Vertical anti-blocking shell-and-tube heat exchanger
By employing a vertical anti-clogging design and an adaptive mechanism, the problems of vibration, clogging, and uneven flow in traditional shell-and-tube heat exchangers are solved, achieving efficient anti-clogging and adaptive adjustment, and improving the stability and service life of the heat exchanger.
Patent Information
- Application Number
- CN202510254868.2
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2025-03-05
- Publication Date
- 2025-11-11
- Estimated Expiration
- 2045-03-05
AI Technical Summary
Traditional shell-and-tube heat exchangers have significant technical shortcomings in terms of vibration, blockage, and uneven flow, resulting in decreased heat exchange efficiency, increased maintenance frequency, and a lack of effective anti-blockage and adaptive adjustment capabilities.
It adopts a vertical anti-clogging design, combined with a conversion mechanism and an adaptive mechanism. Through the staggered setting of the exchange tube and turbine drive, it achieves dynamic anti-clogging and flow self-adaptation, reduces the risk of resonance, and improves the media residence time and flow stability.
It effectively prevents friction leakage in the heat exchange tubes, improves heat exchange efficiency and equipment stability, avoids blockage, and enhances equipment applicability and service life.
Smart Images

Figure CN119826582B_ABST
Abstract
Description
Technical Field
[0001] This invention relates to the field of heat exchanger equipment technology, specifically a vertical anti-clogging shell-and-tube heat exchanger. Background Technology
[0002] Shell-and-tube heat exchangers, as key equipment in industrial heat transfer, are widely used in chemical, energy, and refrigeration systems. Their performance directly affects heat conversion efficiency and operational stability. Traditional shell-and-tube heat exchangers typically use fixed-arrangement heat exchange tubes to exchange heat with the shell-side fluid. However, in practical applications, they often face challenges such as tube wear caused by vibration, localized blockage due to uneven medium flow, and leakage risks caused by mechanical vibration. Especially when handling fluids containing impurities or with high viscosity, traditional equipment lacks effective anti-clogging designs, easily leading to decreased heat exchange efficiency, increased maintenance frequency, and the rigid structure's inability to suppress resonance effects, further exacerbating equipment wear. While existing technologies attempt to alleviate these problems by optimizing tube layout or adding support structures, a synergistic optimization of anti-clogging, vibration reduction, and adaptive adjustment has not yet been achieved.
[0003] However, existing shell-and-tube heat exchangers still have significant technical shortcomings: First, traditional tube bundle support structures (such as baffles) are mostly rigid connections, which cannot effectively absorb equipment vibration energy, leading to resonant friction between the heat exchange tubes and the shell, accelerating tube wall wear and increasing the risk of leakage; Second, the lack of a dynamic anti-clogging mechanism makes it easy for impurities to accumulate in the shell-side fluid in low-velocity regions, especially under fluctuating flow conditions, making it difficult to avoid clogging through self-cleaning design; Third, fixed flow channel designs cannot adaptively adjust the heat exchange tube flux according to the medium flow rate, resulting in insufficient flow velocity in some tube bundles at low loads, exacerbating fouling accumulation; Fourth, traditional equipment lacks optimization of the flow path of hot and cold media, resulting in short medium residence time and limited heat exchange efficiency. These defects restrict the long-term stable operation and energy efficiency improvement of heat exchangers, and breakthroughs are urgently needed through the integration of elastic vibration reduction, dynamic anti-clogging, and flow adaptive technologies. Summary of the Invention
[0004] (a) Technical problems to be solved
[0005] This invention provides a vertical, anti-clogging shell-and-tube heat exchanger that solves the problems mentioned in the background section.
[0006] (II) Technical Solution
[0007] To achieve the above objectives, the present invention provides the following technical solution: a vertical anti-clogging shell-and-tube heat exchanger, comprising a heat exchange tube, a top cover fixedly fastened to the top outer surface of the heat exchange tube, and a bottom cover fixedly connected to the bottom of the heat exchange tube, wherein the diameter of the heat exchange tube is smaller than that of the top cover and the bottom cover, and further comprising:
[0008] The conversion mechanism is fixedly installed inside the heat exchange tube;
[0009] An adaptive mechanism is fixedly installed inside the base cover and positioned directly below the conversion mechanism, with its top contacting and fitting against the bottom of the conversion mechanism.
