CN207204400U - A kind of cyclone separator with split blast pipe - Google Patents
A kind of cyclone separator with split blast pipe Download PDFInfo
- Publication number
- CN207204400U CN207204400U CN201720552166.3U CN201720552166U CN207204400U CN 207204400 U CN207204400 U CN 207204400U CN 201720552166 U CN201720552166 U CN 201720552166U CN 207204400 U CN207204400 U CN 207204400U
- Authority
- CN
- China
- Prior art keywords
- blast pipe
- cyclone separator
- exhaust pipe
- split
- disengagement chamber
- 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.)
- Expired - Fee Related
Links
- 239000000428 dust Substances 0.000 claims abstract description 8
- 238000010276 construction Methods 0.000 claims abstract 3
- 239000007787 solid Substances 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 2
- 238000000926 separation method Methods 0.000 abstract description 14
- 230000008901 benefit Effects 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract 1
- 230000003134 recirculating effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 210000001503 joint Anatomy 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Cyclones (AREA)
Abstract
Description
技术领域technical field
本发明涉及分选技术领域,属于旋风分离器技术领域,具体说是将气体中的固相或液相杂质采用离心分离的方式分离出去的装置。The invention relates to the technical field of separation and belongs to the technical field of cyclone separators, in particular to a device for separating solid or liquid impurities in gas by means of centrifugal separation.
背景技术Background technique
旋风分离器是一种非常重要的除尘设备,在很多行业中都有比较大的应用,比较常见的有化工行业、石油行业、火力发电厂以及环保行业等。与别的分离器相比,旋风分离器的结构比较简单,各个部件都是相对静止的,分离的效率比较高,并且其压降没有诸如袋式除尘器高,旋风除尘器还有一个很大的优点,就是适用于高温、高压、并且浓度较高的工艺气体。Cyclone separator is a very important dust removal equipment, which is widely used in many industries, such as chemical industry, petroleum industry, thermal power plant and environmental protection industry. Compared with other separators, the structure of the cyclone separator is relatively simple, each part is relatively static, the separation efficiency is relatively high, and its pressure drop is not as high as that of the bag filter, and the cyclone separator has a large The advantage is that it is suitable for process gases with high temperature, high pressure and high concentration.
传统的旋风分离器在工作时,从旋风分离器内净化后的气流进入排气管后仍保持较高的旋转速度,由于排气管内的旋转气流对于分离已毫无益处,气流的高速旋转只能带来能量的消耗,而且旋转速度越高,旋转动能越大,能量消耗也越大。此外,排气管内气流的轴向速度从边壁向中心逐渐降低,而且速度梯度很大,呈强剪切流的特征,在中心附近轴向速度甚至出现负值,产生了回流区。排气管中心附近回流区的存在必然导致排气管内流动阻力增加,从而造成相应的能量损失。When the traditional cyclone separator is working, the purified airflow from the cyclone separator still maintains a high rotation speed after entering the exhaust pipe. Since the rotating airflow in the exhaust pipe is of no benefit to separation, the high-speed rotation of the airflow only It can bring energy consumption, and the higher the rotation speed, the greater the rotational kinetic energy and the greater the energy consumption. In addition, the axial velocity of the airflow in the exhaust pipe gradually decreases from the side wall to the center, and the velocity gradient is large, showing the characteristics of a strong shear flow. The axial velocity even appears negative near the center, resulting in a recirculation zone. The existence of the recirculation zone near the center of the exhaust pipe will inevitably lead to an increase in the flow resistance in the exhaust pipe, resulting in a corresponding energy loss.
发明内容Contents of the invention
本发明的目的在于解决传统旋风分离器排气管内气流的高速旋转对分离毫无益处并且带来较大的能量损耗问题。本发明的另一个目的是解决传统旋风分离器排气管内所产生的回流区。The purpose of the present invention is to solve the problem that the high-speed rotation of the air flow in the exhaust pipe of the traditional cyclone separator is not beneficial to the separation and causes a large energy loss. Another object of the present invention is to address the recirculation zone created in the exhaust duct of a conventional cyclone separator.
