CN218392927U

CN218392927U - Combined type splitter

Info

Publication number: CN218392927U
Application number: CN202222958508.5U
Authority: CN
Inventors: 杨建�
Original assignee: Orange Cloud Internet Design Co ltd
Current assignee: Orange Cloud Internet Design Co ltd
Priority date: 2022-11-07
Filing date: 2022-11-07
Publication date: 2023-01-31
Anticipated expiration: 2032-11-07

Abstract

The utility model discloses a combined type splitter belongs to the technical field that the gaseous pollutants purified, including the barrel, the air intake has been seted up to the below of barrel one side, and the air outlet has been seted up at the top of barrel, and air intake, air outlet communicate the inside and the external world of barrel respectively, are equipped with the whirl board in the barrel, and the top of air intake is arranged in to the whirl board, is equipped with the interception dish device in the barrel, and the interception dish device is arranged in between air outlet and the whirl board. The pollutants with larger particle concentration and higher concentration are removed by the cyclone plate, and the pollutants with smaller concentration and lower concentration are removed by the intercepting disc device, so that the overall processing capacity of the composite separating equipment is improved.

Description

Combined type splitter

Technical Field

The utility model belongs to the technical field of the polluted gas purifies, especially, relate to a combined type splitter.

Background

The cyclone plate tower is a jet type tower plate washer, is a high-efficiency device for treating polluted gas, is often used as a first-stage device for treating polluted gas, and is used for treating polluted gas containing dust, oil, paint mist and the like.

However, in practical application, the applicant finds that: the condition that a large amount of water mist and pollutants are still carried in the gas from the cyclone plate is analyzed, and the applicant believes that the reason that the gas flow in the cyclone plate tower is high in flow velocity and discharged due to insufficient washing is solved, so that how to reduce the wind speed in the tower and improve the working effect of the cyclone plate tower is a technical problem to be solved by a person skilled in the art.

SUMMERY OF THE UTILITY MODEL

The utility model discloses to the not enough of prior art existence, provide a combined type splitter.

The utility model provides an above-mentioned technical problem's technical scheme as follows:

the utility model provides a combined type splitter, includes the barrel, the air intake has been seted up to the below of barrel one side, and the air outlet has been seted up at the top of barrel, and air intake, air outlet communicate the inside and the external world of barrel respectively, are equipped with the whirl board in the barrel, and the top of air intake is arranged in to the whirl board, are equipped with the intercepting dish device in the barrel, and the intercepting dish device is arranged in between air outlet and the whirl board.

Further, one side of barrel is provided with circulating water pump, and the bottom of barrel is provided with the circulating water tank who is linked together with the barrel is inside, and circulating water pump's inlet tube and circulating water tank communicate each other, and the tip of circulating water pump's outlet pipe is equipped with the shower nozzle, and the shower nozzle is arranged in the inside of barrel and is located between whirl board and the interception dish device, and the shower nozzle just is to the whirl board.

Further, the spray head is provided with a plurality of spray heads.

Furthermore, the intercepting disc device comprises a plurality of dynamic intercepting discs which are vertically distributed in the cylinder body, and each dynamic intercepting disc is driven by a corresponding motor.

Furthermore, the intercepting disc device comprises a plurality of dynamic intercepting discs which are vertically distributed in the cylinder body, and the dynamic intercepting discs are driven by a motor.

Furthermore, the intercepting disc device comprises a plurality of dynamic intercepting discs, the dynamic intercepting discs are horizontally distributed in the cylinder body, and each dynamic intercepting disc is driven by a motor corresponding to the dynamic intercepting disc.

Further, the number of the dynamic intercepting discs is at least two.

In summary, compared with the prior art, the above technical solution has at least one of the following beneficial effects:

(1) The utility model combines the separation technology of the spiral-flow plate and the separation technology of the dynamic intercepting plate, firstly carries out primary treatment on the dusty gas passing through the spiral-flow plate, then carries out secondary treatment through the intercepting plate device, and intercepts the pollutants leaked out of the incomplete demisting of the spiral-flow plate, thereby improving the overall treatment effect;

(2) In terms of functional division, pollutants with larger particles and higher concentration are removed by the aid of a rotational flow plate technology, and pollutants with smaller concentration and lower concentration are removed by the aid of a dynamic intercepting disc technology, so that overall processing capacity of equipment can be improved;

(3) The cyclone plate belongs to a wet centrifugal wind power driven decontamination mode, the intercepting plate device belongs to a dry dynamic intercepting decontamination mode, the decontamination efficiency of the cyclone plate can be changed by the fluctuation of wind speed, the intercepting plate device is relatively stable and controllable, the performances of the two devices have certain complementarity, the other function of the dynamic intercepting plate is a defogging function, the dynamic intercepting plate is used for replacing a defogging section in a cyclone plate tower to carry out dynamic defogging, and compared with the static defogging in a classical cyclone plate tower, the defogging effect is better, and meanwhile, the occupied space is smaller;

(4) The spray head sprays water mist, which is helpful to prevent viscous liquid drops from adhering to the dynamic interception disk and not falling off, and is helpful to form a liquid film on the dynamic interception disk and the surface of dust for dust pollutants, so that the dust can adhere to the dynamic interception disk and be separated.

