CN101915514A - A semi-open rotor - Google Patents
A semi-open rotor Download PDFInfo
- Publication number
- CN101915514A CN101915514A CN 201010246358 CN201010246358A CN101915514A CN 101915514 A CN101915514 A CN 101915514A CN 201010246358 CN201010246358 CN 201010246358 CN 201010246358 A CN201010246358 A CN 201010246358A CN 101915514 A CN101915514 A CN 101915514A
- Authority
- CN
- China
- Prior art keywords
- rotor
- semi
- hollow shaft
- open
- primary blades
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 230000004323 axial length Effects 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims description 4
- 229910010293 ceramic material Inorganic materials 0.000 claims description 2
- 239000002131 composite material Substances 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- 239000012530 fluid Substances 0.000 abstract description 55
- 230000000694 effects Effects 0.000 abstract description 15
- 238000010586 diagram Methods 0.000 description 9
- 238000000034 method Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 230000002708 enhancing effect Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 238000005452 bending Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本发明提供了一种半敞开式转子,包括空心轴、主叶片和辅叶片,主叶片和辅叶片设置在空心轴外表面上,主叶片轴向长度较长,转子后端的主叶片是悬空的,形成半敞开式结构,与使用中相邻转子的前端轴向上相重叠、径向上具有间隙或配合,空心轴上主叶片前部分径向宽度小于后部分的径向宽度,主叶片前部分旋转直径小,主叶片后端部分旋转外径较大,辅叶片设置在转子前端,轴向长度较短。本发明的转子的主叶片前部分旋转直径小,起到扰流换热管中心流体的作用,将中心流体分散到四周,主叶片后部分旋转外径较大,对换热管内层流边界层流体的扰流效果较好,并且可以调整辅叶片的轴向长度来调整流体对转子的驱动力矩,这样加强了转子适应流体的性能。
The invention provides a semi-open rotor, which includes a hollow shaft, main blades and auxiliary blades, the main blades and auxiliary blades are arranged on the outer surface of the hollow shaft, the axial length of the main blades is relatively long, and the main blades at the rear end of the rotor are suspended , forming a semi-open structure, overlapping with the front end of the adjacent rotor in use axially, and having a gap or fit in the radial direction, the radial width of the front part of the main blade on the hollow shaft is smaller than the radial width of the rear part, and the front part of the main blade The rotating diameter is small, the rotating outer diameter of the rear end of the main blade is larger, and the auxiliary blade is arranged at the front end of the rotor, and the axial length is relatively short. The rotating diameter of the front part of the main blade of the rotor of the present invention is small, which plays the role of disturbing the central fluid of the heat exchange tube, and disperses the central fluid to the surroundings. The fluid turbulence effect is better, and the axial length of the auxiliary vane can be adjusted to adjust the driving torque of the fluid to the rotor, which enhances the performance of the rotor adapting to the fluid.
Description
技术领域technical field
本发明涉及的是一种应用于管壳式换热器、热交换反应器等设备中换热管内强化传热和防垢除垢的内插元件。The invention relates to an interpolation element for enhancing heat transfer, anti-scaling and descaling in heat exchange tubes of equipment such as shell-and-tube heat exchangers and heat exchange reactors.