本发明的技术方案:一种带有开缝式排气管的旋风分离器。其排气管安装在分离腔轴向位置,排气管的内插长度大约延伸到与入口底部齐平的位置,8个矩形直缝均匀分布于排气管下部,并且底部为封闭结构。The technical scheme of the present invention: a cyclone separator with a slotted exhaust pipe. The exhaust pipe is installed in the axial position of the separation chamber. The inset length of the exhaust pipe extends approximately to the level with the bottom of the inlet. Eight rectangular straight slits are evenly distributed in the lower part of the exhaust pipe, and the bottom is a closed structure.
本发明的优点与积极效果在于:此旋风分离器在工作时,由于排气管的底部为封闭结构并且在其下部均匀设置8个直缝,气体无法从排气管底部轴向进入,只能从直缝沿径向进入,当气体进入后从排气管沿轴向排出。此时排气管内气流不再高速旋转从而降低了能量损耗。由于底部为封闭结构,排气管中心附近轴向速度不会产生负值,从而抑制了回流区的产生。本发明结构合理,易于加工和制造,排气管的开缝式设计有效降低了排气管内部的能量损耗以及抑制了回流区的产生,减少了旋风分离器的内部压力损失,改善了旋风分离器的内部流场。The advantages and positive effects of the present invention are: when the cyclone separator is working, since the bottom of the exhaust pipe is a closed structure and 8 straight slits are evenly arranged at its lower part, the gas cannot axially enter from the bottom of the exhaust pipe, and can only It enters radially from the straight seam, and when the gas enters, it is discharged axially from the exhaust pipe. At this time, the air flow in the exhaust pipe no longer rotates at a high speed, thereby reducing energy loss. Because the bottom is a closed structure, the axial velocity near the center of the exhaust pipe will not have a negative value, thereby suppressing the generation of the recirculation zone. The invention has a reasonable structure and is easy to process and manufacture. The slotted design of the exhaust pipe effectively reduces the energy loss inside the exhaust pipe and suppresses the generation of the recirculation zone, reduces the internal pressure loss of the cyclone separator, and improves the cyclone separation. The internal flow field of the device.
附图说明Description of drawings
图1是本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
图2是图1中排气管的立体示意图。Fig. 2 is a schematic perspective view of the exhaust pipe in Fig. 1 .
图3是图1中排气管的正视图。Fig. 3 is a front view of the exhaust pipe in Fig. 1 .
图4是图1中排气管直缝处的剖视图。Fig. 4 is a cross-sectional view of the straight seam of the exhaust pipe in Fig. 1 .
图中:1为排气管,2为入口,3为分离腔,4为排尘口,5为直缝,6为封闭结构。In the figure: 1 is an exhaust pipe, 2 is an inlet, 3 is a separation chamber, 4 is a dust outlet, 5 is a straight seam, and 6 is a closed structure.
具体实施方式Detailed ways
下面结合附图1-4对本发明进行详细说明。The present invention will be described in detail below in conjunction with accompanying drawings 1-4.
1、实施例:1. Embodiment:
参照图1,图示中的旋风分离器,包括排气管(1)、入口(2)、分离腔(3)、排尘口(4),所述分离腔(3)与入口(2)密封对接形成该旋风分离器的外壳体,所述排气管(1)安装在分离腔(3)的轴线位置。上述的排气管(1)的下部分设置有直缝(5)并且底部为封闭结构(6)。上述的直缝(5)设置为8个并且均匀分布于排气管下部。排气管(1)的内插长度大约延伸到与入口(2)底部齐平的位置。Referring to Figure 1, the cyclone separator in the illustration includes an exhaust pipe (1), an inlet (2), a separation chamber (3), and a dust outlet (4), and the separation chamber (3) and the inlet (2) The outer casing of the cyclone separator is formed by sealing butt joint, and the exhaust pipe (1) is installed at the axial position of the separation chamber (3). The lower part of the above-mentioned exhaust pipe (1) is provided with a straight seam (5) and the bottom is a closed structure (6). The above-mentioned straight seams (5) are set to 8 and are evenly distributed in the lower part of the exhaust pipe. The inset length of the exhaust pipe (1) extends approximately flush with the bottom of the inlet (2).