[0010] The conversion mechanism includes a heat inlet pipe, which is fixedly connected to the top outer surface of the heat exchange tube. A heat outlet pipe is fixedly connected to the bottom outer surface of the heat exchange tube. A cold inlet pipe is fixedly connected to the outer surface of the bottom cover. A cold outlet pipe is fixedly connected to the outer surface of the top cover. Fixed plates are fixedly installed on the inner surfaces of both ends of the heat exchange tube. A connecting rod is fixedly connected to the surfaces of the two fixed plates that are close to each other. An exchange tube is fixedly connected to the outer surface of the fixed plate. Two sets of exchange tubes are provided, and the two sets of exchange tubes are symmetrically arranged. The two ends of the exchange tubes are respectively connected to the bottom cover and the top cover.
[0011] Preferably, the heat inlet pipe and the heat outlet pipe are arranged inside the fixed plate, and a first stabilizing plate is fixedly arranged on the inner surface of the heat exchange tube. The first stabilizing plate is fixedly sleeved on the outer surface of one group of heat exchange tubes, and four first stabilizing plates are arranged at fixed intervals along the inner surface of the heat exchange tube.
[0012] Preferably, a second stabilizing plate is fixedly installed on the inner surface of the heat exchange tube away from the first stabilizing plate. The second stabilizing plate is fixedly sleeved on the outer surface of another set of heat exchange tubes. Five second stabilizing plates are fixedly spaced along the inner surface of the heat exchange tube. The first and second stabilizing plates are fixedly connected to the fixed plate by a connecting rod.
[0013] Preferably, the first and second stabilizing plates are semi-circular and staggered. A rubber ring is fixedly connected to the outer surface of the fixed disk, and the outer side of the rubber ring is fixedly connected to the inner surface of the heat exchange tube. Rubber rings are also fixedly connected to the outer surfaces of the first and second stabilizing plates.
[0014] Preferably, the adaptive mechanism includes a turbine, a rotating rod is fixedly connected to the middle of the turbine, and the bottom of the turbine is rotatably connected to the bottom inner surface of the base via the rotating rod. The turbine and the base are set to the same central axis, and the outer side of the turbine is positioned directly opposite the cooling inlet pipe.
[0015] Preferably, an isolation ring is fixedly connected to the upper surface edge of the turbine, the isolation ring is disposed above the cooling inlet pipe, the side surface of the isolation ring is rotatably connected to the middle inner surface of the bottom cover, and the inner diameter of the isolation ring is smaller than the diameter of the turbine.
[0016] Preferably, a first plug rod is provided above the turbine. The first plug rod is arc-shaped, and plug grooves are provided on both sides of the first plug rod. A second plug rod is slidably inserted into the plug grooves. The first plug rod and the second plug rod are combined to form a ring.
[0017] Preferably, a telescopic rod is fixedly connected to the outer surface of the second plug rod, the first telescopic rod is elastic, and the end of the first telescopic rod away from the second plug rod is fixedly connected to the inner surface of the bottom cover.
[0018] Preferably, the inner surface of the first plug-in rod is provided with a sliding groove, and a counterweight is slidably connected in the sliding groove. A second telescopic rod is fixedly connected to the inner surface of the counterweight. A connecting seat is fixedly connected to the end of the second telescopic rod away from the counterweight. The bottom surface of the connecting seat is fixedly connected to the top of the rotating rod. Three counterweights are fixedly spaced along the central axis of the connecting seat. A friction strip is fixedly embedded in the inner side of the first plug-in rod. An isolation membrane is fixedly connected to the bottom surface of the first plug-in rod. The isolation membrane is annular, and its outer end is fixedly connected to the inner surface of the bottom cover. When this heat exchanger is needed, the cold medium can be introduced from the cold inlet pipe, and the hot medium can be introduced from the heat inlet pipe simultaneously. After the cold medium enters the bottom cover, it will be transported through the exchange tube and then enter the top cover, and finally exit through the cold outlet pipe. After the hot medium enters the heat exchange tube, it will be transported from the top to the bottom of the heat exchange tube, contacting the outer surface of the heat exchange tube during the process to complete the heat exchange operation, and finally exit through the heat outlet pipe at the bottom.