背景技术Background technique
当前,节能减排是一项全世界都非常重视的关键技术,在石油、化工、火电、核电、冶金、轻工、航空器件和船舶车辆等众多领域都要应用到许多的换热器,其中应用最为广泛的是管壳式换热器,但在这些换热管中内壁普遍存在层积污垢,导致流体在管道中输送阻力增加,严重时会堵塞管道,同时传热性能大为下降;换热管内污垢会严重降低传热效率而引起重大能源浪费,与此同时污垢一般具有腐蚀性,管壁会因此腐蚀,如果泄露流体会造成重大的安全隐患,因此在传统上的处理办法就是被迫采取停产清洗,这样不仅耽搁了工厂的生产进度,同时还需要支付昂贵的清洗费用;为了更好地解决这些问题,人们一直研究采用不停产的在线自动强化传热和除垢防垢的各种办法和装置。近年来出现了许多防垢除垢方法和装置,其中之一利用流体推动螺旋纽带旋转能实现在线自动除垢的方法,螺旋纽带中国专利申请号为:ZL95236063.2,名称为“传热管内除垢防垢的清洗装置”的发明创造,该发明创造的技术方案由换热管内装有与换热管大体相等长度的纽带构成,纽带的径向尺寸小于换热管的内径,在换热管进液口处设置有轴向固定架,其中间部位有进液孔,轴向固定架的头部有一个轴孔,其内装有销轴,销轴尾部并与纽带相连接;发明名称为“双扰流螺旋式强化换热及自动除垢装置”,中国专利申请公开号为CN1424554,该装置用作强化传热及其自动除垢,包括有螺旋纽带、固定架,螺旋纽带设置在螺旋管内,利用通过换热管内流体流动带动螺旋纽带转动。由于螺旋纽带为一条整带,换热管在经过加工安装后不够顺直,螺旋纽带与换热管内壁之间会产生不均匀的缝隙,这样纽带的除垢作用小而不均匀,除垢效果不理想。螺旋纽带法除垢装置中,螺旋纽带均是单端固定的,另一端自由摆动,纽带的径向尺寸小于传热管的内径。综合一下螺旋纽带有以下主要缺点:(1)纽带为一整体,对传热管直接刮擦,损伤换热管内壁;(2)流体流动时推动纽带转动需要较大的驱动力矩,消耗更多的流体动能;(3)单端固定用的轴承的使用寿命短;(4)纽带产生的场协同强化传热效果不显著。之后中国专利号为ZL200520127121.9,公开了发明名称为“转子式自清洁强化传热装置”的专利申请,此装置是由固定架、转子、柔性轴和支撑管构成,两固定架分别固定在换热管的两端;转子的外表面有螺旋棱,转子上有中心孔;支撑架设在转子与固定架之间,柔性轴穿过转子的中心孔和支撑管固定在两固定架上。该装置具有在线自动防垢除垢和强化传热的功能,流体在传热管内顺流或者逆流的情况下,均有防垢除垢和强化传热的作用。但是缺点是在一定流体通过时,转子的旋转速度是由螺棱的螺旋升角所决定的,在螺棱导程小时转子的旋转速度快,同时对流体的阻力随之增加;为解决此问题,中国专利申请号200620172805.5,发明名称为“传热管内自清洁强化传热的低流阻转子”,该装置是由转子、支撑架和连接轴线构成,支撑架固定在传热管两端,连接轴线的两端分别固定在支撑架上,多个转子穿装在连接轴线上,转子是由空心轴和叶片构成,每个叶片与空心轴成同样的倾斜状,相邻叶片首尾相接,该结构对流体阻力减小,流体通过性能好,但其转动速度较高,转子轴向力叠加对挂件及轴线的作用力较大,转轴寿命会降低,以上所述的转子叶片对换热管内中心流体的扰流程度不够高,换热管内中心流体和换热管边界层的流体温度相差较大,没有实现换热管内所有流体都能与壳层介质有很好的换热效果,同时叶片的径向宽度在轴向方向上没有变化,换热管内中心层流体和层流层流体的混合度不够好,限制了转子的强化传热和防垢除垢能力的效果。At present, energy saving and emission reduction is a key technology that the whole world attaches great importance to. It is applied to many heat exchangers in many fields such as petroleum, chemical industry, thermal power, nuclear power, metallurgy, light industry, aviation devices and ship vehicles. Among them The most widely used is the shell-and-tube heat exchanger, but the inner wall of these heat exchange tubes generally has layered dirt, which leads to an increase in the resistance of the fluid in the pipeline, and in severe cases, the pipeline will be blocked, and the heat transfer performance will be greatly reduced; The dirt in the heat pipe will seriously reduce the heat transfer efficiency and cause a major waste of energy. At the same time, the dirt is generally corrosive, and the pipe wall will be corroded. If the fluid leaks, it will cause a major safety hazard. Therefore, the traditional treatment method is forced Taking stop-production cleaning will not only delay the production progress of the factory, but also need to pay expensive cleaning fees; in order to better solve these problems, people have been studying the use of non-stop on-line automatic heat transfer and descaling and anti-scaling. methods and devices. In recent years, many anti-scaling and descaling methods and devices have appeared, one of which uses fluid to drive the rotation of the spiral bond to realize the online automatic descaling method. The Chinese patent application number of the spiral bond is: ZL95236063. Scale and anti-scaling cleaning device "invention and creation, the technical solution of this invention is composed of a bond that is roughly equal to the length of the heat exchange tube in the heat exchange tube. The radial dimension of the bond is smaller than the inner diameter of the heat exchange tube. There is an axial fixing frame at the liquid inlet, and there is a liquid inlet hole in the middle part. There is a shaft hole at the head of the axial fixing frame, and a pin shaft is installed in it, and the tail of the pin shaft is connected with a tie; the invention name is " Double-disturbance spiral type enhanced heat exchange and automatic descaling device", the Chinese patent application publication number is CN1424554, the device is used to enhance heat transfer and automatic descaling, including a spiral tie, a fixing frame, and the spiral tie is set in the spiral tube , using the fluid flow through the heat exchange tube to drive the spiral bond to rotate. Since the spiral bond is a whole belt, the heat