Spiral high-efficiency heat exchange tube
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- WUXI YUFENG ENERGY SAVING TECH CO LTD
- Filing Date
- 2025-08-13
- Publication Date
- 2026-08-07
AI Technical Summary
[0003]上述装置在进行使用时,设置凹凸壁面,提高传热面积和强化流体介质的紊流,螺旋部强化内部流体介质的紊流,提高传热系数和抑制污垢的沉积,但螺旋部设置的凹凸壁面会增加污垢堆积的速度,在污垢堆积较多时会严重影响换热管的换热效率
[0013]本实用新型实际使用时,通过在换热翅片和接触式换热片的对应设置状态下,能够增加换热管与外部换热介质接触的面积,从而增加换热管的换热效率,同时接触式换热片会与换热管内部的导热介质进行接触,从而能够有效的增加换热管导热的效率,进一步的增加换热管换热的效率和效果,同时在第二倾斜切槽和第一倾斜切槽的对应设置状态下,能够将换热管内外两侧的换热介质中的杂质向外部引导,从而避免过多的杂质在换热翅片和接触式换热片内部的缝隙中堆积。
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Figure CN224608264U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of heat recovery technology, and more specifically, to a spiral high-efficiency heat exchange tube. Background Technology
[0002] Heat exchange tubes are commonly found in shell-and-tube, tubular, and double-tube heat exchangers in petroleum, chemical, power, and refrigeration equipment, and their applications are widespread. Selecting good heat exchange tubes results in high heat transfer efficiency, inhibits fouling, and improves product reliability and economy. Publication number (CN206847454U) describes a spiral high-efficiency heat exchange tube, comprising lead tube sections at both ends and a heat exchange section located between the lead tube sections. The lead tube sections are smooth-walled circular tubes, and the heat exchange section is a hollow tube. The outer wall of the heat exchange section has a spiral portion that spirals and protrudes along the axis of the heat exchange section. Multiple spiral portions are arranged circumferentially along the heat exchange section, and these spiral portions are coiled together. The spiral portion and the heat exchange section share the same fluid chamber. The outer wall of the heat exchange section is a concave-convex wall surface. The outer wall includes outer wall protrusions arranged in a row and protruding from the outer wall, and an outer wall recess located between two outer wall protrusions. The inner wall of the heat exchange section is also a concave-convex wall surface. The inner wall includes elongated inner wall protrusions arranged in parallel and protruding from the inner wall, and an inner wall recess located between two inner wall protrusions.
[0003] When the above-mentioned device is in use, it is equipped with uneven walls to increase the heat transfer area and enhance the turbulence of the fluid medium. The spiral part enhances the turbulence of the internal fluid medium, increases the heat transfer coefficient and inhibits the deposition of fouling. However, the uneven walls of the spiral part will increase the rate of fouling accumulation. When there is a lot of fouling, it will seriously affect the heat exchange efficiency of the heat exchange tube. Utility Model Content
[0004] In order to overcome the above-mentioned defects of the prior art, the present invention provides a spiral high-efficiency heat exchange tube. The technical problem to be solved by the present invention is: how to increase the heat exchange efficiency of the heat exchange tube.
[0005] To achieve the above objectives, the present invention provides the following technical solution: a spiral high-efficiency heat exchange tube, comprising a heat exchange tube with heat exchange water guiding holes inside, and heat exchange fins provided on the outer end face of the middle part of the heat exchange tube, the heat exchange fins passing through the end face of the heat exchange tube and extending into the interior of the heat exchange tube.
[0006] The heat exchange fins have contact heat exchange plates inside the heat exchange tube. One end face of the contact heat exchange plate has a first inclined groove, and one end face of the heat exchange fins has a second inclined groove.
[0007] In a preferred embodiment, the heat exchange tube is a copper component, and the number of heat exchange fins is multiple, arranged in a ring array outside the center point of the heat exchange tube in the right-view direction.
[0008] In a preferred embodiment, the heat exchange fins are arranged in a spiral configuration on the outer end face of the heat exchange tube, and the heat exchange fins are made of copper.
[0009] In a preferred embodiment, the second inclined groove is provided in two quantities and is arranged in a mirror image on both sides of the vertical central axis in the main view direction of the heat exchange fin. The first inclined groove is provided in two quantities and is arranged in a mirror image on both sides of the vertical central axis in the main view direction of the contact heat exchange fin.
[0010] In a preferred embodiment, the number of contact heat exchange plates is multiple, and they are arranged in a ring array outside the center point of the heat exchange tube in the right-view direction. The contact heat exchange plates are arranged in a spiral state on the inner end face of the heat exchange tube.
[0011] In a preferred embodiment, the length of the contact heat exchanger in the main viewing direction is less than the length of the heat exchange fin in the main viewing direction, and the contact heat exchanger is arranged in a staggered state on the inner end faces of adjacent heat exchange fins.
[0012] The technical effects and advantages of this utility model are as follows:
[0013] In practical use, the corresponding arrangement of the heat exchange fins and contact heat exchange plates increases the contact area between the heat exchange tube and the external heat exchange medium, thereby increasing the heat exchange efficiency of the heat exchange tube. At the same time, the contact heat exchange plates come into contact with the heat-conducting medium inside the heat exchange tube, which effectively increases the heat conduction efficiency of the heat exchange tube, further increasing the heat exchange efficiency and effect of the heat exchange tube. In addition, the corresponding arrangement of the second inclined groove and the first inclined groove can guide impurities in the heat exchange medium on both sides of the heat exchange tube to the outside, thereby preventing excessive impurities from accumulating in the gaps inside the heat exchange fins and contact heat exchange plates. Attached Figure Description
[0014] Figure 1 This is a schematic diagram of the overall structure of this utility model.
