Novel efficient dust remover

Through the design of the new high-efficiency dust collector, the centrifugal separation of the cyclone pipe and the water impact effect of the lower impact water tank are solved, and the dust removal effect is efficient, energy-saving, compact and easy-to-maintenance dust removal effect is achieved.

CN120054147APending Publication Date: 2025-05-30HEBEI GUOHUA DINGZHOU POWER GENERATION
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Patent Information

Application Number
CN202510214577.0
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-02-26
Publication Date
2025-05-30

AI Technical Summary

Technical Problem

Traditional dust collectors have problems such as low dust removal efficiency, large equipment size, high operating cost and difficult maintenance, especially poor dust removal effect on high-specific resistance dust.

Method used

The design of a new high-efficiency dust collector is adopted, including an upper adsorption purification box, a cyclone air intake chamber and a lower impact water tank. The dual functions of centrifugal separation of the cyclone pipe and the water impact of the lower impact water tank are achieved efficient dust removal.

Benefits of technology

It realizes efficient removal of dust particles in dust-containing gas. The dust collector is small in size and covers a small area, which is easy to install and maintain, has low operating costs and is convenient to maintain.

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Abstract

The invention discloses a novel efficient dust remover, and belongs to the technical field of dust removers, the novel efficient dust remover comprises an upper adsorption purification box, a cyclone air inlet bin and a lower impact water tank, the upper adsorption purification box is communicated with the cyclone air inlet bin, the lower impact water tank is communicated with the lower part of the cyclone air inlet bin, a cyclone is mounted outside the cyclone air inlet bin, and the cyclone air inlet bin is communicated with the lower impact water tank. Due to the structural design that the multiple row cyclone pipes are connected in parallel, when the dust remover treats large air volume, the size is still small, the occupied area is small, the dust remover can be conveniently installed and used in various industrial places, water is adopted as a dust removal medium, expensive filtering materials or complex electrostatic equipment does not need to be used, the operation cost is low, and meanwhile due to the high dust removal efficiency, the dust removal effect is good. The structure is simple, no complex quick-wear part exists, the daily maintenance is mainly to regularly clean the sewage draining exit and check the water level control system, the maintenance workload is small, and the maintenance cost is low.
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Description

Technical Field

[0001] The present invention relates to the technical field of dust collectors, and specifically, to a novel and efficient dust collector. Background Art

[0002] During the industrial production process, a large amount of waste gas containing dust is generated. If these dusts are directly discharged into the atmosphere, it will not only cause serious environmental pollution, but also endanger human health. Traditional dust collectors have problems such as low dust removal efficiency, large equipment volume, high operating cost, and difficult maintenance. For example, in a common bag dust collector, the bags are easily blocked and need to be frequently replaced, increasing the operating cost and maintenance workload; while the electrostatic dust collector has certain requirements for the specific resistance of dust, and the dust removal effect for high specific resistance dust is not good. Developing an efficient, energy-saving, compact and easy-to-maintain dust collector has important practical significance. Therefore, a novel and efficient dust collector is proposed. Summary of the Invention

[0003] The purpose of the present invention is to provide a novel and efficient dust collector to solve the problems raised in the above background art.

[0004] To achieve the above purpose, the present invention provides the following technical solution: A novel and efficient dust collector includes an upper adsorption purification box, a cyclone inlet chamber, and a lower impact water tank. The upper adsorption purification box is connected to the cyclone inlet chamber, the lower impact water tank is connected to the lower part of the cyclone inlet chamber. A cyclone is installed outside the cyclone inlet chamber, and the external dust-containing gas is connected to the air inlet of the cyclone. A spray pipe is connected to the cyclone, and the water outlet end of the spray pipe penetrates through the outer wall of the cyclone. A baffle is fixedly connected inside the cyclone inlet chamber, and the baffle is located above the air outlet of the cyclone. A cyclone water body dust removal structure is installed inside the cyclone inlet chamber, and dust removal water is stored inside the lower impact water tank, and the lower end of the cyclone water body dust removal structure is inserted into the dust removal water.

[0005] Preferably, the cyclone dust removal structure includes a header air distribution box, the header air distribution box is installed inside the cyclone inlet chamber, a row of cyclone pipes is installed below the header air distribution box, and the lower air outlet of the row of cyclone pipes is inserted into the dust removal water.

[0006] Preferably, a spray inlet pipe is installed inside the lower impact water tank, and a plurality of spray holes are opened outside the spray inlet pipe.