exchange tube is not straight enough after processing and installation, and there will be uneven gaps between the spiral bond and the inner wall of the heat exchange tube, so the descaling effect of the bond is small and uneven, and the descaling effect not ideal. In the spiral bond method descaling device, the spiral bond is fixed at one end, and the other end is free to swing, and the radial dimension of the bond is smaller than the inner diameter of the heat transfer tube. To sum up, the spiral bond has the following main disadvantages: (1) The bond is a whole, which directly scratches the heat transfer tube and damages the inner wall of the heat transfer tube; (2) When the fluid flows to push the bond to rotate, it requires a large driving torque and consumes more (3) The service life of the bearing used for single-end fixing is short; (4) The field synergy enhanced heat transfer effect generated by the bond is not significant. Afterwards, the Chinese patent number is ZL200520127121.9, which discloses a patent application titled "rotor type self-cleaning enhanced heat transfer device". This device is composed of a fixed frame, a rotor, a flexible shaft and a support tube. The two ends of the heat exchange tube; the outer surface of the rotor has helical ribs, and the rotor has a central hole; the supporting frame is arranged between the rotor and the fixed frame, and the flexible shaft passes through the central hole of the rotor and the supporting tube and is fixed on the two fixed frames. The device has the functions of online automatic scale prevention and descaling and enhanced heat transfer. When the fluid flows in the heat transfer tube along or against the flow, it has the functions of anti-scaling and descaling and enhanced heat transfer. But the disadvantage is that when a certain fluid passes through, the rotation speed of the rotor is determined by the helix angle of the flight. When the flight lead is small, the rotation speed of the rotor is fast, and the resistance to the fluid increases accordingly; in order to solve this problem , Chinese patent application number 200620172805.5, the title of the invention is "low flow resistance rotor with self-cleaning and enhanced heat transfer in the heat transfer tube", the device is composed of a rotor, a support frame and a connecting axis. The two ends of the axis are respectively fixed on the support frame, and multiple rotors are mounted on the connecting axis. The rotor is composed of a hollow shaft and blades. Each blade is inclined in the same shape as the hollow shaft. Adjacent blades are connected end to end. The fluid resistance of the structure is reduced, and the fluid passing performance is good, but its rotation speed is high, and the superposition of the axial force of the rotor exerts a large force on the pendant and the shaft, and the life of the shaft will be reduced. The degree of turbulence of the fluid is not high enough, the temperature difference between the central fluid in the heat exchange tube and the fluid in the boundary layer of the heat exchange tube is large, and it has not been realized that all the fluid in the heat exchange tube can have a good heat exchange effect with the shell medium. The radial width does not change in the axial direction, and the mixing degree of the central layer fluid and the laminar layer fluid in the heat exchange tube is not good enough, which limits the effect of enhancing heat transfer and anti-scaling and descaling capabilities of the rotor.
发明内容Contents of the invention
本发明的目的是设计一种新结构的转子,采用了不同长度的主叶片和辅叶片组合设置在空心轴上,保证换热管内中心流体流向换热管内壁,大力提高转子的强化传热和防垢除垢性能。The purpose of this invention is to design a rotor with a new structure, which adopts the combination of main blades and auxiliary blades of different lengths arranged on the hollow shaft, so as to ensure that the central fluid in the heat exchange tube flows to the inner wall of the heat exchange tube, and greatly improve the enhanced heat transfer and performance of the rotor. Anti-scaling and descaling properties.
