Heat exchanger with impurity treatment function

By designing a heat exchanger with impurity treatment capabilities, continuous cleaning is achieved through heat conduction and agitation mechanisms, solving the problems of high cleaning costs and production continuity associated with existing heat exchangers, and improving production efficiency and stability.

CN121474923APending Publication Date: 2026-02-06WUXI XINRUIDA TECH CO LTD
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Patent Information

Application Number
CN202511950233.2
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-12-23
Publication Date
2026-02-06

AI Technical Summary

Technical Problem

Existing methods for cleaning impurities from heat exchangers are costly, disrupt production continuity, require offline cleaning and additional heating equipment, leading to production interruptions and additional costs.

Method used

A heat exchanger with impurity treatment function was designed, including two sets of heat exchanger bodies distributed at the top and bottom, heat conduction components and a stirring mechanism. It is controlled by connecting pipes and valves, and uses the principle of heat conduction to heat the cleaning fluid. The stirring mechanism enables continuous cleaning and avoids offline cleaning.

Benefits of technology

This technology enables the cleaning of impurities from heat exchangers without interrupting production, reducing cleaning costs and improving production continuity and efficiency.

✦ Generated by Eureka AI based on patent content.

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Abstract

The invention relates to the technical field of impurity cleaning, in particular to a heat exchanger with an impurity treatment function, which comprises a heat conducting assembly and two sets of heat exchanger bodies, the two sets of heat exchanger bodies are distributed up and down, connecting pipes are arranged at the tube pass and shell pass inlet and outlet ends of the two sets of heat exchanger bodies 1 in a communicating mode, middle valve bodies are installed in the middles of the connecting pipes, and side pipe valves are arranged on the upper sections and the lower sections of the connecting pipes in a communicating mode. The heat exchanger has the beneficial effects that the upper heat exchanger body and the lower heat exchanger body are arranged, the connecting pipes are arranged at the inlet ends and the outlet ends of the shell sides and the tube sides of the upper heat exchanger body and the lower heat exchanger body in a communicating mode, and the middle valve bodies and the side tube valves are arranged in the middles and at the two ends of the connecting pipes; the two sets of heat exchanger bodies can be connected into a heat exchange system in series by adjusting the smoothness of the middle valve body and the side pipe valves, or one heat exchanger body is connected into the heat exchange system, and the other heat exchanger body is firstly connected with a high-pressure liquid pump and then connected with a heat conduction assembly, so that impurity cleaning of the heat exchanger bodies is achieved, and production is not interrupted.
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Description

Technical Field

[0001] This invention relates to the field of impurity removal technology, specifically to a heat exchanger with impurity treatment function. Background Technology

[0002] Heat exchangers, as key equipment for energy transfer and recovery in industrial production, are widely used in various industries such as chemical, energy, metallurgy, and refrigeration. During long-term operation, solid impurities such as silt and suspended matter carried by the heat exchange medium gradually accumulate in the heat exchange channels and surfaces. Simultaneously, the medium also generates stubborn impurities such as scale, grease, and biological slime during heat exchange. The presence of these impurities significantly reduces the heat transfer efficiency of the heat exchanger, increases operating energy consumption, and can even cause problems such as channel blockage and equipment corrosion, seriously affecting the operational stability and service life of the heat exchanger. Therefore, it is essential to regularly clean the heat exchanger to achieve energy-efficient heat exchange operation.

[0003] Currently, the industry generally uses offline cleaning methods to remove impurities from heat exchangers. The standard procedure is as follows: first, high-pressure water rinsing is used to remove accumulated solid impurities, followed by chemical cleaning methods such as acid washing and alkaline washing to remove stubborn impurities such as scale and grease. The reaction efficiency of acid washing and alkaline washing is closely related to temperature. To accelerate the chemical reaction rate between the acid / alkali and the impurities, improve cleaning efficiency, and shorten cleaning time, the acid washing temperature is typically controlled at 40–60℃, and the alkaline washing temperature at 60–80℃.

