CN210905518U

CN210905518U - Cyclone gas-liquid separator

Info

Publication number: CN210905518U
Application number: CN201921932721.0U
Authority: CN
Inventors: 郭庆保; 黄建春; 郭峰
Original assignee: Ningbo Jiangshen Environmental Protection Equipment Co ltd
Current assignee: Ningbo Jiangshen Environmental Protection Equipment Co ltd
Priority date: 2019-11-11
Filing date: 2019-11-11
Publication date: 2020-07-03
Anticipated expiration: 2029-11-11

Abstract

The cyclone gas-liquid separator comprises a mandrel, a hub and cyclone plates, wherein the hub is arranged at the periphery of the mandrel, at least three cyclone plates are uniformly distributed at the periphery of the hub, and a separation net is arranged between every two adjacent cyclone plates. Further, the separation mesh is non-planarly arranged between adjacent swirl plates. Further, the separation net between the cyclone plates comprises at least two layers of wire nets. Furthermore, each layer of silk screen is provided with a plurality of bulges along the length direction, and gaps exist between every two adjacent layers of silk screens. Furthermore, the separation net between the rotational flow plates is fixedly arranged on the hub in a V shape. The utility model has the advantages of: still can install direct and urceolus fixed connection in the dabber to further play and support the fixed action, the utility model discloses still have small, simple structure, the resistance is little, need not frequent maintenance, and the running cost is low, and dust collection efficiency is high, purifies back air water content low grade advantage.

Description

Cyclone gas-liquid separator

Technical Field

The utility model belongs to the technical field of the dust removal technique and specifically relates to a whirl vapour and liquid separator.

Background

At present, in various construction sites with more dust, a wet dust collector is generally used for processing the dust and is used as a gas-liquid separator with a main function in the wet dust collector, the existing gas-liquid separator mostly depends on an internal cyclone plate to adsorb mixed water mist, then the gas-liquid separator plays a role in gas-water separation through centrifugal force and finally achieves the purpose of dust removal, but the existing cyclone plate has limited adsorption capacity on the water mist, the defects of large volume and large wind resistance of the cyclone plate generally exist for increasing the contact area with the water mist, and the dust removal efficiency is low.

Disclosure of Invention

In order to solve the above problems, an object of the present invention is to provide a cyclone gas-liquid separator, which increases the adsorption capacity of water mist through the separation net between the cyclone plate and the cyclone plate, and further improves the dust removal efficiency of the whole device.

The utility model provides a technical scheme that its technical problem adopted is: a whirl vapour and liquid separator, including dabber, wheel hub and whirl board, wheel hub installs in the periphery of dabber, wheel hub's periphery evenly distributed has at least three whirl board, all installs the separation net between the adjacent whirl board. Further, the separation mesh is non-planarly arranged between adjacent swirl plates. Further, the separation net between the cyclone plates comprises at least two layers of wire nets. Furthermore, each layer of silk screen is provided with a plurality of bulges along the length direction, and gaps exist between every two adjacent layers of silk screens. Furthermore, the separation net between the rotational flow plates is fixedly arranged on the hub in a V shape. Furthermore, a connecting column is fixedly installed on the hub between every two adjacent rotational flow plates, the separation net is lapped on the connecting column, and the separation net between every two adjacent rotational flow plates is arranged in a V shape. Further, a support is fixedly mounted on the mandrel, an outer barrel is sleeved on the periphery of the support, and the spiral-flow plate and the separating net are both located in the outer barrel.

The utility model has the advantages of: a whirl vapour and liquid separator, the area of contact of increase and water smoke can be showing to the separation net of installation between the adjacent whirl board to improve the adsorption efficiency of its water smoke, the separation net comprises the multilayer silk screen, can also reduce the resistance when rotatory when increasing water smoke adhesive force. The area that the separation net can increase around wheel hub with the multifold structure of V type encircles, can guarantee like this and catch dirt efficiency and can reduce the ventilation resistance again to realize high-efficient low energy. Still can install direct and urceolus fixed connection in the dabber to further play and support the fixed action, the utility model discloses still have small, simple structure, the resistance is little, need not frequent maintenance, and the running cost is low, and dust collection efficiency is high, purifies back air water content low grade advantage.