本发明技术方案的具体内容是:一种半敞开式转子,它包括空心轴、主叶片和辅叶片,空心轴内径大于转轴的外径,主叶片和辅叶片设置在空心轴外表面上,主叶片轴向长度较长,转子后端的主叶片是悬空的,形成半敞开式结构,与使用中相邻转子的前端轴向上相重叠、径向上具有间隙或配合,空心轴上主叶片前部分径向宽度小于后部分的径向宽度,主叶片前部分旋转直径小,起到扰流换热管中心流体的作用,将中心流体分散到四周,主叶片后端部分旋转外径较大,与换热管内壁距离较小,更好地破坏层流层流体,加强防垢除垢和强化传热的效果,辅叶片设置在转子前端,轴向长度较短,主要作用是扰流换热管内中心流体的作用,使得中心流体向四周分散,加大流体的湍流程度,换热管内壁流体与换热管内中心流体的温差较小,从而提高了换热管内流体的换热强度。The specific content of the technical solution of the present invention is: a semi-open rotor, which includes a hollow shaft, main blades and auxiliary blades, the inner diameter of the hollow shaft is larger than the outer diameter of the rotating shaft, the main blades and auxiliary blades are arranged on the outer surface of the hollow shaft, The axial length of the blade is long, and the main blade at the rear end of the rotor is suspended, forming a semi-open structure, which overlaps with the front end of the adjacent rotor in use axially, and has a gap or fit in the radial direction, and the front part of the main blade on the hollow shaft The radial width is smaller than the radial width of the rear part, and the rotating diameter of the front part of the main blade is small, which plays the role of disturbing the central fluid of the heat exchange tube and dispersing the central fluid to the surroundings. The rotating outer diameter of the rear part of the main blade is larger, and The distance between the inner walls of the heat exchange tubes is smaller, which can better destroy the laminar fluid, strengthen the effect of anti-scaling and descaling, and enhance heat transfer. The auxiliary blades are arranged at the front end of the rotor with a short axial length. The role of the central fluid makes the central fluid disperse to the surroundings, increasing the degree of turbulence of the fluid, and the temperature difference between the inner wall fluid of the heat exchange tube and the central fluid in the heat exchange tube is small, thereby improving the heat exchange intensity of the fluid in the heat exchange tube.
本发明一种半敞开式转子的空心轴截面形状为空心圆锥形、空心圆柱形、空心波节形或空心多棱形,主叶片和辅叶片上可以设置透空结构,减小叶片对流体的流动阻力,节约能源,同时还可以节省材料。The cross-section shape of the hollow shaft of a semi-open rotor of the present invention is hollow conical, hollow cylindrical, hollow nodular or hollow polygonal, and the main blade and auxiliary blade can be provided with a through-hole structure to reduce the impact of the blade on the fluid. Flow resistance saves energy and at the same time saves material.
本发明一种半敞开式转子的空心轴两端设置有同轴结构,数个穿装在两个挂件之间转轴上的转子,其转子的空心轴两端设置有同轴结构,两个相邻的转子其中一个转子的空心轴尾部和另一个转子的空心轴的头部相结合。转子的空心轴同轴结构可以是球窝方式、圆锥方式、卡扣方式或者万向节方式。The two ends of the hollow shaft of a semi-open rotor in the present invention are provided with a coaxial structure, and several rotors are mounted on the rotating shaft between two pendants, and the two ends of the hollow shaft of the rotor are provided with a coaxial structure. The tail of the hollow shaft of one of the adjacent rotors is combined with the head of the hollow shaft of the other rotor. The hollow-shaft coaxial structure of the rotor can be in the form of a ball socket, a cone, a buckle or a universal joint.
本发明一种半敞开式转子的主叶片、辅叶片和空心轴是由高分子材料、高分子基复合材料、金属或者陶瓷材料制作的。The main vane, auxiliary vane and hollow shaft of a semi-open rotor of the present invention are made of polymer material, polymer-based composite material, metal or ceramic material.
本发明一种半敞开式转子的主叶片和辅叶片的横截面的形状是矩形、梯形、或者是圆弧形,主叶片和辅叶片可以为螺旋棱。The shape of the cross-section of the main blade and the auxiliary blade of the semi-open rotor of the present invention is rectangle, trapezoid, or circular arc, and the main blade and the auxiliary blade can be helical edges.