[0019] (III) Beneficial Effects
[0020] This invention provides a vertical, anti-clogging shell-and-tube heat exchanger. It offers the following advantages:
[0021] (I) This vertical, anti-clogging shell-and-tube heat exchanger isolates the exchange tubes by inserting them between the No. 1 and No. 2 stabilizing plates. This ensures the exchange tubes are in a relatively dispersed state during operation, avoiding the risk of leakage due to friction between the tubes caused by equipment vibration. Furthermore, after the hot medium enters the heat exchange tubes, the staggered arrangement between the No. 1 and No. 2 stabilizing plates causes the hot medium to flow in an S-shape towards the bottom within the heat exchange tubes, significantly increasing the residence time of the hot medium and thus greatly improving the heat exchange effect. During the heat exchange process of the cold medium passing through the exchange tubes, due to the No. 1 stabilizing plate… The first and second stabilizing plates are connected to the fixed plate as a whole via a connecting rod. The rubber ring allows the first, second, and fixed plates to have a certain range of motion. This greatly reduces the vibration generated by the equipment body during operation when it is transmitted to the first, second, and fixed plates, thereby significantly reducing the possibility of resonance between the heat exchange tube and the equipment. This protects the heat exchange tube and prevents it from rupturing and leaking due to frequent resonance with the equipment during operation. It also significantly improves the service life of the heat exchanger and enhances its operational stability.
[0022] (II) In this vertical anti-clogging shell-and-tube heat exchanger, the cold medium is continuously sprayed onto the turbine through the inlet pipe when it enters the bottom cover. The turbine is automatically driven to rotate when the cold medium enters the bottom cover. The rotation of the turbine keeps the cold medium in the bottom cover in a constant state of motion, avoiding the problem of pressure dead zones and impurity accumulation that would eventually cause blockage of the heat exchanger after the cold medium enters the bottom cover. This further improves the service life of the heat exchanger. In addition, the isolation ring ensures that the cold medium can only be transported through the gap between the turbine blades when it first enters the bottom cover, thereby increasing the impact force of the cold medium on the turbine. This ensures that the turbine can still be driven to work under low flow heat exchange conditions, which greatly improves the applicability of the heat exchanger.
[0023] (III) This vertical anti-clogging shell-and-tube heat exchanger automatically adjusts its turbine speed to match the varying impact forces exerted on the turbine by different flow rates of cold medium. When the turbine rotates, it drives the connecting seat to rotate via a rotating rod. The rotation of the connecting seat, in turn, drives the counterweight to rotate along the inner groove of the first insertion rod via the second telescopic rod. The different centrifugal forces generated by the turbine speed also automatically adapt to the impact force exerted on the outer side of the counterweight during rotation. This allows the opening and closing cavity between the first and second insertion rods to adaptively change according to different flow rates, thereby automatically controlling the number of openings and closings of the exchange tubes. This ensures that the cold medium always maintains its optimal operating temperature under varying flow rates. The flow pattern, via the exchange pipes, avoids the blockage caused by insufficient pressure in some exchange pipes leading to prolonged accumulation of cold medium when the flow rate is low but the number of exchange pipes is large. When the counterweight is rotating, the friction strips on the inner side of the first connector rod cause the counterweight to intermittently contact the friction strips, thereby intermittently increasing the friction between the counterweight and the first connector rod. This intermittently limits the rotational speed of the counterweight, thus controlling the turbine's rotational speed. This makes the operation between the first and second connector rods and the counterweight more stable, preventing the counterweight and turbine from exceeding their load limits and causing loss of control. Attached Figure Description
[0024] Figure 1 This is a schematic diagram of the overall structure of the present invention;
[0025] Figure 2 This is a schematic diagram of the internal structure of the heat exchange tube of the present invention;
[0026] Figure 3 This is a schematic diagram of the structure of the fixing disk of the present invention;
[0027] Figure 4 This is a schematic diagram of the connecting rod of the present invention;
[0028] Figure 5 This is a schematic diagram of the internal structure of the bottom cover of the present invention;
[0029] Figure 6 This is a schematic diagram of the structure of the separator membrane of the present invention;
[0030] Figure 7 This is a schematic diagram of the turbine structure of the present invention;
[0031] Figure 8 This is a schematic diagram of the friction strip of the present invention.