[0007] Preferably, an overflow pipe is connected inside the lower impact water tank, the water outlet of the overflow pipe penetrates through the outer wall of the lower impact water tank, and the water inlet position of the overflow pipe is higher than the spray inlet pipe.

[0008] Preferably, an electric drain valve is connected to the bottom of the lower impact water tank.

[0009] Preferably, a liquid level gauge is installed on the electric sewage discharge valve.

[0010] Preferably, a demister is installed inside the upper adsorption purification tank.

[0011] Preferably, a purified air outlet pipe is connected to the outside of the upper adsorption purification tank, and one end of the purified air outlet pipe away from the upper adsorption purification tank is connected to a negative pressure fan.

[0012] Preferably, an observation window is installed on the outside of the upper adsorption purification tank.

[0013] Preferably, four support feet are installed on the outside of the lower impact water tank.

[0014] Compared with the prior art, the beneficial effects of the present invention are as follows: In the present invention, through the dual effects of the centrifugal separation of the row-connected cyclone tubes and the water impact of the lower impact water tank, the dust particles in the dust-containing gas can be effectively removed. The structural design of multiple row-connected cyclone tubes in parallel enables the dust collector to have a relatively small volume and a small floor area when dealing with a large gas volume, which is convenient for installation and use in various industrial sites. The present invention uses water as the dust removal medium, without the need to use expensive filter materials or complex electrostatic equipment, resulting in low operating costs. At the same time, due to the high dust removal efficiency, the cost of subsequent waste gas treatment is reduced, and the maintenance is convenient: the structure is simple, without complex vulnerable parts, and the daily maintenance mainly includes regularly cleaning the sewage outlet and checking the water level control system, with a small amount of maintenance work and low maintenance costs. BRIEF DESCRIPTION OF THE DRAWINGS

[0015] Figure 1 is one of the three-dimensional structural schematic diagrams in the embodiment of the present invention; Figure 2 is the three-dimensional sectional structural schematic diagram in the embodiment of the present invention; Figure 3 is the second three-dimensional structural schematic diagram in the embodiment of the present invention.

[0016] In the figure: 100, upper adsorption purification tank; 101, purified air outlet pipe; 102, negative pressure fan; 103, cyclone; 104, spray pipe; 105, lower impact water tank; 106, electric sewage discharge valve; 107, support foot; 108, cyclone inlet chamber; 109, baffle; 200, header air distribution box; 201, row-connected cyclone tubes; 202, spray inlet pipe; 203, overflow pipe; 300, liquid level gauge; 400, observation window; 500, demister. DETAILED DESCRIPTION OF THE EMBODIMENTS

[0017] The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. All other embodiments obtained by those of ordinary skill in the art based on the embodiments of the present invention without creative efforts shall fall within the protection scope of the present invention.

[0018] As Figure 1 - Figure 2 shown, a novel and efficient dust collector of the present application includes an upper adsorption purification box 100, a cyclone air inlet chamber 108, and a lower impact water tank 105. The upper adsorption purification box 100 is connected to the cyclone air inlet chamber 108, the lower impact water tank 105 is connected below the cyclone air inlet chamber 108, a cyclone 103 is installed outside the cyclone air inlet chamber 108, an external dust-laden gas pipeline is connected to the air inlet of the cyclone 103, a spray pipe 104 is connected to the cyclone 103, and the water outlet end of the spray pipe 104 penetrates the outer wall of the cyclone 103. A baffle 109 is fixedly connected inside the cyclone air inlet chamber 108, and the baffle 109 is located above the air outlet of the cyclone 103. A cyclone water body dust removal structure is installed inside the cyclone air inlet chamber 108, the lower impact water tank 105 stores dust removal water, and the lower end of the cyclone water body dust removal structure is inserted into the dust removal water.

[0019] Specifically, during the use process, an industrial dust removal pipe is connected through the cyclone 103, and the industrial dust removal pipe continuously conveys the dust-laden gas into the cyclone 103. When the dust-laden gas continuously enters the cyclone 103, primary dust removal is carried out by the water flow sprayed from the spray pipe 104. After primary dust removal, the gas is continuously conveyed into the cyclone air inlet chamber 108. After the gas continuously enters the cyclone air inlet chamber 108, it will first be blocked by the baffle 109, and the larger dust particles in the gas are blocked by the baffle 109 and fall off and are removed. The smaller dust particles are sprayed again by the spray pipe 104 and enter the lower impact water tank 105 together with the air flow. After the dust falls into the lower impact water tank 105, it will come into contact with the dust removal water inside the lower impact water tank 105, and secondary dust removal is carried out through the cyclone water body dust removal structure.

