drives the lifting base to move and drives the cleaning assembly to operate at the same time is arranged in the heat exchange tank.

Description

TECHNICAL FIELD

[0001] The application relates to the technical field of production equipment, in particular to a steam heat exchange device and method for high-temperature-resistant electrode foil formation based on an AI server. BACKGROUND

[0002] In recent years, with the rapid development of artificial intelligence, cloud computing and data centers, the performance requirements of AI servers for power electronic components have significantly increased. As the core material of aluminum electrolytic capacitors, the performance of electrode foil directly affects the voltage resistance, capacity stability and service life of the capacitor. Electrode foil formation is a chemical or electrochemical process that forms an oxide film with specific properties on the surface of the electrode foil. This oxide film not only improves the specific capacitance of the electrode foil, but also improves its surface morphology and microstructure, further enhancing the high-frequency impedance performance of the electrode foil.

[0003] As prior art patent document No. CN214095655U, the patent document discloses an electrode foil formation production line steam heat exchange system, which relates to the technical field of electrode foil production equipment, and mainly aims to provide an electrode foil formation production line steam heat exchange system that can eliminate the risk of dry heating of the heating pipe and leakage, and reduce production costs and failure rate. The main technical scheme of the patent document is: an electrode foil formation production line steam heat exchange system, comprising: a water supply component, a first regulating valve arranged on the water inlet pipe; a gas supply component, a second regulating valve arranged on the gas inlet pipe; a heat exchange component, one end of the heat exchange water pipe is connected to the water inlet pipe, the other end is connected to the drain pipe, one end of the heat exchange gas pipe is connected to the water inlet pipe, the other end is connected to the exhaust pipe; a storage component, the drain pipe is connected to the heat preservation tank, one end of the conveying pipeline is connected to the heat preservation tank, the other end is connected to the production line liquid supply pipeline. The patent document is mainly used for heating deionized water.

[0004] In the existing related technical system, the method of using steam and deionized water for heat exchange to achieve deionized water heating is more common. Specifically, this technology usually uses a tubular heat exchanger to complete this heat exchange process. Steam flows outside or inside the tube wall of the tubular heat exchanger, and exchanges heat with deionized water flowing inside or outside the tube. Steam often contains a certain amount of impurities, such as calcium, magnesium ions and small solid particles. During the cooling of the steam, as the temperature decreases, these impurities will gradually reach a supersaturated state, and then precipitate and deposit on the tube wall of the tubular heat exchanger, forming a scale layer. The scale layer has very poor thermal conductivity, and its thermal conductivity coefficient is much lower than that of the metal tube wall and the steam, deionized water and other media. Therefore, the application proposes a steam heat exchange device and method for high-temperature-resistant electrode foil formation based on an AI server. SUMMARY

[0005] The present application aims to provide a steam heat exchange device and method for AI server high-temperature-resistant electrode foil formation to solve the problems in the background art.

[0006] To achieve the above-mentioned purpose, the present application provides the following technical solutions: a steam heat exchange device for AI server high-temperature-resistant electrode foil formation, comprising a heat exchange tank, further comprising: A plurality of vortex tubes are arranged concentrically along the central axis of the heat exchange tank, the bottom of the heat exchange tank is connected to a steam inlet pipe for inputting high-temperature steam into the plurality of vortex tubes, and a centrifugal assembly is arranged inside the heat exchange tank to drive the plurality of vortex tubes to rotate synchronously. A spiral scraping tube is spirally arranged inside the vortex tube and adheres to the inner wall of the vortex tube, a sealed rotating shell is rotatably connected to the inside of the vortex tube, a positioning piece for clamping the spiral scraping tube is fixedly connected to the inside of the sealed rotating shell, and a cleaning assembly is arranged on the outer surface of the sealed rotating shell to drive the positioning piece to rotate intermittently. A lifting seat is arranged above the plurality of vortex tubes, and the lifting seat can pressurize the vortex tubes to deform, and a trigger assembly is arranged inside the heat exchange tank to drive the lifting seat to move while driving the cleaning assembly to operate.

[0007] Preferably, the centrifugal assembly comprises a central shaft arranged inside the heat exchange tank and rotatably connected to one end of the steam inlet pipe, a plurality of steam inlet shells are slidably connected to the outer surface of the central shaft and communicate with the central shaft, one end of the vortex tube communicates with the steam inlet shell, and a driving motor is fixedly connected to the top of the heat exchange tank to drive the central shaft to rotate.

[0008] Preferably, a plurality of cooling steam pipes are arranged inside the heat exchange tank and diverge along the center thereof, a plurality of support collars are commonly connected to the plurality of cooling steam pipes, one end of each vortex tube is rotatably connected to a second-order steam discharge ring of each support collar, and the second-order steam discharge ring allows the fluid in the vortex tube to be discharged into the support collar.