[0004] However, the aforementioned conventional cleaning methods have many inherent drawbacks, severely restricting the economy and continuity of industrial production. On the one hand, to meet the temperature requirements of acid and alkaline washing, enterprises need to equip themselves with corresponding heating devices to heat the cleaning solution. The purchase, installation, and energy consumption of these heating devices undoubtedly increase the additional costs of equipment maintenance and increase the pressure on production operations. On the other hand, both the high-pressure water rinsing stage and the subsequent acid and alkaline washing stages require the normal operation of the heat exchanger to be suspended and disassembled or isolated offline from the production system. This shutdown cleaning mode directly disrupts the normal production rhythm, leading to production interruptions. This not only reduces overall production efficiency but may also cause a series of chain problems such as order delays and capacity losses due to production stagnation.

[0005] In summary, existing methods for cleaning impurities from heat exchangers suffer from high costs and disruptions to production continuity, making them unsuitable for the demands of modern industry for efficient, economical, and continuous production. Summary of the Invention

[0006] The purpose of this invention is to provide a heat exchanger with impurity treatment function to solve the prominent problems of high cost and impact on production continuity of existing heat exchanger impurity cleaning methods mentioned in the background art.

[0007] To achieve the above objectives, the present invention provides the following technical solution: a heat exchanger with impurity treatment function, comprising: The two heat exchanger bodies are distributed vertically, and a connecting pipe is provided at the inlet and outlet ends of the tube side and shell side of the two heat exchanger bodies. A central valve body is installed in the middle of the connecting pipe, and a side valve is provided at the upper and lower sections of the connecting pipe. Closing the central valve body and opening a side valve can control a heat exchanger body to stop working. The heat-conducting components are all rotatably mounted on the connecting frame, and the state of the heat-conducting components is adjustable; the heat-conducting components are detachably sleeved on the heat exchanger body in the working state, and the output end of the heat-conducting components is connected to a side pipe valve. The system consists of a base frame, a vertical shaft, a stirring mechanism, and two parallel stirring drums. Both the vertical shaft and the stirring drums are mounted on the base frame, with the vertical shaft positioned between the two stirring drums. The stirring mechanism is also connected to the vertical shaft. During use, the stirring mechanism can be raised and lowered and rotated around the vertical shaft to alternately mix the materials in the two stirring drums. The stirring drums are connected to the inlet of the heat-conducting component via a pipe and a liquid pump.

[0008] Preferably, the heat-conducting components each include two arc-shaped chambers with a central angle of 180°, the contact surfaces of the two arc-shaped chambers are set as open, and a spiral plate is provided on the inner side of each arc-shaped chamber. A spiral flow channel is formed in the space formed by the two arc-shaped chambers through the two spiral plates; an inlet and outlet pipe communicating with the spiral flow channel is provided at the ends of the two arc-shaped chambers that are far apart from each other.

[0009] Preferably, a frame is provided on each of the two arc-shaped chambers, and an end shaft is fixedly provided on the side of the two frames that are far apart from each other; the connecting frame includes a first support plate and a second support plate with adjustable spacing, and an end tube is fixedly provided on the top of the first support plate and the second support plate, and the two end tubes are connected and sleeved on the end shaft through bearings.

[0010] Preferably, a bottom cylinder is vertically connected to the bottom of the first support plate, and a locking post is fixedly installed on the inner side wall of the bottom cylinder; an insertion shaft is vertically connected to the bottom of the second support plate, and a locking groove is provided on the side wall of the insertion shaft; the insertion shaft extends into the bottom cylinder, and the locking post is located in the locking groove.

[0011] Preferably, the connecting frame also includes a support rod, with the two ends of the support rod connected to the connecting devices of the two heat exchanger bodies. An arc-shaped plate is fixedly installed in the middle of the support rod, and an annular plate is fixedly installed on the arc-shaped plate. The bottom cylinder extends into the space formed by the annular plate and the annular plate. The bolt installed through the middle annular plate can simultaneously penetrate the bottom cylinder and the insert shaft.