本发明涉及的换热管内轴向长度不同的叶片组合式转子,即一种半敞开式转子,主叶片和辅叶片的轴向长度、螺旋升角和旋转外圆直径等参数,可以根据换热管内径、管内的介质流速和温度等工作条件以及制造加工成本等来确定,相邻转子之间可以采取同步旋转或者是独立旋转结构。The blade combined rotor with different axial lengths in the heat exchange tubes involved in the present invention is a semi-open rotor. The internal diameter of the tube, the medium flow rate and temperature in the tube and other working conditions, as well as the manufacturing and processing costs, etc. are determined. The adjacent rotors can adopt synchronous rotation or independent rotation structure.
本发明的有益效果是:1、空心轴上主叶片前部分径向宽度小于后部分的径向宽度,主叶片前部分旋转直径小,起到扰流换热管中心流体的作用,将中心流体分散到四周,主叶片后部分旋转外径较大,对换热管内层流边界层流体的扰流效果较好,起到强化传热和防垢除垢的效果;2、辅叶片是设置在转子空心轴前半部分,与主叶片配合,提高转子扰流中心流体的作用,把换热管内中心流体分散向换热管的四周,加强中心流体的换热效果;3、辅叶片轴线长度较小,减小了转子对流体的阻力,同时节省转子的材料成本;4、可以调整辅叶片的轴向长度来调整流体对转子的驱动力矩,这样加强了转子适应流体的性能。The beneficial effects of the present invention are: 1, the radial width of the front part of the main blade on the hollow shaft is smaller than the radial width of the rear part, and the rotation diameter of the front part of the main blade is small, which plays the role of disturbing the central fluid of the heat exchange tube, and the central fluid Scattered around, the rear part of the main blade rotates with a larger outer diameter, which has a better turbulence effect on the laminar boundary layer fluid in the heat exchange tube, and has the effect of enhancing heat transfer and anti-scaling and descaling; 2. The auxiliary blade is set on The first half of the hollow shaft of the rotor cooperates with the main blades to improve the effect of the rotor spoiling the central fluid, disperse the central fluid in the heat exchange tube to the surroundings of the heat exchange tube, and enhance the heat exchange effect of the central fluid; 3. The axial length of the auxiliary blade is small , reduces the resistance of the rotor to the fluid, and saves the material cost of the rotor; 4. The axial length of the auxiliary blade can be adjusted to adjust the driving torque of the fluid to the rotor, which enhances the performance of the rotor to adapt to the fluid.
本发明一种半敞开式转子安装在换热管内,根据具体的换热管长度,用转轴将数个转子串联在一起,穿在换热管内,同时利用固定在换热管端部的挂件在换热管两端对转轴进行轴向固定,当流体流过主叶片和辅叶片时,对转子有垂直于径向的切向力,使转子绕转轴旋转,转子就会对换热管内壁上起到防垢除垢的效果;转子空心轴上设置有长度不同的主叶片和辅叶片,同时主叶片的径向宽度在轴向长上是发生变化的,小直径部分的叶片扰流换热管内中心流体,大直径部分的叶片扰流换热管内壁的层流边界层的流体,主叶片悬空部分与小直径叶片的转子头部相配合,这样加大了转子对流体的扰流程度,使得换热管中心流体与换热管内壁的流体温差变得很小,起到增强防垢除垢和强化传热的效果。同时还可以根据实际需要,在主叶片和辅叶片上透空结构,降低转子对流体流动的阻力,节省了转子的材料和价格成本。A semi-open rotor of the present invention is installed in the heat exchange tube. According to the specific length of the heat exchange tube, several rotors are connected in series with a rotating shaft and passed through the heat exchange tube. At the same time, the pendant fixed at the end of the heat exchange tube is The two ends of the heat exchange tube are axially fixed to the shaft. When the fluid flows through the main blade and the auxiliary blade, there is a tangential force perpendicular to the radial direction on the rotor, so that the rotor rotates around the shaft, and the rotor will be on the inner wall of the heat exchange tube. It has the effect of anti-scaling and descaling; the hollow shaft of the rotor is equipped with main blades and auxiliary blades with different lengths, and the radial width of the main blades changes in the axial length, and the small-diameter blades disturb the heat exchange The central fluid in the tube, the large-diameter blade spoils the flow of the laminar boundary layer fluid on the inner wall of the heat exchange tube, and the suspended part of the main blade cooperates with the rotor head of the small-diameter blade, which increases the degree of disturbance of the rotor to the fluid. The temperature difference between the fluid in the center of the heat exchange tube and the fluid on the inner wall of the heat exchange tube becomes very small, and the effect of enhancing scale prevention and descaling and enhancing heat transfer is achieved. At the same time, according to actual needs, a hollow structure can be provided on the main blade and the auxiliary blade to reduce the resistance of the rotor to fluid flow, and save the material and price cost of the rotor.