Drawings

Fig. 1 is a schematic view of an overall structure in an embodiment of the present invention;

fig. 2 is a schematic diagram of an overall structure in an embodiment of the present invention;

fig. 3 is a schematic diagram of the overall structure in the embodiment of the present invention.

Description of the reference numerals: 1. a cylinder body; 11. an air inlet; 12. an air outlet; 2. a swirl plate; 3. a catch tray device; 31. a dynamic intercepting disc; 32. a motor; 4. a water circulating pump; 5. a circulating water tank; 6. and (4) a spray head.

Detailed Description

The principles and features of the present invention are described below in conjunction with the following drawings, the examples given are only intended to illustrate the present invention and are not intended to limit the scope of the present invention.

The embodiment of the utility model discloses combined type splitter.

Referring to fig. 1-3, a combined type separation device comprises a cylinder 1, wherein the cylinder 1 is in a cylindrical shape, a circular air inlet 11 is formed below one side of the cylinder 1, a circular air outlet 12 is formed at the top of the cylinder 1, the air inlet 11 and the air outlet 12 are respectively communicated with the inside and the outside of the cylinder 1, and dust-containing gas enters the cylinder 1 from the air inlet 11 and then flows out from the air outlet 12.

The cyclone plate 2 is horizontally installed in the cylinder 1, the cyclone plate 2 is arranged above the air inlet 11, and dust-containing gas enters the cylinder 1 and then passes through the cyclone plate 2 to change the flow direction.

One side of barrel 1 is provided with circulating water pump 4, and the bottom of barrel 1 is provided with the circulating water tank 5 that is linked together with barrel 1 inside, and circulating water pump 4's inlet tube and circulating water tank 5 communicate each other, and shower nozzle 6 is installed to the tip of circulating water pump 4's outlet pipe, and shower nozzle 6 can have one also can have a plurality ofly, and shower nozzle 6 is arranged in barrel 1's inside and is arranged in directly over whirl board 2, and shower nozzle 6 is just to setting up with whirl board 2. And starting the circulating water pump 4, enabling the dust-containing gas passing through the cyclone plate 2 to be combined with pollutants such as pollutant particles and oil drops under the action of water mist sprayed by the spray head 6, throwing the water drops and the pollutants with larger particles onto the wall surface of the barrel body 1 under the action of centrifugal force, enabling the pollutants to flow into the circulating water tank 5 at the bottom along with water flow on the wall surface of the barrel body 1, and enabling the residual fine particle pollutants in the air flow to continuously flow upwards along with the air flow and the water mist.

The barrel body 1 is internally provided with an intercepting disc device 3, the intercepting disc device 3 is arranged between the air outlet 12 and the rotational flow plate 2, and meanwhile, the intercepting disc device 3 is positioned above the spray head 6, so that the spray head 6 is positioned between the rotational flow plate 2 and the intercepting disc device 3. Finer liquid droplets or particles in the upwardly flowing gas are intercepted by the intercepting disc means 3 when passing the intercepting disc means 3. Because the spray head 6 for continuously spraying water mist is arranged at the lower part of the intercepting disc device 3 during operation, the intercepting disc device 3 is always wetted by the water mist, a layer of water is arranged on the outer surface of the liquid drop with stronger viscosity, the liquid drop is prevented from being adhered to the intercepting disc device 3, and the liquid drop is thrown onto the inner wall of the cylinder body 1 along with the high-speed rotation of the intercepting disc device 3, so that the normal operation of the system can be guaranteed.

For dust pollutants, fine dust can be adhered and intercepted by the intercepting disc device 3 after being wetted by water mist, and is thrown to the inner wall of the cylinder body 1 under the action of centrifugal force along with water flow on the surface of the intercepting disc device 3 for separation.

The rotational flow plate 2 and the intercepting plate device 3 have the characteristics of low wind resistance and high dirt removing capacity. The cyclone plate 2 belongs to a wet centrifugal wind-driven decontamination mode, and the intercepting disc device 3 belongs to a dry dynamic intercepting decontamination mode. The decontamination efficiency of the rotational flow plate 2 can be changed by the fluctuation of the wind speed, and the intercepting disc device 3 is relatively stable and controllable; the two have certain complementarity in performance.

At the in-process of handling the pollutant, earlier carry out preliminary treatment through the dirty gas of whirl board 2, carry out secondary treatment through intercepting dish device 3 again, intercept 2 not thorough and the pollutant that spills of whirl board defogging to promote holistic treatment.