[0009] Preferably, the cleaning assembly comprises a sleeve handle sleeved on the outer surface of the sealed rotating shell, a ratchet is fixedly connected to the outer surface of the sealed rotating shell, a pawl rotatably connected to the inside of the sleeve handle is adapted to the ratchet, and a tension spring is fixedly connected to the inside of the sleeve handle.

[0010] Preferably, the trigger assembly comprises a connecting frame arranged inside the heat exchange tank and fixedly connected to the outer surface of the central shaft, a scissor-type telescopic frame rotatably connected to one side of the connecting frame is used to drive the lifting seat to lift, a contact wheel is rotatably connected to the end of the scissor-type telescopic frame away from the connecting frame, a vertical pipe is arranged inside the heat exchange tank to drive the contact wheel to move, and a transmission handle rotatably connected to one end of the sleeve handle is fixedly connected to the bottom of the lifting seat.

[0011] Preferably, an auxiliary rod is fixedly connected to one side of the connecting frame, one end of the auxiliary rod is slidably connected to a sliding rod fixedly connected to the interference wheel, the outer surface of the sliding rod is provided with a spring that drives itself to reset, and the inside of the auxiliary rod is slidably connected to a counterweight bead that interferes with one end of the sliding rod.

[0012] Preferably, the top of the steam inlet shell is fixedly connected to a sleeve spring sleeved on the outer surface of the central axis rod, and the top of the sleeve spring is fixedly connected to the central axis rod.

[0013] Preferably, a plurality of liquid storage racks are fixedly connected to the outer surface of the heat exchange tank, and a plurality of drainage pipes extending into the liquid storage racks are connected to one side of the cooling steam pipe, and a support leg is fixedly connected to the bottom of the liquid storage rack.

[0014] Preferably, one side of each of the liquid storage and testing frames is connected to a liquid outlet pipe, and the multiple liquid outlet pipes are commonly connected to a discharge pipe.

[0015] The present invention also provides a steam heat exchange method based on a high-temperature resistant electrode foil for an AI server, comprising the following steps: S1, 150℃ boric acid steam enters the vortex tube through the steam inlet pipe and exchanges heat with the liquid in the heat exchange tank; S2. Start the centrifugal assembly to make the steam and condensate flow rapidly in the vortex tube, forming turbulence during the flow process and finally discharge from the vortex tube; S3. The rotation of the vortex tube drives the trigger assembly to operate, and the intermittent transmission lifting seat moves downward to apply pressure to the vortex tube, causing it to change from a flat shape to a conical shape to increase the heat exchange area. S4, at the same time, drives the cleaning component to drive the spiral scraper to rotate and clean the vortex tube Compared with the prior art, the present invention has the following beneficial effects: 1. The vortex tubes are placed horizontally inside the heat exchange tank. Their unique vortex structure significantly increases the contact area with the deionized water in the heat exchange tank. Compared to traditional straight tube structures, they can exchange heat more times per unit time, ensuring more complete heat transfer between the high-temperature steam and the deionized water, significantly improving heat exchange efficiency. On the one hand, the drive motor rotates the central shaft, which in turn causes the multiple vortex tubes to rotate synchronously. Centrifugal force causes the steam to rotate along the inner walls of the vortex tubes, creating turbulent flow. This turbulent flow disrupts the thermal boundary layer, enhancing heat transfer within the fluid and allowing heat to transfer more rapidly from steam to the deionized water. On the other hand, the spiral scraper is spirally arranged inside the vortex tube and fits closely to the inner wall. Its spiral structure further changes the flow state of the steam, providing turbulent conditions for steam flow, further strengthening the heat exchange process and improving heat exchange efficiency. The cooling steam pipe guides the flow of condensate, which is discharged into the liquid storage rack through the drain pipe. Finally, the drain pipe connected by multiple outlet pipes discharges the condensate in a centralized manner, facilitating subsequent reuse of the condensate. Driven by the cleaning component, the spiral scraper can roll inside the vortex tube, thoroughly cleaning the inner wall of the vortex tube and eliminating dirt adhesion. Dirt accumulation can reduce the heat exchange performance of the vortex tube and affect heat exchange efficiency. The automatic cleaning function eliminates the need for frequent manual disassembly of the equipment for cleaning, reducing the workload and downtime of equipment maintenance, lowering maintenance costs, and ensuring that the equipment is always in good operating condition. The spiral arrangement of the spiral scraper can push dirt out of the vortex tube while cleaning it, preventing dirt accumulation and blockage inside the vortex tube, ensuring the cleanliness and smooth flow of the vortex tube, and further improving the reliability and service life of the equipment.