[0032] In the diagram: 1. Heat exchanger tube; 2. Top cover; 3. Bottom cover; 4. Conversion mechanism; 41. Inlet heat pipe; 42. Outlet heat pipe; 43. Inlet cold pipe; 44. Outlet cold pipe; 45. Fixed plate; 46. Connecting rod; 47. Exchange tube; 48. Stabilizing plate No. 1; 49. Stabilizing plate No. 2; 410. Rubber ring; 5. Adaptive mechanism; 51. Turbine; 52. Rotating rod; 53. Isolation ring; 54. Insertion rod No. 1; 55. Insertion groove; 56. Insertion rod No. 2; 57. Telescopic rod No. 1; 58. Slide groove; 59. Counterweight; 510. Telescopic rod No. 2; 511. Connecting seat; 512. Friction strip; 513. Isolation membrane. Detailed Implementation
[0033] 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.
[0034] First embodiment: as follows Figures 1 to 8 As shown, the present invention provides a technical solution: a vertical anti-clogging shell-and-tube heat exchanger, including a heat exchange tube 1, a top cover 2 fixedly fastened to the top outer surface of the heat exchange tube 1, and a bottom cover 3 fixedly connected to the bottom of the heat exchange tube 1. The diameter of the heat exchange tube 1 is smaller than that of the top cover 2 and the bottom cover 3. The invention also includes:
[0035] The conversion mechanism 4 is fixedly installed inside the heat exchange tube 1;
[0036] Adaptive mechanism 5 is fixedly installed inside the base cover 3. Adaptive mechanism 5 is located directly below conversion mechanism 4, and the top of adaptive mechanism 5 is in contact with and attached to the bottom of conversion mechanism 4.
[0037] The conversion mechanism 4 includes a heat inlet pipe 41, which is fixedly connected to the top outer surface of the heat exchange tube 1. A heat outlet pipe 42 is fixedly connected to the bottom outer surface of the heat exchange tube 1. A cold inlet pipe 43 is fixedly connected to the outer surface of the bottom cover 3. A cold outlet pipe 44 is fixedly connected to the outer surface of the top cover 2. Fixed plates 45 are fixedly installed on the inner surfaces of both ends of the heat exchange tube 1. A connecting rod 46 is fixedly connected to the surface of the two fixed plates 45 that are close to each other. An exchange pipe 47 is fixedly connected to the outer surface of the fixed plate 45. Two sets of exchange pipes 47 are provided, and the two sets of exchange pipes 47 are symmetrically arranged. The two ends of the exchange pipes 47 are connected to the bottom cover 3 and the top cover 2, respectively.
[0038] The heat inlet pipe 41 and the heat outlet pipe 42 are located inside the fixed plate 45. A first stabilizing plate 48 is fixedly installed on the inner surface of the heat exchange tube 1. The first stabilizing plate 48 is fixedly sleeved on the outer surface of one set of exchange tubes 47. Four first stabilizing plates 48 are fixedly installed at fixed intervals along the inner surface of the heat exchange tube 1.
[0039] A second stabilizing plate 49 is fixedly installed on the inner surface of the heat exchange tube 1 away from the first stabilizing plate 48. The second stabilizing plate 49 is fixedly sleeved on the outer surface of another set of heat exchange tubes 47. Five second stabilizing plates 49 are fixedly spaced along the inner surface of the heat exchange tube 1. The first stabilizing plate 48 and the second stabilizing plate 49 are fixedly connected to the fixed plate 45 through the connecting rod 46.