Drawings

Fig. 1 is a schematic diagram of a three-dimensional structure of the present invention;

FIG. 2 is an enlarged partial view of I of FIG. 1;

FIG. 3 is a schematic view of the construction of a screen;

FIG. 4 is a schematic sketch of a position of the separation wire between the swirl plates;

FIG. 5 is a schematic sketch of another position of the separation mesh between the swirl plates;

FIG. 6 is a schematic view of the present invention with the bracket and the outer barrel;

FIG. 7 is a schematic structural view of another embodiment of the whirl plate of the present invention;

fig. 8 is an end view of the structure of fig. 7.

In the figure, 1, a mandrel 2, a hub 3, a cyclone plate 4, a separation net 5, a connecting column 6, a bracket 7, an outer cylinder 8 and a wire net 8.

Detailed Description

A whirl vapour and liquid separator, as shown in figure 1, including dabber 1, wheel hub 2 and whirl board 3, wheel hub 2 installs in dabber 1's periphery, and dabber 1 is located wheel hub 2 central point and puts, and whirl vapour and liquid separator can use dabber 1 to rotate as the center. Wheel hub 2's periphery evenly distributed has at least three whirl board 3, whirl board 3 with certain angle evenly distributed in wheel hub 2's the outside and with wheel hub 2 fixed together, all install separation net 4 between the adjacent whirl board 3, separation net 4 can follow the high-speed rotation of whirl board 3, separation net 4 collides at water smoke, the dust in the in-process of high-speed rotation with the air, water smoke forms the water curtain on separation net 4, greatly increased the catching ability to slight dust.

Furthermore, the separation net 4 is arranged between the adjacent rotational flow plates 3 in a non-planar manner, so that the contact area of the whole rotational flow gas-liquid separator with water mist and dust can be increased, and the stroke of the dust-containing air flow in the rotational flow gas-liquid separator is increased, so that the adsorption capacity of the water mist and the dust is improved.

Further, as shown in fig. 2, the separation net 4 between the cyclone plates 3 comprises at least two layers of wire nets 8, as shown in fig. 3, each layer of wire net 8 is provided with a plurality of bulges along the length direction thereof, the bulges on the wire nets 8 can enable certain gaps to exist between the adjacent wire nets 8, the gaps allow dust-removing gas to pass through while the capture area of water mist and dust is increased, the wind resistance of the separation net 4 during rotation is effectively reduced, the arrangement of the multiple layers of wire nets 8 can further refine the requirements of the whole cyclone gas-liquid separator on the grade of dust-removing particles, meanwhile, the collision between the dust-removing gas and the wire nets 8 is increased, and the dust-removing efficiency is improved. When the air containing water mist and dust passes through the cyclone gas-liquid separator, the cyclone plate 3 rotates at a high speed due to kinetic energy generated by air flow, so that the separation net 4 rotates, the separation net 4 collides with the water mist and the dust in the dedusting gas at a high speed, the water mist forms a water curtain on the separation net 4, the contact area of the separation net 4 and the dust can be further increased by the water curtain, and the adsorption capacity to fine dust is greatly increased.