[0016] 2. The lifting seat applies pressure to the vortex tube, causing it to deform from a flat surface to a conical shape. This deformation breaks through the limitations of the traditional two-dimensional plane and increases the contact area between the vortex tube and the liquid in the heat exchange tank. More contact area means that more heat exchanges can be carried out in the same amount of time, which significantly improves the heat exchange efficiency and makes the heat transfer between high-temperature steam and deionized water more sufficient. The deformation of the vortex tube and the rotation of the spiral scraper will change the flow state of the liquid in the heat exchange tank, forming a stronger disturbance. The disturbance of the liquid can destroy the thermal boundary layer, enhance the heat transfer inside the fluid, and enable heat to be transferred from steam to deionized water more quickly, further improving the heat exchange efficiency. The up and down movement of the lifting seat not only deforms the vortex tube, but also drives the spiral scraper to rotate inside the vortex tube through the cooperation of the transmission handle and the sleeve handle. This linkage mechanism ensures that the spiral scraper can fully and continuously clean the inner wall of the vortex tube during its deformation process, effectively removing attached dirt, improving cleaning efficiency, and avoiding the degradation of heat exchange performance caused by dirt accumulation. The intermittent friction between the friction wheel and the vertical tube causes the lifting seat to reciprocate. This reciprocating motion drives the spiral scraper to rotate back and forth within the vortex tube, which can better promote the removal of cleaned impurities, prevent impurities from accumulating and clogging the vortex tube, and ensure the cleanliness and smooth flow of the vortex tube. BRIEF DESCRIPTION OF THE DRAWINGS

[0017] Figure 1 It is a schematic diagram of the three-dimensional structure of the present invention; Figure 2 Schematic diagram of the cross-sectional structure of the heat exchange tank in the present invention; Figure 3 This is a schematic diagram of the structure of the present invention without the heat exchange tank; Figure 4 Schematic diagram of the structure of the vortex tube in the present invention; Figure 5 Schematic diagram of the cross-sectional structure of the vortex tube in the present invention; Figure 6 For the present invention Figure 5 A schematic diagram of the structure at point A in the middle; Figure 7 It is a schematic diagram of the cross-sectional structure of the present invention; Figure 8 For the present invention Figure 7 A magnified schematic diagram of the structure at B in the middle; Figure 9 For the present invention Figure 8 A magnified schematic diagram of the structure at C in the middle; Figure 10 Schematic diagram of the cross-sectional structure of the sealed rotating shell in the present invention; Figure 11 It is a schematic diagram of the cross-sectional structure of the auxiliary rod in the present invention.

[0018] In the figure: 100, heat exchange tank; 200, vortex pipe; 201, inlet shell; 202, second-order exhaust ring; 203, support ring; 204, cooling steam pipe; 205, drain pipe; 206, steam inlet pipe; 207, driving motor; 208, central shaft; 209, liquid storage frame; 210, liquid outlet pipe; 211, support; 212, exhaust pipe; 300, spiral scraper pipe; 301, sealed rotating shell; 302, positioning sheet; 303, ratchet; 304, pawl; 305, tension spring; 306, sleeve handle; 307, transmission handle; 400, lifting seat; 401, connecting frame; 402, scissor-type telescopic frame; 403, abutting wheel; 404, auxiliary rod; 405, sliding rod; 406, spring; 407, counterweight bead; 408, sleeve spring; 409, vertical pipe. DETAILED DESCRIPTION

[0019] The technical solutions in the embodiments of the present application will be described clearly and completely below in combination with the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those skilled in the art without creative labor fall within the scope of protection of the present application.

[0020] Embodiment one: please refer to Figures 1-11 The present application provides a technical solution: a steam heat exchange device based on AI server and using high-temperature-resistant electrode foil formation, comprising a heat exchange tank 100, wherein the heat exchange tank 100 stores deionized water inside, which is convenient for subsequent liquid supply for electrode foil formation, and the heat exchange tank 100 can be filled with water through the top and drained through the bottom.

[0021] It also comprises a vortex pipe 200, which is configured with multiple vortex pipes and arranged uniformly along the central axis of the heat exchange tank 100, the bottom of the heat exchange tank 100 is connected with a steam inlet pipe 206 for inputting high-temperature steam into the multiple vortex pipes 200, and the inside of the heat exchange tank 100 is provided with a centrifugal assembly for driving the multiple vortex pipes 200 to rotate synchronously, by arranging the vortex pipes 200 horizontally in the inside of the heat exchange tank 100, the contact area with the liquid in the heat exchange tank 100 can be increased, at the same time, the steam inlet pipe 206 delivers high-temperature steam into the inside of the vortex pipes 200 to increase the heat exchange efficiency by fully flowing, and the centrifugal assembly can rotate the vortex pipes 200 to accelerate the flow rate of the steam, at the same time, the steam is rotated along the inner wall of the vortex pipes 200 to form turbulent flow under the centrifugal force, thereby increasing the heat exchange efficiency.