[0040] The first stabilizing plate 48 and the second stabilizing plate 49 are set as semi-circles, and the first stabilizing plate 48 and the second stabilizing plate 49 are staggered. A rubber ring 410 is fixedly connected to the outer surface of the fixed plate 45. The outer side of the rubber ring 410 is fixedly connected to the inner surface of the heat exchange tube 1. The outer surfaces of the first stabilizing plate 48 and the second stabilizing plate 49 are also fixedly connected to the rubber ring 410.
[0041] Second embodiment: as follows Figures 1 to 8 As shown, the adaptive mechanism 5 includes a turbine 51, a rotating rod 52 is fixedly connected to the middle of the turbine 51, and the bottom of the turbine 51 is rotatably connected to the bottom inner surface of the bottom cover 3 through the rotating rod 52. The turbine 51 and the bottom cover 3 are set to the same central axis, and the outer side of the turbine 51 is set to face the cooling pipe 43.
[0042] An isolation ring 53 is fixedly connected to the upper surface edge of the turbine 51. The isolation ring 53 is located above the cooling pipe 43. The side surface of the isolation ring 53 is rotatably connected to the middle inner surface of the bottom cover 3. The inner diameter of the isolation ring 53 is smaller than the diameter of the turbine 51.
[0043] A first plug rod 54 is provided above the turbine 51. The first plug rod 54 is arc-shaped, and plug grooves 55 are provided on both sides of the first plug rod 54. A second plug rod 56 is slidably inserted into the plug grooves 55. The first plug rod 54 and the second plug rod 56 are combined to form a ring.
[0044] A telescopic rod 57 is fixedly connected to the outer surface of the second connector rod 56. The first telescopic rod 57 is elastic, and the end of the first telescopic rod 57 away from the second connector rod 56 is fixedly connected to the inner surface of the bottom cover 3.
[0045] A groove 58 is provided on the inner surface of the first plug rod 54. A counterweight 59 is slidably connected in the groove 58. A second telescopic rod 510 is fixedly connected to the inner surface of the counterweight 59. A connecting seat 511 is fixedly connected to the end of the second telescopic rod 510 away from the counterweight 59. The bottom surface of the connecting seat 511 is fixedly connected to the top of the rotating rod 52. Three counterweights 59 are fixedly spaced along the central axis of the connecting seat 511. A friction strip 512 is fixedly embedded in the inner side of the first plug rod 54. An isolation membrane 513 is fixedly connected to the bottom surface of the first plug rod 54. The isolation membrane 513 is annular. The outer end of the isolation membrane 513 is fixedly connected to the inner surface of the bottom cover 3.
[0046] During operation, when this heat exchanger is needed, the cold medium can be introduced through the cold inlet pipe 43, and the hot medium can be introduced simultaneously through the hot inlet pipe 41. After entering the bottom cover 3, the cold medium will be distributed and transported through the exchange pipe 47 into the top cover 2, and finally discharged through the cold outlet pipe 44. The hot medium enters the heat exchange pipe 1 and is transported from the top to the bottom of the heat exchange pipe 1, during which it contacts the outer surface of the exchange pipe 47 to complete the heat exchange operation, and finally discharged through the bottom heat outlet pipe 42. The exchange pipe 47 is isolated and inserted on the first stabilizing plate 48 and the second stabilizing plate 49, so that the exchange pipe 47 is in a relatively dispersed state during operation, avoiding the risk of leakage caused by friction between the exchange pipes 47 due to equipment vibration. After entering the heat exchange tube 1, the staggered arrangement between the first stabilizing plate 48 and the second stabilizing plate 49 causes the heat medium to be transported to the bottom in an S-shape within the heat exchange tube 1, significantly increasing the residence time of the heat medium in the heat exchange tube 1 and thus greatly improving the heat exchange effect. During the heat exchange process of the cold medium through the exchange tube 47, since the first stabilizing plate 48 and the second stabilizing plate 49 are connected to the fixed plate 45 as a whole by the connecting rod 46, and the rubber ring 410 allows the first stabilizing plate 48, the second stabilizing plate 49 and the fixed plate 45 to have a certain range of motion, the vibration generated by the equipment body during operation is greatly reduced when it reaches the first stabilizing plate 48, the