本发明的工作原理:当待分离物料从旋风分离器的入口(2)进入分离器内部,该入口(2)沿切向布置。进入分离器内,气流便开始向下做旋转运动,在气流旋转的过程中,颗粒由于受到离心力的作用而向分离腔(3)以及排尘口(4)壁面运动,被甩向壁面的固体颗粒接触到壁面后自身失去了惯性力,便依靠自身的重力向下沉降,从排尘口(4)排出。气体沿螺旋线形式一直向下运动,直到旋风分离器下部圆锥段,进入圆锥段以后继续旋转下降,但是其旋转的半径越来越小,根据动量矩不变的原理,气体的速度不断的提高,当达到圆锥段的某一个点时,便以同样的旋转速度从旋风分离器中部,由下反转向上。由于排气管(1)底部为封闭结构(6),因此反转向上的气体只能从排气管的直缝(5)切向进入,最终从排气管(1)出口排出。The working principle of the present invention: when the material to be separated enters the separator from the inlet (2) of the cyclone separator, the inlet (2) is arranged tangentially. When entering the separator, the airflow begins to rotate downwards. During the rotation of the airflow, the particles are moved to the wall of the separation chamber (3) and the dust outlet (4) due to the centrifugal force, and are thrown to the solids on the wall. After the particles touch the wall, they lose their inertial force, and rely on their own gravity to settle down and be discharged from the dust outlet (4). The gas moves downward along the helical line until the cone section at the lower part of the cyclone separator. After entering the cone section, it continues to rotate and descend, but the radius of its rotation becomes smaller and smaller. According to the principle of constant momentum moment, the speed of the gas continues to increase. , when it reaches a certain point of the conical section, it will rotate from the middle of the cyclone separator to the top at the same rotation speed. Since the bottom of the exhaust pipe (1) is a closed structure (6), the upwardly reversed gas can only enter tangentially from the straight seam (5) of the exhaust pipe, and finally be discharged from the outlet of the exhaust pipe (1).
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720552166.3U CN207204400U (en) | 2017-05-18 | 2017-05-18 | A kind of cyclone separator with split blast pipe |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720552166.3U CN207204400U (en) | 2017-05-18 | 2017-05-18 | A kind of cyclone separator with split blast pipe |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207204400U true CN207204400U (en) | 2018-04-10 |
Family
ID=61811054
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720552166.3U Expired - Fee Related CN207204400U (en) | 2017-05-18 | 2017-05-18 | A kind of cyclone separator with split blast pipe |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207204400U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112973995A (en) * | 2021-04-07 | 2021-06-18 | 石河子大学 | Cyclone separator with contraction angle on feeding port |
-
2017
- 2017-05-18 CN CN201720552166.3U patent/CN207204400U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112973995A (en) * | 2021-04-07 | 2021-06-18 | 石河子大学 | Cyclone separator with contraction angle on feeding port |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2011137668A1 (en) | Cyclone dust collector | |
CN110270189B (en) | Guide vane type high-pressure cyclone separator | |
CN206276165U (en) | A kind of multistage cyclone separator | |
CN106824571B (en) | Cyclone separator | |
CN111637753B (en) | Centrifugal filter device for smoke dust of cooling tower | |
CN204544459U (en) | A kind of screw type prickle discharging pole | |
CN206549860U (en) | A kind of cyclones in series | |
CN207204400U (en) | A kind of cyclone separator with split blast pipe | |
CN105289861A (en) | Cyclone separator | |
CN205701110U (en) | A kind of drying machine cyclone dust extractor | |
CN202762559U (en) | Scroll cyclone dust collector | |
CN205613595U (en) | Cyclone dust collector | |
CN207308133U (en) | A kind of axial swirler and system for being suitable for gas-solid two phases | |
CN206549853U (en) | A kind of cyclone separator | |
CN201603630U (en) | A cyclone dust collector | |
CN210846797U (en) | Horizontal high-efficiency cyclone separator | |
CN211385433U (en) | Lower-section expansion type fine powder separator | |
CN204220315U (en) | A kind of cyclone separator | |
CN206661463U (en) | Circulation cyclone dust collectors for molecule | |
CN209901523U (en) | Wet cyclone separator and separating device | |
CN207929429U (en) | A kind of cyclone separator | |
CN113198257A (en) | High-efficiency gas-solid separation device | |
CN106269315A (en) | Inlet particle sequence type cyclone | |
CN111686519A (en) | Cyclone dust removal device | |
CN206549861U (en) | A kind of current stabilization double acting cyclone separator |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180410 Termination date: 20190518 |
|
CF01 | Termination of patent right due to non-payment of annual fee |