[0022] The centrifugal assembly comprises a middle shaft 208 arranged in the heat exchange tank 100 and rotatably connected with one end of the steam inlet pipe 206, and the outer surface of the middle shaft 208 is slidably connected with a plurality of steam inlet shells 201 in communication with the middle shaft 208, and one end of the vortex pipe 200 is in communication with the steam inlet shell 201, and the top of the heat exchange tank 100 is fixedly connected with a driving motor 207 for driving the middle shaft 208 to rotate, the driving motor 207 can drive the middle shaft 208 to rotate to make the plurality of vortex pipes 200 rotate synchronously, and the steam enters the middle shaft 208 through the steam inlet pipe 206 and then enters the steam inlet shell 201 under the action of centrifugal force and then flows into the inside of the vortex pipe 200.

[0023] The inside of the heat exchange tank 100 is provided with a plurality of cooling steam pipes 204 in a diverging manner along the center, and the plurality of cooling steam pipes 204 are in common communication with a plurality of support collars 203, one end of each vortex pipe 200 is in communication with a second-order steam discharge ring 202 rotatably connected with each support collar 203, and the second-order steam discharge ring 202 can discharge the fluid in the vortex pipe 200 into the support collar 203, the cooling steam pipe 204 can be used for secondary use of steam after use, and the cooling steam pipe 204 can guide the flow of condensed water, the support collar 203 can effectively support the vortex pipe 200 to keep stability during rotation, and under the action of centrifugal force, the steam and the condensed water can be discharged into the inside of the support collar 203 through the second-order steam discharge ring 202.

[0024] The outer surface of the heat exchange tank 100 is fixedly connected with a plurality of liquid storage racks 209, one side of the cooling steam pipe 204 is in communication with a plurality of drain pipes 205 extending into the liquid storage rack 209, the bottom of the liquid storage rack 209 is fixedly connected with a supporting leg 211, one side of each liquid storage rack 209 is in communication with a liquid outlet pipe 210, and the plurality of liquid outlet pipes 210 are in common communication with a discharge pipe 212, the combination of the drain pipe 205 and the liquid storage rack 209 can discharge the condensed water, the discharge pipe 212 can concentrate and discharge the condensed water for subsequent reuse.

[0025] Further, it further comprises a spiral scraper 300, which is spirally arranged in the inside of the vortex pipe 200 and adheres to the inner wall of the vortex pipe 200, the inside of the vortex pipe 200 is rotatably connected with a sealing rotating shell 301, and the inside of the sealing rotating shell 301 is fixedly connected with a positioning piece 302 for clamping the spiral scraper 300, the outer surface of the sealing rotating shell 301 is provided with a cleaning assembly for driving the positioning piece 302 to rotate intermittently, the spiral scraper 300 is arranged on the inner wall of the vortex pipe 200, which can provide turbulent flow conditions for the flow of steam, and the vortex pipe 200 is spirally arranged in the inside of the spiral scraper 300, so that when it cooperates with the cleaning assembly, it can clean the inner wall of the vortex pipe 200 comprehensively, thereby eliminating dirt, and the spiral arrangement can push the dirt to move out of the inside of the vortex pipe 200.

[0026] Among them, the cleaning component includes a sleeve handle 306 which is sleeved on the outer surface of the sealed rotating shell 301, and the outer surface of the sealed rotating shell 301 is fixedly connected to the ratchet 303, and the internal rotation of the sleeve handle 306 is connected to a pawl 304 which can be adapted to the ratchet 303, and the top of the pawl 304 is fixedly connected to a tension spring 305 which is fixedly connected to the inner wall of the sleeve handle 306. By setting the transmission sleeve handle 306 to rotate, the pawl 304 can be engaged with the ratchet 303 to drive the sealed rotating shell 301 to move, so that the positioning piece 302 drives the spiral scraper 300 to rotate, and then drives it as a whole to roll in the vortex tube 200, thereby cleaning the inner wall of the vortex tube 200, and the spiral scraper 300 can also push the condensed water to move and discharge.