second stabilizing plate 49 and the fixed plate 45, thereby significantly reducing the vibration between the exchange tube 47 and the equipment. The possibility of resonance between the components is reduced, thus protecting the exchange tube 47 and preventing it from frequently resonating with the equipment during operation, which could lead to rupture and leakage. This also significantly improves the service life and operational stability of the heat exchanger. When the cold medium enters the bottom cover 3, it continuously flows onto the turbine 51 through the cooling inlet pipe 43. The cooling inlet pipe 43 automatically drives the turbine 51 to rotate, keeping the cold medium in the bottom cover 3 in constant motion. This prevents pressure dead zones and impurity buildup that could eventually clog the heat exchanger, further extending its service life. Furthermore, the isolation ring 53 ensures that the cold medium is constantly in motion upon entering the bottom cover 3. The internal flow can only be transported through the gaps between the blades of turbine 51, thereby increasing the impact force of the cold medium on turbine 51. This ensures that turbine 51 can still be driven to work under low flow heat exchange conditions, greatly improving the applicability of this heat exchanger. As the impact force of the cold medium on turbine 51 varies with different flow rates, the rotation speed of turbine 51 will automatically match. When turbine 51 rotates, it will drive connecting seat 511 to rotate via rotating rod 52. When connecting seat 511 starts to rotate, it will drive counterweight 59 to start rotating along the sliding groove 58 on the inner side of first insertion rod 54 via second telescopic rod 510. Moreover, the centrifugal force generated by turbine 51 varies with different rotation speeds, so the counterweight 59 will automatically adapt to the impact force on the outer side when rotating.This allows the opening and closing cavity between connector 54 and connector 56 to adaptively change according to different flow rates, thereby automatically controlling the number of openings and closings of the exchange pipes 47. This ensures that the cold medium always flows through the exchange pipes 47 under different flow rates, preventing insufficient pressure in some exchange pipes 47 when the flow rate is low but the number of exchange pipes 47 is large, which could lead to blockages caused by prolonged accumulation of cold medium. When the counterweight 59 is rotating, the friction strip 512 on the inner side of connector 54 intermittently contacts the counterweight 59, thus intermittently increasing the friction between the counterweight 59 and connector 54. This intermittently limits the rotational speed of the counterweight 59, i.e., controls the rotational speed of the turbine 51. This makes the operation between connectors 54 and connector 56 and the counterweight 59 more stable, preventing the counterweight 59 and turbine 51 from exceeding their load and causing loss of control.
[0047] 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. Without further limitations, an element defined by the phrase "comprising one..." does not exclude the presence of other identical elements in the process, method, article, or apparatus that includes said element.
[0048] 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 vertical anti-clogging shell-and-tube heat exchanger, comprising heat exchange tubes (1), characterized in that: A top cover (2) is fixedly fastened to the top outer surface of the heat exchange tube (1), and a bottom cover (3) is fixedly connected to the bottom of the heat exchange tube (1). The diameter of the heat exchange tube (1) is smaller than that of the top cover (2) and the bottom cover (3). The tube also includes: The conversion mechanism (4) is fixedly installed inside the heat exchange tube (1); An adaptive mechanism (5) is fixedly installed inside the bottom cover (3). The adaptive mechanism (5) is located directly below the conversion mechanism (4), and the top of the adaptive mechanism (5) is in contact with the bottom of the conversion mechanism (4). The conversion mechanism (4) includes a heat inlet pipe (41), which is fixedly connected to the top outer surface of the heat exchange tube (1). A heat outlet pipe (42) is fixedly connected to the bottom outer surface of the heat exchange tube (1). A cold inlet pipe (43) is fixedly connected to the outer surface of the bottom cover (3). A cold outlet pipe (44) is fixedly connected to the outer surface of the top cover (2). Fixed plates (45) are fixedly installed on the inner surfaces of both ends of the heat exchange tube (1). A connecting rod (46) is