[0012] Preferably, the stirring mechanism is installed at one end of the horizontal plate, and a linear bearing is installed at the other end of the horizontal plate. The linear bearing is slidably sleeved on the vertical shaft. The bottom of the telescopic cylinder located on the side of the vertical shaft is connected to the base frame, and the telescopic end of the telescopic cylinder is connected to the side plate rotatably mounted on the linear bearing.

[0013] Preferably, two clamping arc plates are bolted together on the vertical shaft, and a brake rod is fixedly installed on the side of the two clamping arc plates that is far apart from each other; a brake hole is provided on the horizontal plate; after the stirring mechanism extends into a certain stirring drum, a certain brake rod extends into the brake hole.

[0014] Preferably, a drive motor is installed on the horizontal plate, and a drive gear is fixedly installed on the power output shaft of the drive motor; a fixed gear is sleeved on the top of the vertical shaft, and a bolt is installed through the connecting pipe installed on the fixed gear, and the bolt is installed through a connecting hole of the vertical shaft; after the stirring mechanism rises, the drive gear and the fixed gear mesh, and the drive motor drives the stirring mechanism to rotate.

[0015] Preferably, multiple wheels are installed under the base frame, two sets of brackets are fixedly installed above the base frame, and a support pipe is fixedly installed between the two sets of brackets.

[0016] Preferably, the bottom of the vertical shaft is bolted into the support tube; the two mixing drums are respectively mounted on two sets of brackets; a control module is also provided on the base frame, and the control module is electrically connected to the liquid pump, the telescopic cylinder and the drive motor.

[0017] Compared with the prior art, the beneficial effects of the present invention are: 1. The present invention provides two heat exchanger bodies, one upper and one lower, with connecting pipes at the inlet and outlet ends of their shell and tube sides. A central valve body and a side valve are provided at the middle and both ends of the connecting pipes. By adjusting the flow of the central valve body and the side valves, the two heat exchanger bodies can be connected in series to the heat exchange system, or one heat exchanger body can be connected to the heat exchange system while the other is first connected to the high-pressure liquid pump and then to the heat transfer components. This allows for the cleaning of impurities from the heat exchanger bodies without interrupting production.

[0018] 2. The heat-conducting component of this invention includes two arc-shaped chambers, which are rotatably mounted on a first support plate and a second support plate. The first and second support plates are adjustablely mounted on a support rod. Therefore, after the arc-shaped chambers are detached from the heat exchanger body, the first and second support plates can be controlled to rotate around the bottom cylinder and the insertion shaft to the side of another heat exchanger body, and then the arc-shaped chambers can be pushed close to the heat exchanger body. Finally, the two arc-shaped chambers are connected by bolts to fit against the heat exchanger body, and the pickling solution or alkaline cleaning solution is heated by the principle of heat conduction, changing the previous situation where additional heating equipment was required and reducing the cost of impurity cleaning.

[0019] 3. The present invention has a vertical shaft between two stirring cylinders, and a stirring mechanism is provided on the side of the vertical shaft. The stirring mechanism can rotate around the vertical shaft. Therefore, during the process of conveying the washing liquid to the heat exchanger body in one stirring cylinder, the position of the stirring mechanism can be adjusted so that it extends into the other stirring cylinder and mixes the material in the stirring cylinder. Repeating this step can achieve continuous cleaning of the heat exchanger body. Attached Figure Description