[0015] Figure 2 This is a schematic diagram of the overall front view cross-sectional structure of this utility model.
[0016] Figure 3 This is a schematic diagram of the overall right-side structure of this utility model.
[0017] Figure 4 This is a partially enlarged structural diagram of the heat exchange fins of this utility model.
[0018] Figure 5 This utility model Figure 2 Enlarged structural diagram of section A in the middle.
[0019] The attached figures are labeled as follows: 1 heat exchange tube, 2 heat exchange fin, 3 second inclined groove, 4 contact heat exchange plate, 5 first inclined groove, and 6 heat exchange water guide hole. Detailed Implementation
[0020] This invention provides a spiral high-efficiency heat exchange tube, such as Figure 1 and 2 As shown, the device includes a heat exchange tube 1 with heat exchange water guide holes 6 inside. Heat exchange fins 2 are provided on the outer end face of the middle part of the heat exchange tube 1. The heat exchange fins 2 pass through the end face of the heat exchange tube 1 and extend into the interior of the heat exchange tube 1. A second inclined groove 3 is provided on one end face of the heat exchange fins 2. The heat exchange tube 1 is made of copper. Multiple heat exchange fins 2 are arranged in a ring array outside the center point in the right-view direction of the heat exchange tube 1. The heat exchange fins 2 are arranged in a spiral configuration on the outer end face of the heat exchange tube 1. The heat exchange fins 2 are made of copper. Two second inclined grooves 3 are arranged in a mirror image configuration on both sides of the vertical central axis in the main view direction of the heat exchange fins 2.
[0021] like Figure 3 , 4 As shown in Figure 5, the heat exchange fins 2 are provided with contact heat exchange plates 4 inside the heat exchange tube 1. One end face of the contact heat exchange plate 4 is provided with a first inclined groove 5. There are two first inclined grooves 5, which are arranged in a mirror state on both sides of the vertical central axis of the contact heat exchange plate 4 in the main view direction. There are multiple contact heat exchange plates 4, which are arranged in a ring array outside the center point of the heat exchange tube 1 in the right view direction. The contact heat exchange plates 4 are arranged in a spiral state on the inner end face of the heat exchange tube 1. The length of the contact heat exchange plate 4 in the main view direction is less than the length of the heat exchange fins 2 in the main view direction. The contact heat exchange plates 4 are arranged in a staggered state on the inner end faces of adjacent heat exchange fins 2.
[0022] Working principle of this utility model:
[0023] When using this utility model, after the operator has installed it, external hot water is introduced into the heat exchange water guide hole 6 of the heat exchange tube 1. Then, the operator can immerse the outside of the heat exchange tube 1 in cold water. The contact heat exchange plate 4 and the heat exchange tube 1 can effectively absorb the heat in the hot water inside the heat exchange water guide hole 6, thereby effectively transferring it to the outer end face of the heat exchange tube 1 and the heat exchange fin 2. When the cold water flows through two adjacent heat exchange fins 2, it can effectively increase the efficiency and effect of heat recovery and exchange inside the heat exchange tube 1.
[0024] Finally, it should be noted that: the accompanying drawings of the embodiments disclosed in this utility model only involve the structures involved in the embodiments disclosed in this utility model. Other structures can refer to the general design. In the absence of conflict, the same embodiment and different embodiments of this utility model can be combined with each other.
[0025] The above description is only a preferred embodiment of the present utility model and is not intended to limit the present utility model. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present utility model should be included within the protection scope of the present utility model.
Claims
1. A spiral high-efficiency heat exchange tube, characterized in that, include: A heat exchange tube (1) has a heat exchange water guide hole (6) inside. The outer end face of the middle part of the heat exchange tube (1) is provided with heat exchange fins (2). The heat exchange fins (2) pass through the end face of the heat exchange tube (1) and extend into the interior of the heat exchange tube (1). The heat exchange fins (2) have contact heat exchange plates (4) inside the heat exchange tube (1). The contact heat exchange plates (4) have a first inclined groove (5) on one side end face and a second inclined groove (3) on one side end face.
2. The spiral high-efficiency heat exchange tube according to claim 1, characterized in that: The heat exchange tube (1) is a copper component, and the heat exchange fins (2) are arranged in a ring array outside the center point of the heat exchange tube (1) in the right-view direction.
3. The spiral high-efficiency heat exchange tube according to claim 1, characterized in that: The heat exchange fins (2) are arranged in a spiral state on the outer end face of the heat exchange tube (1), and the heat exchange fins (2) are made of copper.
4. The spiral high-efficiency heat exchange tube according to claim 1, characterized in that: The second inclined groove (3) is provided in two quantities and is set in a mirror state on both sides of the vertical central axis in the main view direction of the heat exchange fin (2). The first inclined groove (5) is provided in two quantities and is set in a mirror state on both sides of the vertical central axis in the main view direction of the contact heat exchange plate (4).
5. A spiral high-efficiency heat exchange tube according to claim 1, characterized in that: The number of contact heat exchange plates (4) is multiple, and they are arranged in a ring array outside the center point of the heat exchange tube (1) in the right view direction. The contact heat exchange plates (4) are arranged in a spiral state on the inner end face of the heat exchange tube (1).
6. The spiral high-efficiency heat exchange tube according to claim 1, characterized in that: The length of the contact heat exchange plate (4) in the main viewing direction is less than the length of the heat exchange fin (2) in the main viewing direction, and the contact heat exchange plate (4) is set in a staggered state on the inner end face of the adjacent heat exchange fin (2).
Citation Information
Patent Citations
Spiral high -efficiency heat exchange tube
CN206847454U