fixedly connected to the surface of the two fixed plates (45) that are close to each other. An exchange tube (47) is fixedly connected to the outer surface of the fixed plate (45). There are two sets of exchange tubes (47), and the two sets of exchange tubes (47) are symmetrically arranged. The two ends of the exchange tube (47) are respectively connected to the bottom cover (3) and the top cover (2). The adaptive mechanism (5) includes a turbine (51), a rotating rod (52) is fixedly connected to the middle of the turbine (51), and the bottom of the turbine (51) is rotatably connected to the bottom inner surface of the bottom cover (3) through the rotating rod (52). The turbine (51) and the bottom cover (3) are set to the same central axis, and the outer side of the turbine (51) is set to face the cooling pipe (43). An isolation ring (53) is fixedly connected to the upper surface edge of the turbine (51). The isolation ring (53) is located above the cooling pipe (43). The side surface of the isolation ring (53) is rotatably connected to the inner surface of the middle part of the bottom cover (3). The inner diameter of the isolation ring (53) is smaller than the diameter of the turbine (51). A first plug rod (54) is provided above the turbine (51). The first plug rod (54) is arc-shaped. Plug grooves (55) are provided on both sides of the first plug rod (54). A second plug rod (56) is slidably inserted into the plug grooves (55). The first plug rod (54) and the second plug rod (56) are combined to form a ring. The outer surface of the second plug rod (56) is fixedly connected to the first telescopic rod (57), the first telescopic rod (57) is elastic, and the end of the first telescopic rod (57) away from the second plug rod (56) is fixedly connected to the inner surface of the bottom cover (3). The inner surface of the first plug rod (54) is provided with a sliding groove (58), and a counterweight (59) is slidably connected in the sliding groove (58). The inner surface of the counterweight (59) is fixedly connected with a second telescopic rod (510). The end of the second telescopic rod (510) away from the counterweight (59) is fixedly connected with a connecting seat (511). The bottom surface of the connecting seat (511) is fixedly connected to the top of the rotating rod (52). Three counterweights (59) are fixedly spaced along the central axis of the connecting seat (511). The inner side of the first plug rod (54) is fixedly inlaid with a friction strip (512). The bottom surface of the first plug rod (54) is fixedly connected with an isolation membrane (513). The isolation membrane (513) is set as an annular shape. The outer end of the isolation membrane (513) is fixedly connected to the inner surface of the bottom cover (3).
2. A vertical anti-clogging shell-and-tube heat exchanger according to claim 1, characterized in that: The heat inlet pipe (41) and heat outlet pipe (42) are arranged inside the fixed plate (45). A first stabilizing plate (48) is fixedly arranged on the inner surface of the heat exchange pipe (1). The first stabilizing plate (48) is fixedly sleeved on the outer surface of one of the heat exchange pipes (47). Four first stabilizing plates (48) are arranged at fixed intervals along the inner surface of the heat exchange pipe (1).
3. A vertical anti-clogging shell-and-tube heat exchanger according to claim 2, characterized in that: A second stabilizing plate (49) is fixedly installed on the inner surface of the heat exchange tube (1) away from the first stabilizing plate (48). The second stabilizing plate (49) is fixedly sleeved on the outer surface of another set of heat exchange tubes (47). Five second stabilizing plates (49) are fixedly spaced along the inner surface of the heat exchange tube (1). The first stabilizing plate (48) and the second stabilizing plate (49) are fixedly connected to the fixed plate (45) through a connecting rod (46).
4. A vertical anti-clogging shell-and-tube heat exchanger according to claim 3, characterized in that: The first stabilizing plate (48) and the second stabilizing plate (49) are set as semi-circles, and the first stabilizing plate (48) and the second stabilizing plate (49) are staggered. A rubber ring (410) is fixedly connected to the outer surface of the fixed disk (45). The outer side of the rubber ring (410) is fixedly connected to the inner surface of the heat exchange tube (1). The outer surfaces of the first stabilizing plate (48) and the second stabilizing plate (49) are also fixedly connected to the rubber ring (410).
Citation Information
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Industrial heat exchanger
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