附图说明Description of drawings
图1是本发明一种半敞开式转子——四叶式转子结构示意图。Fig. 1 is a schematic diagram of the structure of a semi-open rotor of the present invention—a four-leaf rotor.
图2是图1的右视图。Fig. 2 is a right side view of Fig. 1 .
图3是本发明一种半敞开式转子——六叶式转子结构示意图(3个主叶片和3个辅叶片)。Fig. 3 is a schematic diagram of the structure of a semi-open rotor of the present invention—a six-bladed rotor (3 main blades and 3 auxiliary blades).
图4是本发明一种半敞开式转子——六叶式转子结构示意图(2个主叶片和4个辅叶片)。Fig. 4 is a schematic diagram of the structure of a semi-open rotor of the present invention—a six-blade rotor (2 main blades and 4 auxiliary blades).
图5是本发明一种半敞开式转子——六叶式转子结构示意图(4个主叶片和2个辅叶片)。Fig. 5 is a schematic diagram of the structure of a semi-open rotor of the present invention—a six-bladed rotor (4 main blades and 2 auxiliary blades).
图6是本发明一种半敞开式转子——四叶式转子透空结构示意图。Fig. 6 is a schematic diagram of a semi-open rotor of the present invention—a four-leaf rotor with a hollow structure.
图7是本发明一种半敞开式转子安装应用示意图。Fig. 7 is a schematic diagram of the installation and application of a semi-open rotor of the present invention.
图中:1-主叶片,2-辅叶片,3-空心轴,4-球窝凸台,5-球窝凹台,6-悬空部分,7-透空结构,8-换热管,9-挂件,10-转轴,11-液膜。In the figure: 1-main blade, 2-auxiliary blade, 3-hollow shaft, 4-ball-socket convex platform, 5-ball-socket concave platform, 6-suspension part, 7-permeable structure, 8-heat exchange tube, 9 -Pendant, 10-rotating shaft, 11-liquid film.
具体实施方式Detailed ways
如图7所示,本发明涉及一种半敞开式转子的一种实施例子,换热管8内安装有本发明一种半敞开式转子、挂件9和转轴10,数个所述转子穿装在两个挂件9间的转轴10上,挂件9固定在换热管8两端,转轴10的两端分别固定在挂件9上,所述转子是由长度不同的主叶片1和辅叶片2组合固定在空心轴3上面的,主叶片1的径向宽度在轴向上是变化的,并且转子后部分的主叶片1设置悬空部分6,可以与相邻所述转子前端相配合。As shown in Figure 7, the present invention relates to an implementation example of a semi-open rotor. A semi-open rotor of the present invention, a
图1至图6所示,本发明转子的空心轴3截面形状为空心圆柱形;图1和图2中,转子空心轴3上设置有两个主叶片1和两个辅叶片2;图3所示为转子空心轴3上设置有三个主叶片1和三个辅叶片2的六个叶片的结构示意图;图4所示,是两个主叶片1和四个辅叶片2的六叶式转子结构示意图;图5是四个主叶片1和两个辅叶片2六叶式转子结构示意图。转子的空心轴3两端设置有同轴结构,本实例中同轴结构是在每个空心轴3的头部和尾部分别设置有球窝凸台4和球窝凹台5,数个所述转子穿装在两个挂件9之间的转轴10上,其空心轴3两端设置有球窝凸台4和球窝凹台5,两个相邻转子其中一个转子的空心轴3头部的球窝凸台4和另一个的球窝凹台5相结合,结合面间形成的液膜11减少转子间的摩擦,从而降低转子转动时相互间的磨损,此外,同轴结构的另一目的是使相邻转子在工作时保持同轴,同时具有适应换热管8弯曲的柔性连接结构,同轴结构除了球窝结构外,还可以是圆锥方式、卡扣方式或者万向节方式,同轴度要求不高时可以直接采用平面结构。图6所示的转子的主叶片1上有透空结构7。As shown in Fig. 1 to Fig. 6, the cross section shape of the
换热管内流体流过本发明一种半敞开式转子前部分的小直径的叶片时,流体受转子叶片作用成旋向流,由换热管内中心流体分散向转子的四周,加大流体的湍流程度,促进中心流体与换热管8附近流体的交换与流动,转子后部分叶片的外径表面离换热管内壁的距离较小,能有效地扰动换热管内壁的层流边界层,提高防垢除垢和强化传热的效果,同时转子后部分悬空部分6能与相邻转的前子部分配合,进一步利用转子加大流体的湍流程度,提高转子强化传热的效果。When the fluid in the heat exchange tube flows through the small-diameter blades of the front part of the semi-open rotor of the present invention, the fluid is acted by the rotor blades to form a swirl flow, and the fluid in the center of the heat exchange tube is dispersed to the periphery of the rotor, increasing the turbulence of the fluid The distance between the center fluid and the fluid near the
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010102463584A CN101915514B (en) | 2010-08-06 | 2010-08-06 | Semi-open-type rotor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010102463584A CN101915514B (en) | 2010-08-06 | 2010-08-06 | Semi-open-type rotor |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101915514A true CN101915514A (en) | 2010-12-15 |