[0027] Specifically, when in use, high-temperature steam is introduced into the interior of the central shaft 208 through the steam inlet pipe 206. When the steam flows through the central shaft 208, it will be respectively collected into multiple steam inlet shells 201 and then pass through the vortex tube 200 to exchange heat with the liquid in the heat exchange tank 100. During this process, the steam gradually releases heat and then liquefies. The drive motor 207 is started to drive the central shaft 208 to rotate, so that the multiple vortex tubes 200 rotate to generate centrifugal force. Under the action of centrifugal force, the steam is accelerated to move in the vortex tube 200, and the liquid generated by the cooling is cooled. The steam flows along the inner wall of the vortex tube 200. At the same time, the spiral scraper 300 placed in the vortex tube 200 will assist the steam to form turbulence, and the flow along the inner wall of the vortex tube 200 increases the heat exchange efficiency between the steam and the vortex tube 200. After passing through the vortex tube 200, the steam and condensed water will enter the interior of the support ring 203 through the second-stage exhaust ring 202, and then pass through multiple cooling steam pipes 204 to allow the steam and liquid to be reused for a second time. The condensed water will be discharged through the drain pipe 205 and merged into the liquid storage test frame 209, and finally discharged through the drain pipe 212.

[0028] In summary, the vortex tube 200 is placed horizontally inside the heat exchange tank 100, and its unique vortex structure greatly increases the contact area with the deionized water in the heat exchange tank 100. Compared with the traditional straight tube structure, more heat exchanges can be carried out per unit time, making the heat transfer between high-temperature steam and deionized water more sufficient, thereby significantly improving the heat exchange efficiency. On the one hand, the drive motor 207 drives the central shaft 208 to rotate, thereby causing multiple vortex tubes 200 to rotate synchronously. Under the action of centrifugal force, the steam rotates along the inner wall of the vortex tube 200 to form turbulence. The turbulent state can destroy the thermal boundary layer, enhance heat transfer within the fluid, and enable heat to be transferred from steam to deionized water more quickly. On the other hand, the spiral scraper 300 is spirally arranged inside the vortex tube 200 and fits the inner wall. Its spiral structure further changes the flow state of the steam, provides turbulent conditions for the steam flow, further strengthens the heat exchange process, and improves the heat exchange efficiency. The cooling steam pipe 204 guides the flow of condensed water and discharges the condensed water into the liquid storage rack 209 through the drain pipe 205. Finally, the drain pipe 212 connected to multiple liquid outlet pipes 210 discharges the condensed water in a centralized manner, which is convenient for the subsequent reuse of the condensed water. Driven by the cleaning component, the spiral scraper 300 can roll in the vortex tube 200, comprehensively clean the inner wall of the vortex tube 200, and eliminate dirt adhesion. The accumulation of dirt will reduce the heat exchange performance of the vortex tube 200 and affect the heat exchange efficiency. The automatic cleaning function does not require frequent manual disassembly of the equipment for cleaning, which reduces the workload and downtime of equipment maintenance, reduces maintenance costs, and ensures that the equipment is always in good operating condition. The spiral arrangement of the spiral scraper 300 can push the dirt out of the inside of the vortex tube 200 while cleaning the dirt, avoiding the accumulation and blockage of dirt in the vortex tube 200, ensuring the cleanliness and smoothness of the inside of the vortex tube 200, and further improving the reliability and service life of the equipment.

[0029] Example 2: Please refer to Figures 1-11 The present invention also provides a technical solution, which is different from the technical solution of the first embodiment: the steam heat exchange device based on the high-temperature resistant electrode foil for AI server also includes a lifting seat 400, which is arranged above the multiple vortex tubes 200, and the lifting seat 400 can apply pressure to the vortex tubes 200 to cause them to deform. The interior of the heat exchange tank 100 is provided with a trigger component that drives the lifting seat 400 to move and simultaneously drives the cleaning component to operate. By setting the trigger component, downward pressure can be applied to the lifting seat 400, and this force can drive the cleaning component to operate while deforming the vortex tube 200, so that it breaks through the limitations of the two-dimensional plane and increases the heat exchange efficiency with the liquid in the heat exchange tank 100.

[0030] Furthermore, the trigger assembly includes a connecting frame 401 arranged inside the heat exchange tank 100 and fixedly connected to the outer surface of the central axis rod 208, and one side of the connecting frame 401 is rotatably connected to a scissor-type telescopic frame 402 for driving the lifting seat 400 to rise and fall, and the scissor-type telescopic frame 402 is rotatably connected to an interference wheel 403 at one end away from the connecting frame 401, and a vertical tube 409 is provided inside the heat exchange tank 100 for driving the interference wheel 403 to move, and the bottom of the lifting seat 400 is fixedly connected to a transmission handle 307 rotatably connected to one end of the sleeve handle 306. By setting the scissor-type telescopic frame 402, the position of the lifting seat 400 can be effectively controlled. When the scissor-type telescopic frame 402 is extended or retracted, the lifting seat 400 is driven to cooperate with the transmission handle 307 to drive the sleeve handle 306 to rotate.