The intercepting disc device 3 is driven by the motor 32 to rotate at a high speed, air flow flows through gaps in the intercepting disc device 3, liquid drops such as oil stains, water mist and the like in the air flow can be adhered to the intercepting disc device 3 when contacting with the intercepting disc device 3, are thrown onto the wall of the outer side of the intercepting disc device 3 under the action of centrifugal force, and then flow to the bottom along with gravity. The water mist sprayed by the spray head 6 just solves the problem that the over-adhered liquid drops are not easy to flow when adhered to the intercepting disc device 3.

As shown in fig. 1, the intercepting disc device 3 has many combinations, and may include two dynamic intercepting discs 31, the two dynamic intercepting discs 31 are sequentially disposed in an up-down relationship inside the cylinder 1, and each dynamic intercepting disc 31 is driven by a corresponding motor 32. The dust-containing gas is treated by the two dynamic intercepting discs 31, and the separation section of the rear part of the cyclone plate 2 tower is replaced, so that the demisting capacity is improved.

As shown in fig. 2, the catch tray device 3 may further include two dynamic catch trays 31, the two dynamic catch trays 31 are sequentially disposed inside the barrel 1 in an up-down relationship, but the two dynamic catch trays 31 are driven by a motor 32. When saving a motor 32, carry out secondary treatment to dirty gas, replace 2 tower back parts's on whirl board separation sections, improve the defogging ability.

As shown in fig. 3, the intercepting pan device 3 may further include three dynamic intercepting pans 31, the three dynamic intercepting pans 31 are sequentially arranged inside the barrel 1 in a horizontal relationship, the three dynamic intercepting pans 31 jointly form a plane to intercept the internal cavity of the barrel 1, at this time, each dynamic intercepting pan 31 is driven by a corresponding motor 32, so as to process the dust-containing gas, replace a separation section at the rear part of the cyclone plate 2 tower, and improve the defogging capability.

The above is a combination of three kinds of dynamic intercepting disks 31, and other combinations such as series connection and parallel connection between other numbers of dynamic intercepting disks 31 may be used.

The implementation principle of the combined type separation equipment in the embodiment of the application is as follows:

during operation dirty gas gets into barrel 1 from air intake 11, enters the air current district after 2 direction of whirl board afterwards, starts circulating water pump 4, and 6 blowout water smoke of shower nozzle, dirty gas enter into the mixed district of air current and water smoke, and the pollutant in the air current here produces the condensation after mixing with water, and volume and weight can increase, and great granule pollutant level water droplet is got rid of to barrel 1 inner wall under the effect of centrifugal force afterwards, flows down along barrel 1 inner wall along with the water under the effect of gravity. The fine fog drops and pollutants enter the intercepting disc device 3 along with the air flow to be intercepted, and the residual clean air flow flows out from the air outlet.

The above description is only for the preferred embodiment of the present invention, and is not intended to limit the present invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included within the protection scope of the present invention.

Claims

1. A combined type splitter, its characterized in that: including barrel (1), air intake (11) have been seted up to the below of barrel (1) one side, and air outlet (12) have been seted up at the top of barrel (1), and air intake (11), air outlet (12) communicate the inside and the external world of barrel (1) respectively, are equipped with whirl board (2) in barrel (1), and the top of air intake (11) is arranged in whirl board (2), are equipped with in barrel (1) and intercept dish device (3), and intercept dish device (3) are arranged in between air outlet (12) and whirl board (2).

2. The composite separation apparatus of claim 1, wherein: one side of barrel (1) is provided with circulating water pump (4), and the bottom of barrel (1) is provided with circulating water tank (5) that are linked together with barrel (1) inside, and circulating water pump's (4) inlet tube and circulating water tank (5) communicate each other, and the tip of the outlet pipe of circulating water pump (4) is equipped with shower nozzle (6), and inside of barrel (1) is arranged in shower nozzle (6) and is located between whirl board (2) and intercepting dish device (3), and shower nozzle (6) are just to whirl board (2).

3. The composite separation apparatus of claim 2, wherein: the spray head (6) is provided with a plurality of spray heads.

4. The composite separation apparatus of claim 1, wherein: the intercepting disc device (3) comprises a plurality of dynamic intercepting discs (31), the dynamic intercepting discs (31) are vertically distributed in the cylinder body (1), and each dynamic intercepting disc (31) is driven by a motor (32) corresponding to the dynamic intercepting disc (31).

5. The composite separation apparatus of claim 1, wherein: the intercepting disc device (3) comprises a plurality of dynamic intercepting discs (31), the dynamic intercepting discs (31) are vertically distributed in the cylinder body (1), and the dynamic intercepting discs (31) are driven by a motor (32) together.

6. The composite separation apparatus of claim 1, wherein: the intercepting disc device (3) comprises a plurality of dynamic intercepting discs (31), the dynamic intercepting discs (31) are horizontally distributed in the cylinder body (1), and each dynamic intercepting disc (31) is driven by a motor (32) corresponding to the dynamic intercepting disc (31).

7. A combined separating device according to one of the claims 4-6, characterised in that the number of the dynamic intercepting discs (31) is at least two.