[0020] Figure 1 This is a schematic diagram of the overall structure of the present invention; Figure 2 This is a schematic diagram of the heat exchanger and heat conduction components of the present invention; Figure 3 This is a schematic diagram of the structure of the heat-conducting component, support plate, and support rod of the present invention; Figure 4 This is a schematic diagram of the structure of the support plate and support rod of the present invention; Figure 5 This is a schematic diagram of the structure of the first support plate of the present invention; Figure 6 This is a schematic diagram of the structure of the second support plate of the present invention; Figure 7 This is a schematic diagram of the support rod of the present invention; Figure 8 This is a first structural schematic diagram of the heat-conducting component of the present invention; Figure 9 This is a schematic diagram of the second structure of the heat-conducting component of the present invention; Figure 10 This is a first structural schematic diagram of the stirring tank and stirring mechanism of the present invention; Figure 11 This is a second structural schematic diagram of the stirring tank and stirring mechanism of the present invention; Figure 12 This is a schematic diagram of the stirring mechanism and base frame of the present invention; Figure 13 This is a schematic diagram of the structure of the base frame of the present invention; Figure 14 This is a schematic diagram of the vertical shaft, stirring mechanism, and telescopic cylinder of the present invention; Figure 15 This is a schematic diagram of the vertical axis structure of the present invention; Figure 16 This is a schematic diagram of the structure of the horizontal plate and drive motor of the present invention.

[0021] The components represented by each number in the attached diagram are listed below: 1. Heat exchanger body; 2. Heat transfer assembly; 3. Stirring drum; 4. Base frame; 5. Connecting pipe; 6. Central valve body; 7. Side valve; 8. First support plate; 9. Second support plate; 10. Support rod; 11. End pipe; 12. Bottom cylinder; 13. Clamping post; 14. Clamping groove; 15. Insert shaft; 16. Arc plate; 17. Annular plate; 18. Flow channel; 19. Frame; 20. End shaft; 21. Spiral plate; 22. 23. Liquid pump; 24. Vertical shaft; 25. Stirring mechanism; 26. Bracket; 27. Telescopic cylinder; 28. Support pipe; 29. ​​Horizontal plate; 30. Connecting hole; 31. Fixed gear; 32. Clamping arc plate; 33. Brake lever; 34. Connecting pipe; 35. Annular end plate; 36. Brake hole; 37. Side plate; 38. Linear bearing; 39. Drive gear; 40. Drive motor; 41. Walking wheel; 42. Liquid inlet pipe; 43. Liquid delivery pipe; 44. Control module. Detailed Implementation

[0022] The technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of the present invention.

[0023] This invention provides a technical solution: In order to solve the prominent problems of high cost and impact on production continuity of existing heat exchanger impurity cleaning methods, this embodiment provides a new heat exchanger.

[0024] like Figure 1 , Figure 2 , Figure 10-12 As shown, the heat exchanger includes two heat exchanger bodies 1, a heat conduction assembly 2, a base frame 4, a vertical shaft 23, a stirring mechanism 24, and two parallel stirring drums 3, etc.

[0025] like Figure 2As shown, two heat exchanger bodies 1 are connected vertically via connecting devices. Connecting pipes 5 are installed at both the tube and shell sides of the two heat exchanger bodies 1, and a central valve body 6 is installed in the middle of the connecting pipe 5. Side valves 7 are also installed at both ends of the connecting pipe 5. When both heat exchanger bodies 1 are operating normally, to connect them in series, one end of the connecting pipe 5 at the tube and shell sides of the two heat exchanger bodies 1 is open, while the other end of the connecting pipe 5 is cut off via the central valve body 6. Then, the two side valves 7 of the cut connecting pipe 5 are connected to the heat exchange system, thus enabling heat exchange between two media at different temperatures through the two heat exchanger bodies 1. When it is necessary to clean impurities from a heat exchanger body 1, close the middle valve 6 of the connecting pipes 5 at both ends of the tube side and shell side. Then, connect the side pipe valve 7, which communicates with the working heat exchanger body 1, to the heat exchange system. Connect the other end of the heat exchanger body 1 to the heat transfer assembly 2 or directly to the output end of the high-pressure liquid pump. When connected to the high-pressure liquid pump, the tube side and shell side can be flushed with high-pressure water; when connected to the heat transfer assembly 2, the tube side and shell side can be acid-washed, alkaline-washed, etc. This setup reduces the impact of cleaning the heat exchanger on production.