[0031] Among them, one side of the connecting frame 401 is fixedly connected to an auxiliary rod 404, one end of the auxiliary rod 404 is slidably connected to a slide rod 405 fixedly connected to the interference wheel 403, the outer surface of the slide rod 405 is provided with a spring 406 that drives itself to reset, the interior of the auxiliary rod 404 is slidably connected to a counterweight bead 407 that interferes with one end of the slide rod 405, the top of the steam inlet shell 201 is fixedly connected to a sleeve spring 408 sleeved on the outer surface of the central axis rod 208, and the top of the sleeve spring 408 is fixedly connected to the central axis rod 208. By setting The cooperation between the counterweight ball 407 and the vertical tube 409 can form a transmission by utilizing the rotation of the central axis 208. As the central axis 208 rotates, the counterweight ball 407 is displaced by the centrifugal force, while pushing the slide bar 405 to move and causing the interference wheel 403 to move, thereby driving the scissor-type telescopic frame 402 to change the angle and adjust the height of the lifting seat 400. As the central axis 208 rotates, the interference wheel 403 and the vertical tube 409 will intermittently interfere with each other, thereby completing the reciprocating motion and causing the lifting seat 400 to move upward.

[0032] Specifically, as the vortex tube 200 rotates, the connecting frame 401 on its surface will rotate with it, and the counterweight bead 407 will be affected by the centrifugal force to push the slide bar 405 to move, causing the interference wheel 403 to intermittently interfere with the vertical tube 409, thereby being forced to reset, and then pushing the scissor-type telescopic frame 402 to reset and drive the lifting seat 400 to move downward, applying pressure on the vortex tube 200 to change it from a flat shape to a conical shape. At the same time, the movement of the vortex tube 200 will drive the steam inlet shell 201 to move downward and pull the sleeve spring 408. Subsequently, after the interference wheel 403 passes over the vertical tube 409, the lifting seat 400 will be reset under the action of the spring 406 and the counterweight bead 407, so that the vortex tube 200 returns to a flat shape. Under the action of the sleeve spring 408 It will generate vibration, and when the lifting seat 400 moves downward to push the vortex tube 200 to deform, it will drive the transmission handle 307 to pull one end of the sleeve handle 306 to move, thereby driving it to rotate on the outer surface of the ratchet 303, so that the pawl 304 hits the ratchet 303 and squeezes the tension spring 305 so that it cannot be engaged. When the lifting seat 400 moves up and resets, it will pull the sleeve handle 306 to rotate in the opposite direction on the surface of the ratchet 303, so that the pawl 304 is engaged in the ratchet 303 and drives it to rotate. At this time, the positioning piece 302 in the sealed rotating shell 301 will limit the spiral scraper 300 to rotate together, so that the spiral scraper 300 as a whole rotates inside the vortex tube 200, thereby cleaning the inner wall of the vortex tube 200 and pushing the impurities cleaned to move.

[0033] In summary, the pressure exerted by the lifting seat 400 on the vortex tube 200 causes it to deform, changing from a flat shape to a conical shape. This deformation breaks the traditional two-dimensional plane restriction, increasing the contact area between the vortex tube 200 and the liquid in the heat exchange tank 100. More contact area means more heat exchange can occur in the same amount of time, significantly improving heat exchange efficiency and making the heat transfer between high-temperature steam and deionized water more complete. The deformation of the vortex tube 200 and the rotation of the spiral scraper tube 300 change the flow state of the liquid in the heat exchange tank 100, creating stronger turbulence. The turbulence of the liquid can break the thermal boundary layer, enhance the heat transfer within the fluid, and make the heat transfer from the steam to the deionized water faster, further improving the heat exchange efficiency. The up and down movement of the lifting seat 400 not only deforms the vortex tube 200, but also drives the spiral scraper tube 300 to rotate within the vortex tube 200 through the cooperation of the transmission handle 307 and the sleeve handle 306. This linkage mechanism ensures that the spiral scraper tube 300 can clean the inner wall of the vortex tube 200 comprehensively and continuously during the deformation of the vortex tube 200, effectively removing dirt and improving cleaning efficiency. This avoids the decline in heat exchange performance caused by dirt accumulation, and the intermittent contact between the friction wheel 403 and the vertical pipe 409 causes the lifting seat 400 to move back and forth. This reciprocating motion drives the spiral scraper tube 300 to rotate back and forth within the vortex tube 200, better pushing the removed impurities to move and preventing the impurities from accumulating and blocking in the vortex tube 200, ensuring the cleanliness and smoothness of the vortex tube 200.