CN101915514B CN101915514B (en) | 2012-03-21 |
Family
ID=43323080
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010102463584A Expired - Fee Related CN101915514B (en) | 2010-08-06 | 2010-08-06 | Semi-open-type rotor |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101915514B (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102128560A (en) * | 2011-04-19 | 2011-07-20 | 北京化工大学 | Twisted belt type pendant in heat exchange pipe |
CN102161045A (en) * | 2011-01-13 | 2011-08-24 | 清华大学 | Self-supporting and self-rotating cleaning and scale-removing element in pipe |
CN103411468A (en) * | 2013-08-05 | 2013-11-27 | 北京化工大学 | Center spring and helical blade rotor in heat exchange tube |
CN103432981A (en) * | 2013-08-27 | 2013-12-11 | 北京化工大学 | Energy-saving high-efficiency self-cleaning polymerizing device |
CN105135932A (en) * | 2015-10-12 | 2015-12-09 | 郑州大学 | Low-flow-resistance rotor for reinforcing heat transfer and scale removal/prevention in heat exchange tube |
CN105371671A (en) * | 2015-11-10 | 2016-03-02 | 南京华夏壹泰节能科技有限公司 | Modular low flow resistance diversion type hanging part |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6222996A (en) * | 1985-07-22 | 1987-01-31 | Toshiba Corp | Multi-tubular heat exchanger |
US5485880A (en) * | 1992-10-29 | 1996-01-23 | Gerstenberg & Agger A/S | Blade system for a scraped surface heat exchanger |
US20030192673A1 (en) * | 2000-03-14 | 2003-10-16 | Schweinichen Jaxa Von | Rotatable roller |
CN201000303Y (en) * | 2006-12-29 | 2008-01-02 | 北京华夏英蓝科技发展有限公司 | Self-cleaning intensify heat transfer low flow resistance rotor in heat transfer pipe |
CN101551214A (en) * | 2008-04-03 | 2009-10-07 | 北京化工大学 | Rotating piece type automatic-cleaning and heat-transfer enhancing device |
CN201368695Y (en) * | 2009-02-20 | 2009-12-23 | 北京华夏英蓝科技发展有限公司 | Unit combined-type enhanced heat transfer device |
-
2010
- 2010-08-06 CN CN2010102463584A patent/CN101915514B/en not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6222996A (en) * | 1985-07-22 | 1987-01-31 | Toshiba Corp | Multi-tubular heat exchanger |
US5485880A (en) * | 1992-10-29 | 1996-01-23 | Gerstenberg & Agger A/S | Blade system for a scraped surface heat exchanger |
US20030192673A1 (en) * | 2000-03-14 | 2003-10-16 | Schweinichen Jaxa Von | Rotatable roller |
CN201000303Y (en) * | 2006-12-29 | 2008-01-02 | 北京华夏英蓝科技发展有限公司 | Self-cleaning intensify heat transfer low flow resistance rotor in heat transfer pipe |
CN101551214A (en) * | 2008-04-03 | 2009-10-07 | 北京化工大学 | Rotating piece type automatic-cleaning and heat-transfer enhancing device |
CN201368695Y (en) * | 2009-02-20 | 2009-12-23 | 北京华夏英蓝科技发展有限公司 | Unit combined-type enhanced heat transfer device |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102161045A (en) * | 2011-01-13 | 2011-08-24 | 清华大学 | Self-supporting and self-rotating cleaning and scale-removing element in pipe |
CN102161045B (en) * | 2011-01-13 | 2012-11-14 | 清华大学 | Self-supporting and self-rotating cleaning and scale-removing element in pipe |
CN102128560A (en) * | 2011-04-19 | 2011-07-20 | 北京化工大学 | Twisted belt type pendant in heat exchange pipe |
CN102128560B (en) * | 2011-04-19 | 2012-10-17 | 北京化工大学 | Twisted ribbon pendant inside the heat exchange tube |