[0026] like Figure 2 As shown, the heat-conducting components 2 are rotatably mounted on the connecting frame, which is connected to the connecting devices of the two heat exchanger bodies 1. Therefore, the heat-conducting components 2 are in a stable installation state. Furthermore, the state of the heat-conducting components 2 is adjustable, and they can move relative to the connecting frame. Therefore, the heat-conducting components 2 can be detachably mounted on the heat exchanger body 1 in the working state. That is, after removing the insulation layer of the heat exchanger body 1, the heat-conducting components 2 can directly contact the heat exchanger body 1, thereby utilizing the principle of heat conduction to increase the temperature of the pickling and alkaline cleaning solutions flowing through the heat-conducting components 2, changing the previous requirement of separate heating equipment. When pickling or alkaline cleaning of the heat exchanger body 1 is required, the output end of the heat-conducting components 2 is connected to a side valve 7.

[0027] like Figure 12As shown, both the vertical shaft 23 and the stirring drum 3 are mounted on the base frame 4, with the vertical shaft 23 positioned between the two stirring drums 3. The stirring mechanism 24 is connected to the vertical shaft 23. When the heat exchanger body 1 needs to be acid-washed or alkali-washed, the acid-washing or alkali-washing raw material is injected into the stirring drum 3, and then mixed by the stirring mechanism 24. Finally, the liquid delivery pipe 42 at the bottom of the stirring drum 3 is connected to the inlet end of the heat-conducting component 2 via the pipe body and the liquid pump 22, so that the acid-washing solution or alkali-washing solution can be delivered to the heat exchanger body 1 by the liquid pump 22. When the acid-washing solution or alkali-washing solution is output from one of the stirring drums 3, the stirring mechanism 24 rises along the vertical shaft 23 and detaches from that stirring drum 3. Then, the stirring mechanism 24 rotates around the vertical shaft 23 and descends to extend into the other stirring drum 3 to mix the material in the other stirring drum 3. By repeating the above steps, the materials in the two mixing drums 3 can be alternately mixed by the lifting and rotating of the stirring mechanism 24 around the vertical axis 23, thus avoiding the impact of the mixing of acid or alkali washing solution on the impurity removal process of the heat exchanger body 1.

[0028] like Figure 8 As shown, in order to fit the heat-conducting component 2 onto a heat exchanger body 1 and provide a channel for the flow of pickling liquid or alkaline cleaning liquid, the heat-conducting component 2 includes two arc-shaped chambers with a central angle of 180°. After the two arc-shaped chambers are placed in close contact with the heat exchanger body 1, their contact edges are connected by bolts, thereby making the arc-shaped chambers fit in close contact with the heat exchanger body 1.

[0029] like Figure 8 , Figure 9 As shown, the contact surfaces of the two arc-shaped chambers are both open, and a spiral plate 21 is provided on the inner side of each arc-shaped chamber. A spiral flow channel 18 is formed in the space formed by the two arc-shaped chambers through the two spiral plates 21. In addition, an inlet and outlet pipe communicating with the spiral flow channel 18 is provided at the ends of the two arc-shaped chambers that are far apart from each other. The liquid pump 22 is connected to one inlet and outlet pipe, and the other inlet and outlet pipe is connected to the side pipe valve 7. This allows the contact time between the liquid pump 22 and the heat exchanger body 1 to be extended through the spiral flow channel 18 when the liquid pump 22 is delivering pickling solution or alkaline washing solution. By adjusting the delivery pressure, it is convenient to heat the pickling solution or alkaline washing solution through the heat exchanger body 1.