[0034] Example Three: Please refer to Figures 1-11 The present application also provides a technical solution, which is different from the technical solution of Example One: a steam heat exchange method based on an AI server using high-temperature-resistant electrode foil, including the following steps: S1, during use, introduce 150℃ boron acid-containing steam into the inside of the central shaft 208 through the steam inlet pipe 206, and the steam flows through the central shaft 208 and then enters the multiple steam inlet shells 201, and then passes through the vortex tube 200 to exchange heat with the liquid in the heat exchange tank 100. In this process, the steam gradually releases heat and then liquefies; S2, start the drive motor 207 to drive the central shaft 208 to rotate, causing the multiple vortex tubes 200 to rotate and generate centrifugal force, which drives the steam to move faster in the vortex tube 200, and at the same time, the liquid generated by the cooling of the steam flows along the inner wall of the vortex tube 200. The spiral scraper tube 300 placed in the vortex tube 200 will assist the steam to form turbulent flow, and the liquid will flow along the inner wall of the vortex tube 200, increasing the heat exchange efficiency between the vortex tube 200 and the liquid. After the steam and condensed water pass through the vortex tube 200, they will enter the inside of the support sleeve 203 through the second-stage steam outlet ring 202, and then pass through the multiple cooling steam pipes 204 to perform secondary utilization of the steam and liquid. The condensed water will be discharged through the drain pipe 205 and collected in the liquid storage frame 209, and finally discharged through the drain pipe 212. S3. As the vortex tube 200 rotates, the connecting frame 401 on its surface will rotate along with it. The counterweight bead 407 will be affected by the centrifugal force to push the slide bar 405 to move, causing the interference wheel 403 to intermittently interfere with the vertical tube 409, thereby being forced to reset, thereby pushing the scissor-type telescopic frame 402 to reset and drive the lifting seat 400 to move downward, applying pressure on the vortex tube 200 to change it from a flat shape to a conical shape. At the same time, the movement of the vortex tube 200 will drive the steam inlet shell 201 to move downward and pull the sleeve spring 408. Subsequently, after the interference wheel 403 passes over the vertical tube 409, the lifting seat 400 will reset under the action of the spring 406 and the counterweight bead 407, so that the vortex tube 200 returns to a flat shape, and it will vibrate under the action of the sleeve spring 408. S4. When the lifting seat 400 moves downward and pushes the vortex tube 200 to deform, it will drive the transmission handle 307 to pull one end of the sleeve handle 306 to move, thereby driving it to rotate on the outer surface of the ratchet 303, so that the pawl 304 hits the ratchet 303 and squeezes the tension spring 305 so that it cannot be engaged. When the lifting seat 400 moves up and resets, it will pull the sleeve handle 306 to rotate in the opposite direction on the surface of the ratchet 303, so that the pawl 304 is engaged in the ratchet 303 and drives it to rotate. At this time, the positioning piece 302 in the sealed rotating shell 301 will limit the spiral scraper 300 to rotate together, so that the spiral scraper 300 as a whole rotates inside the vortex tube 200, thereby cleaning the inner wall of the vortex tube 200 and pushing the cleaned impurities to move.

[0035] It should be noted that, in this document, relational terms such as first and second, etc., are used only to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any actual relationship or order between these entities or operations. Moreover, the terms "comprises," "comprising," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that includes a list of elements includes not only those elements but also other elements not explicitly listed, or elements inherent to such process, method, article, or apparatus.

[0036] While embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions, and variations may be made to these embodiments without departing from the principles and spirit of the invention, and that the scope of the invention is defined by the appended claims and their equivalents.

Claims

1. A steam heat exchange device based on a high temperature resistant electrode foil for an AI server, comprising a heat exchange tank (100), characterized in that: Also includes: The vortex tubes (200) are constructed in a plurality and are uniformly and concentrically arranged along the central axis of the heat exchange tank (100); the bottom of the heat exchange tank (100) is connected to a steam inlet pipe (206) for inputting high-temperature steam into the plurality of vortex tubes (200); and a centrifugal assembly is provided inside the heat exchange tank (100) for driving the plurality of vortex tubes (200) to rotate synchronously; A spiral scraper (300) is spirally arranged inside the vortex tube (200) and is attached to the inner wall of the vortex tube (200); a sealed rotating shell (301) is rotatably connected to the inside of the vortex tube (200); a positioning piece (302) for clamping the spiral scraper (300) is fixedly connected to the inside of the sealed rotating shell (301); and a cleaning component for driving the positioning piece (302) to intermittently rotate is provided on the outer surface of the sealed rotating shell (301); A lifting seat (400) is arranged above the plurality of vortex tubes (200), and the lifting seat (400) can apply pressure to the vortex tubes (200) to cause them to deform. A trigger component is provided inside the heat exchange tank (100) to drive the lifting seat (400) to move and simultaneously drive the cleaning component to operate.