CN103411468A (en) * | 2013-08-05 | 2013-11-27 | 北京化工大学 | Center spring and helical blade rotor in heat exchange tube |
CN103432981A (en) * | 2013-08-27 | 2013-12-11 | 北京化工大学 | Energy-saving high-efficiency self-cleaning polymerizing device |
CN103432981B (en) * | 2013-08-27 | 2015-05-27 | 北京化工大学 | Energy-saving high-efficiency self-cleaning polymerizing device |
CN105135932A (en) * | 2015-10-12 | 2015-12-09 | 郑州大学 | Low-flow-resistance rotor for reinforcing heat transfer and scale removal/prevention in heat exchange tube |
CN105371671A (en) * | 2015-11-10 | 2016-03-02 | 南京华夏壹泰节能科技有限公司 | Modular low flow resistance diversion type hanging part |
Also Published As
Publication number | Publication date |
---|---|
CN101915514B (en) | 2012-03-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103411467B (en) | Low driving rotor with turbulence core and in heat exchange tube | |
CN102116594B (en) | Radial asymmetric blade combined rotor in heat exchange tube | |
CN101915514A (en) | A semi-open rotor | |
CN102128559B (en) | Low driving force self-cleaning and heat transfer enhancement rotor in heat exchange tube | |
CN101210791A (en) | Self-cleaning reinforcement heat transfer low flow resistance rotor in heat-transfer pipe | |
CN105135932A (en) | Low-flow-resistance rotor for reinforcing heat transfer and scale removal/prevention in heat exchange tube | |
CN106403699B (en) | Magnetic bionic blade rotor in heat exchanger tube | |
CN104764355A (en) | Zigzag spiral blade rotor inside heat exchange tube | |
WO2012037745A1 (en) | Self-cleaning enhanced heat transfer device used for heat exchange pipe and manufacturing method thereof | |
CN103225980A (en) | Multi-axis low-rotating-speed spiral rotor in heat exchange tube | |
CN103217055B (en) | Opposite-rotation-direction combined rotor in heat exchange tube | |
CN102102960B (en) | Blades in the heat exchange tube rotate to cross combined rotor | |
CN102102961A (en) | Self rotation type rotor connection structure in heat exchange tube | |
CN103411464B (en) | Through hole spring and helical blade rotor in heat exchange tube | |
CN102425975B (en) | Internal grooving helical blade rotor for heat exchange tube | |
CN101893404A (en) | An arc-shaped static spoiler in the heat exchange tube | |
CN201628513U (en) | Self-rotating rotor connection structure in heat exchange tube | |
CN205027195U (en) | Low flow resistance rotor of enhanced heat transfer and scale control scale removal in heat exchange tube | |
CN103411468B (en) | Center spring and helical blade rotor in heat exchange tube | |
CN201000303Y (en) | Self-cleaning intensify heat transfer low flow resistance rotor in heat transfer pipe | |
CN102645120A (en) | Low drive spoiler rotor in heat exchange tube | |
CN101813437A (en) | Unit-combination type heat transfer enhancement device | |
CN102645122A (en) | Grooving spiral curling rotor in heat exchange tube | |
CN201583184U (en) | Combined rotor provided with blades crossed in rotary direction and arranged in heat exchange tube | |
CN103411465A (en) | Penetration type concave-convex blade rotor inside heat exchange pipe |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120321 |
|
CF01 | Termination of patent right due to non-payment of annual fee |