[0030] like Figure 3 , Figure 4 , Figure 8As shown, in order to adjust the position of the heat-conducting component 2 according to the cleaning requirements and to fit it onto another heat exchanger body 1, frames 19 are provided on both arc-shaped chambers, and end shafts 20 are fixedly provided on the sides of the two frames 19 that are far apart from each other. The connecting frame includes a first support plate 8 and a second support plate 9 with adjustable spacing. End pipes 11 are fixedly provided on the top of the first support plate 8 and the second support plate 9. The two end pipes 11 are connected to the end shafts 20 through bearings, realizing the rotational connection between the arc-shaped chambers and the first support plate 8 and the second support plate 9. That is, after the first support plate 8 and the second support plate 9 drive the arc-shaped chamber away from the heat exchanger body 1, the arc-shaped chamber can be controlled to rotate 180° so that it faces the other heat exchanger body 1. Then the spacing of the first support plate 8 and the second support plate 9 can be controlled and adjusted so that the arc-shaped chamber fits onto the heat exchanger body 1.

[0031] like Figure 5 , Figure 6 As shown, a bottom cylinder 12 is vertically and rotatably connected to the bottom of the first support plate 8, and a locking post 13 is fixedly installed on the inner side wall of the bottom cylinder 12. A shaft 15 is vertically and rotatably connected to the bottom of the second support plate 9, and a slot 14 is provided on the side wall of the shaft 15. The shaft 15 extends into the bottom cylinder 12, and the locking post 13 is located in the slot 14. This arrangement achieves a stable connection between the first support plate 8 and the second support plate 9, and provides convenience for adjusting the distance between the two arc-shaped compartments.

[0032] like Figure 4 , Figure 7 As shown, the connecting frame also includes a support rod 10. Both ends of the support rod 10 are connected to the connecting devices of the two heat exchanger bodies 1. An arc-shaped plate 16 is fixedly installed in the middle of the support rod 10, and an annular plate 17 is fixedly installed on the arc-shaped plate 16. The bottom cylinder 12 extends into the space formed by the arc-shaped plate 16 and the annular plate 17. Therefore, the first support plate 8 and the second support plate 9 can be stably installed with the support of the support rod 10. After the arc-shaped chamber is placed close to the heat exchanger body 1, the bolts that pass through the annular plate 17 in the middle also pass through the bottom cylinder 12 and the insert shaft 15, restricting the position of the first support plate 8 and the second support plate 9. If it is necessary to adjust the position of the heat-conducting component 2, the bolts are removed to release the restriction between the bottom cylinder 12 and the insert shaft 15.

[0033] like Figure 14 , Figure 16 As shown, the stirring mechanism 24 uses a previously disclosed device, which is mounted on an annular end plate 34 at the end of the horizontal plate 28. A linear bearing 37 is mounted on the other end of the horizontal plate 28, and the linear bearing 37 is slidably sleeved on the vertical shaft 23. The bottom of the telescopic cylinder 26, which is located on the side of the vertical shaft 23, is connected to the base frame 4, and the telescopic end of the telescopic cylinder 26 is connected to the side plate 36. The side plate 36 is sleeved on the linear bearing 37 through a bearing connection. Therefore, when the telescopic cylinder 26 is working, the horizontal plate 28 can be raised and lowered, which facilitates adjusting the height of the stirring mechanism 24 to enter and exit the stirring drum 3.

[0034] like Figure 15 As shown, in order to ensure the stable installation of the stirring mechanism 24 after it extends into a stirring drum 3, two clamping arc plates 31 are bolted together on the vertical shaft 23. A brake rod 32 is fixedly installed on the side of each clamping arc plate 31 that is furthest from the other. A brake hole 35 is provided on the horizontal plate 28; after the stirring mechanism 24 extends into the stirring drum 3, one of the brake rods 32 extends into the brake hole 35, braking the horizontal plate 28 to prevent the stirring mechanism 24 from impacting the stirring drum 3.

[0035] like Figure 15 , Figure 16 As shown, to adjust the orientation of the stirring mechanism 24 after it rises, a drive motor 39 is mounted on the horizontal plate 28, and a drive gear 38 is fixedly mounted on the power output shaft of the drive motor 39. A fixed gear 30 is sleeved on the top of the vertical shaft 23. After the stirring mechanism 24 rises, the drive gear 38 and the fixed gear 30 mesh, and the drive motor 39 drives the stirring mechanism 24 to rotate, thereby driving the horizontal plate 28 and the stirring mechanism 24 to rotate, and positioning them directly above the other stirring drum 3. The drive motor 39 here can be a stepper motor, servo motor, etc.