Further, separation net 4 between the whirl board 3 is V type fixed mounting on wheel hub 2, and separation net 4 encircles around wheel hub 2 in order to increase separation net 4's area with the multifold structure of V type, can guarantee like this to catch dirt efficiency and can reduce ventilation resistance again to realize high-efficient low energy. The mounting means of separation net 4 can be in advance with separation net 4 operation of buckling, then will buckle separation net 4 fixed connection after again in 2 peripheries of wheel hub, be the V type state between adjacent whirl board 3 in order to further guarantee that separation net 4 can be, and can not produce deformation etc. along with the increase of live time, a spliced pole 5 of fixed mounting on wheel hub 2 between two adjacent whirl boards 3, separation net 4 overlap joint is on spliced pole 5, separation net 4 between every two adjacent whirl boards 3 is the V type and arranges. As shown in fig. 4, when spliced pole 5 is located 2 upside positions of wheel hub, the lower extreme of whirl board 3, the upper end of spliced pole 5 and the lower extreme of adjacent whirl board 3 are walked around in proper order to separation net 4, are the type of falling V and arrange, as shown in fig. 5, when spliced pole 5 is located 2 downside positions of wheel hub, the upper end of whirl board 3, the lower extreme of spliced pole 5 and the upper end of adjacent whirl board 3 are walked around in proper order to separation net 4, are the type of V and arrange. Wherein, a plurality of connecting columns 5 can be arranged on the upper side and the lower side of the hub 2, and the separating net 4 can sequentially pass through the connecting columns 5 at the adjacent upper and lower positions to be fixed on the hub 2 in a V-shaped surrounding manner.

Further, as shown in fig. 6, fixed mounting has support 6 on the dabber 1, and the periphery cover of support 6 is equipped with urceolus 7, and whirl board 3 and separation net 4 all are located urceolus 7, and when the gravity that its self produced of the dusty liquid drop of gathering on whirl board 3 and the separation net 4 exceeded the adsorption efficiency of separation net 4, rely on the rotatory produced centrifugal force of high-speed rotation of whirl vapour and liquid separator to throw the dusty liquid drop to urceolus 7 inner wall, fall through the dead weight, carry out unified collection processing to reach the purpose of gas-water separation and final dust removal. Wherein the bracket 6 can be arranged on the upper part of the separation net 4 or on the lower part of the separation net 4, and mainly plays a role in supporting and fixing.

As shown in fig. 7 and 8, be another structure embodiment of whirl plate 3 when not installing separation net 4, wherein whirl plate 3 slope certain angle evenly distributed is in wheel hub 2 periphery and together fixed with wheel hub 2, as shown in fig. 8, see at the terminal surface, its whirl plate 3 covers each other in proper order, do not have the clearance to form a confined plane each other, can increase the area of contact with water smoke and dust, dirty gas can drive whirl plate 3 when the process rotates, the collision of water smoke and dust between 3 axial intervals of two whirl plates is strengthened at the rotation in-process, can further improve whirl plate 3 adsorption efficiency to the dust, thereby improve whole device's dust collection efficiency.

Technical scheme of the utility model not be restricted to the utility model the within range of embodiment. The technical contents not described in detail in the present invention are all known techniques.

Claims

1. The utility model provides a whirl vapour and liquid separator, includes dabber (1), wheel hub (2) and whirl board (3), its characterized in that: wheel hub (2) are installed in the periphery of dabber (1), and the periphery evenly distributed of wheel hub (2) has at least three whirl board (3), all installs separation net (4) between adjacent whirl board (3).

2. The cyclone gas-liquid separator according to claim 1 wherein: the separation mesh (4) is arranged non-planar between adjacent swirl plates (3).

3. The cyclone gas-liquid separator according to claim 1 wherein: the separation net (4) between the cyclone plates (3) comprises at least two layers of wire nets (8).

4. The cyclone gas-liquid separator according to claim 3 wherein: each layer of silk screen (8) is provided with a plurality of bulges along the length direction, and gaps are reserved between every two adjacent silk screens (8).

5. The cyclone gas-liquid separator according to claim 1 wherein: the separation net (4) between the rotational flow plates (3) is fixedly arranged on the hub (2) in a V shape.

6. The cyclone gas-liquid separator according to claim 5 wherein: a connecting column (5) is fixedly installed on the hub (2) between every two adjacent cyclone plates (3), the separating net (4) is in lap joint with the connecting column (5), and the separating net (4) between every two adjacent cyclone plates (3) is arranged in a V shape.

7. The cyclone gas-liquid separator according to claim 1 wherein: the cyclone separator is characterized in that a support (6) is fixedly mounted on the mandrel (1), an outer barrel (7) is sleeved on the periphery of the support (6), and the cyclone plate (3) and the separating net (4) are located in the outer barrel (7).