2. The steam heat exchange device based on high-temperature resistant electrode foil for AI server according to claim 1 is characterized in that: The centrifugal assembly comprises a central axis rod (208) arranged inside the heat exchange tank (100) and rotatably connected to one end of the steam inlet pipe (206), the outer surface of the central axis rod (208) being slidably connected to a plurality of steam inlet shells (201) communicating therewith, and one end of the vortex tube (200) being communicated with the steam inlet shell (201), and a driving motor (207) for driving the central axis rod (208) to rotate being fixedly connected to the top of the heat exchange tank (100).

3. The steam heat exchange device based on high-temperature resistant electrode foil for AI server according to claim 1 is characterized in that: A plurality of cooling steam pipes (204) are arranged in a divergent shape inside the heat exchange tank (100) and along the center thereof, and the plurality of cooling steam pipes (204) are commonly connected to a plurality of support collars (203). One end of each of the vortex tubes (200) is connected to a second-stage exhaust ring (202) rotatably connected to each support collar (203), and the second-stage exhaust ring (202) can allow the fluid in the vortex tube (200) to be discharged into the support collar (203).

4. The steam heat exchange device based on high temperature resistant electrode foil for AI server according to claim 2 is characterized in that: The cleaning assembly comprises a sleeve handle (306) sleeved on the outer surface of the sealed rotating shell (301), the outer surface of the sealed rotating shell (301) is fixedly connected to a ratchet (303), the interior of the sleeve handle (306) is rotatably connected to a pawl (304) that can be adapted to the ratchet (303), and the top of the pawl (304) is fixedly connected to a tension spring (305) fixedly connected to the inner wall of the sleeve handle (306).

5. The steam heat exchange device based on the high temperature resistant electrode foil for AI server according to claim 4 is characterized in that: The trigger assembly includes a connecting frame (401) arranged inside the heat exchange tank (100) and fixedly connected to the outer surface of the central axis rod (208), and one side of the connecting frame (401) is rotatably connected to a scissor-type telescopic frame (402) for driving the lifting seat (400) to rise and fall, and one end of the scissor-type telescopic frame (402) away from the connecting frame (401) is rotatably connected to a resistance wheel (403), and a vertical tube (409) for driving the resistance wheel (403) to move is arranged inside the heat exchange tank (100), and the bottom of the lifting seat (400) is fixedly connected to a transmission handle (307) rotatably connected to one end of the sleeve handle (306).

6. The steam heat exchange device based on high temperature resistant electrode foil for AI server according to claim 5 is characterized in that: An auxiliary rod (404) is fixedly connected to one side of the connecting frame (401), and one end of the auxiliary rod (404) is slidably connected to a slide rod (405) fixedly connected to the abutting wheel (403). The outer surface of the slide rod (405) is provided with a spring (406) for driving the slide rod to reset itself, and the interior of the auxiliary rod (404) is slidably connected to a counterweight bead (407) that abuts against one end of the slide rod (405).

7. The steam heat exchange device based on high temperature resistant electrode foil for AI server according to claim 5 is characterized in that: A sleeve spring (408) sleeved on the outer surface of the central axis rod (208) is fixedly connected to the top of the steam inlet shell (201), and the top of the sleeve spring (408) is fixedly connected to the central axis rod (208).

8. The steam heat exchange device based on high temperature resistant electrode foil for AI server according to claim 3 is characterized in that: The outer surface of the heat exchange tank (100) is fixedly connected to a plurality of liquid storage test racks (209), and one side of the cooling steam pipe (204) is connected to a plurality of drainage pipes (205) extending into the liquid storage test rack (209). The bottom of the liquid storage test rack (209) is fixedly connected to a support leg (211).

9. The steam heat exchange device based on high temperature resistant electrode foil for AI server according to claim 8 is characterized in that: One side of each liquid storage and measuring frame (209) is connected to a liquid outlet pipe (210), and a plurality of liquid outlet pipes (210) are commonly connected to a discharge pipe (212).

10. A steam heat exchange method based on a high-temperature resistant electrode foil for an AI server, according to any one of claims 1 to 9, wherein the steam heat exchange device based on a high-temperature resistant electrode foil for an AI server is characterized in that: The following steps are involved: S1, 150°C boric acid-containing steam enters the vortex tube (200) through the steam inlet pipe (206) and exchanges heat with the liquid in the heat exchange tank (100); S2, starting the centrifugal assembly to allow the steam and condensed water to flow rapidly in the vortex tube (200), forming turbulence during the flow process and finally being discharged from the vortex tube (200); S3, the rotation of the vortex tube (200) drives the trigger assembly to operate, and the intermittent transmission lifting seat (400) moves downward to apply pressure to the vortex tube (200) so that it changes from a flat shape to a conical shape to increase the heat exchange area; S4. Simultaneously, the cleaning assembly drives the spiral scraper (300) to rotate to clean the inside of the vortex tube (200).

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