[0036] like Figure 15 As shown, in order to stably mount the fixed gear 30 on the vertical shaft 23, a connecting pipe 33 is fixedly installed on the fixed gear 30, and a bolt is installed through the connecting pipe 33. The bolt is installed through a connecting hole 29 of the vertical shaft 23. There are multiple connecting holes 29, which are distributed along the height direction of the vertical shaft 23.

[0037] like Figure 10 , Figure 12 , Figure 13 As shown, multiple casters 40 are installed below the base frame 4 for easy adjustment of their position as needed. Two sets of brackets 25 are fixedly installed above the base frame 4, and two stirring drums 3 are respectively mounted on the two sets of brackets 25, ensuring stable installation of the stirring drums 3 on the base frame 4. Additionally, a liquid inlet pipe 41 is installed on the top of the stirring drum 3, which can be connected to another liquid pump 22 for liquid input. A support pipe 27 is fixedly installed between the two sets of brackets 25, and the bottom of the vertical shaft 23 is bolted into the support pipe 27. A control module 43 is also installed on the base frame 4. The control module 43 is equipped with corresponding components according to existing technology to electrically connect to the liquid pump 22, the telescopic cylinder 26, and the drive motor 39, and to control the operation of the liquid pump 22, the telescopic cylinder 26, and the drive motor 39. The control module 43 is also electrically connected to the mains power supply for operation.

[0038] It should be noted that, in this document, relational terms such as "first" and "second" are used only to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Furthermore, the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such a process, method, article, or apparatus.

[0039] Although embodiments of the invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the invention, the scope of which is defined by the appended claims and their equivalents.

Claims

1. A heat exchanger with a function of treating impurities, characterized by comprising: The utility model relates to a heat exchanger, which comprises: two sets of heat exchanger bodies (1) arranged in an up-down manner, a connecting pipe (5) arranged at the inlet and outlet of the tube side and shell side of the two sets of heat exchanger bodies (1), a middle valve body (6) installed at the middle part of the connecting pipe (5), and a side pipe valve (7) arranged at the upper and lower parts of the connecting pipe (5); the middle valve body (6) is closed and a certain side pipe valve (7) is opened to control the suspension of a certain set of heat exchanger body (1); a heat conduction assembly (2) rotatably arranged on a connecting frame and adjustable in state; the heat conduction assembly (2) is detachably arranged on the heat exchanger body (1) in a working state, and the output end of the heat conduction assembly (2) is connected with a certain side pipe valve (7); a base frame (4), a vertical shaft (23), a stirring mechanism (24), and two parallel stirring barrels (3); the vertical shaft (23) and the stirring barrels (3) are both installed on the base frame (4), the vertical shaft (23) is located between the two stirring barrels (3), and the stirring mechanism (24) is connected with the vertical shaft (23); during use, the stirring mechanism (24) can be lifted and rotated around the vertical shaft (23) to alternately mix the materials in the two stirring barrels (3); the liquid outlet pipe (42) at the bottom of the stirring barrel (3) is connected with the inlet end of the heat conduction assembly (2) through a pipe body and a liquid pump (22).

2. The heat exchanger with impurity treatment function according to claim 1, characterized in that: Each heat conduction assembly (2) comprises two arc-shaped warehouses with a central angle of 180°, the contact surfaces of the two arc-shaped warehouses are both arranged as openings, a spiral plate (21) is arranged on the inner side of each arc-shaped warehouse, a spiral flow channel (18) is formed in the space formed by the two arc-shaped warehouses through the two spiral plates (21), and an inlet and outlet pipe is arranged at the end of the two arc-shaped warehouses away from each other and communicated with the spiral flow channel (18).

3. The heat exchanger with impurity treatment function according to claim 2, characterized in that: A frame (19) is arranged on each arc-shaped warehouse, and an end shaft (20) is fixedly arranged on the side of the two frames (19) away from each other; the connecting frame comprises a first supporting plate (8) and a second supporting plate (9) with adjustable spacing, end pipes (11) are fixedly arranged on the top of the first supporting plate (8) and the second supporting plate (9), and the two end pipes (11) are sleeved on the end shaft (20) through a bearing.

4. The heat exchanger with impurity treatment function according to claim 3, characterized in that: A bottom barrel (12) is vertically connected to the bottom of the first supporting plate (8), a clamping column (13) is fixedly arranged on the inner side wall of the bottom barrel (12); a plug shaft (15) is vertically connected to the bottom of the second supporting plate (9), a clamping groove (14) is arranged on the side wall of the plug shaft (15); the plug shaft (15) extends into the bottom barrel (12), and the clamping column (13) is located in the clamping groove (14).

5. The heat exchanger with impurity treatment function according to claim 4, characterized in that: The connecting frame further comprises a support rod (10) having two ends connected with the connecting devices of the two sets of heat exchanger bodies (1), an arc-shaped plate (16) fixedly arranged at the middle part of the support rod (10), an annular plate (17) fixedly arranged on the arc-shaped plate (16), and the bottom cylinder (12) extending into the space formed by the arc-shaped plate (16) and the annular plate (17). A bolt arranged through the middle part of the annular plate (17) can simultaneously penetrate the bottom cylinder (12) and the inserting shaft (15) to fix the relative positions of the bottom cylinder (12) and the inserting shaft (15).

6. The heat exchanger with impurity treatment function according to claim 1, characterized in that: The stirring mechanism (24) is mounted on the annular end plate (34) at the end of the horizontal plate (28), a linear bearing (37) is mounted at the other end of the horizontal plate (28), the linear bearing (37) is slidably sleeved on the vertical shaft (23), the bottom of the telescopic cylinder (26) arranged at the side of the vertical shaft (23) is connected with the bottom frame (4), and the telescopic end of the telescopic cylinder (26) is connected with the side plate (36) rotatably mounted on the linear bearing (37).

7. The heat exchanger with impurity treatment function according to claim 6, characterized in that: Two clamping arc plates (31) are sleeved on the vertical shaft (23) and connected by bolts, and a brake lever (32) is fixedly arranged at the side away from the clamping arc plate (31); a brake hole (35) is arranged on the horizontal plate (28); after the stirring mechanism (24) extends into a stirring cylinder (3), one of the brake levers (32) extends into the brake hole (35).

8. The heat exchanger with impurity treatment function according to claim 7, characterized in that: A driving motor (39) is mounted on the horizontal plate (28), a driving gear (38) is fixedly arranged on the power output shaft of the driving motor (39), a fixed gear (30) is sleeved on the top of the vertical shaft (23), a bolt is arranged through the connecting pipe (33) mounted on the fixed gear (30) and a connecting hole (29) of the vertical shaft (23); after the stirring mechanism (24) is raised, the driving gear (38) and the fixed gear (30) are engaged, and the driving motor (39) drives the stirring mechanism (24) to rotate.

9. The heat exchanger with impurity treatment function according to claim 1, characterized in that: A plurality of traveling wheels (40) are mounted below the bottom frame (4), two sets of supports (25) are fixedly arranged above the bottom frame (4), and a support pipe (27) is fixedly arranged between the two sets of supports (25).

10. The heat exchanger with impurity treatment function according to claim 9, characterized in that: The bottom of the vertical shaft (23) is connected by a bolt and inserted into the support pipe (27); the two stirring cylinders (3) are respectively mounted on the two sets of supports (25), and the top of the stirring cylinder (3) is provided with a liquid inlet pipe (41); a control module (43) is further arranged on the bottom frame (4), and the control module (43) is electrically connected with the liquid pump (22), the telescopic cylinder (26) and the driving motor (39).