[0020] As Figure 1 - Figure 2 shown, the cyclone dust removal structure includes a header air distribution box 200, the header air distribution box 200 is installed inside the cyclone air inlet chamber 108, a row of cyclone pipes 201 is installed below the header air distribution box 200, and the lower air outlet of the row of cyclone pipes 201 is inserted into the dust removal water.

[0021] Specifically, in the cyclone dust removal structure, after the gas enters the interior of the lower impact water tank 105, by continuously injecting air flow into the interior of the multiple row-connected cyclone tubes 201, the air flow with dust will also enter the interior of the row-connected cyclone tubes 201. Inside the row-connected cyclone tubes 201, there is a spiral channel (not shown in the figure), and the spiral channel is a tapered structure, with the pipe diameter gradually decreasing from the air inlet end to the air outlet end. This can enhance the rotation speed of the gas and increase the centrifugal force, thereby more effectively separating dust particles. And after the air flow with dust is ejected together through the air outlet of the row-connected cyclone tubes 201, the ejected air flow has a greater impact force and is ejected from the air outlet of the row-connected cyclone tubes 201 at a higher speed, impacting the dust removal water and thus hitting up a large amount of foam and water droplets, so as to achieve the purpose of purifying the air.

[0022] Furthermore, the multiple row-connected cyclone tubes 201 are in a parallel structure, which increases the gas processing capacity and improves the overall dust removal efficiency of the dust collector. Moreover, this structure makes the volume of the dust collector relatively small, facilitating installation and maintenance.

[0023] As Figure 1 and Figure 2 shown, a demister 500 is installed inside the upper adsorption purification box 100, and a purified air outlet pipe 101 is connected to the outside of the upper adsorption purification box 100. One end of the purified air outlet pipe 101 away from the upper adsorption purification box 100 is connected to a negative pressure fan 102.

[0024] Specifically, after the gas with dust is dust-removed by the row-connected cyclone tubes 201 and the dust removal water, the staff can turn on the negative pressure fan 102. When the negative pressure fan 102 is turned on, the purified gas, under the negative pressure of the negative pressure fan 102, passes through the demister 500 and is discharged by the negative pressure fan 102, and the water droplets contained in the purified gas are removed by the demister 500.

[0025] As Figure 2 shown, a spray inlet pipe 202 is installed inside the lower impact water tank 105. A plurality of spray holes are opened on the outside of the spray inlet pipe 202. By continuously injecting water flow into the interior of the spray inlet pipe 202 through an external water pipe, the water flow can be sprayed onto the side wall surface of the lower impact water tank 105 through the externally opened spray holes, thereby flushing the side wall surface of the lower impact water tank 105, and the water flow ejected through the spray holes is used to supplement the dust removal water inside the lower impact water tank 105.

[0026] As Figure 2 and Figure 3 shown, an overflow pipe 203 is connected to the inside of the lower impact water tank 105. The water outlet of the overflow pipe 203 penetrates the outer wall of the lower impact water tank 105, and the water inlet position of the overflow pipe 203 is higher than that of the spray inlet pipe 202.

[0027] Specifically, through the setting of the overflow pipe 203, when the water flow inside the lower impact water tank 105 is excessive and the water level reaches the inlet position of the overflow pipe 203, the water flow will be discharged to the outside through the overflow pipe 203, preventing the water flow from continuously accumulating inside the lower impact water tank 105.

[0028] As Figure 1 - Figure 3 shown, an electric sewage discharge valve 106 is connected to the bottom of the lower impact water tank 105, and a liquid level gauge 300 is installed on the electric sewage discharge valve 106. After the dust removal water for purifying gas is used for a certain period of time, it needs to be replaced because the water contains a large amount of dust. When replacing the water, the electric sewage discharge valve 106 is opened, and the sewage containing a large amount of dust is discharged through the drain port. When the sewage is basically drained, the liquid level gauge 300 controls the solenoid valve installed on the water inlet main pipe to open (the water supply pressure is 2 - 4 kg / cm), and the water is sprayed out through the spray holes outside the header air distribution box 200 by the water inlet pipe, washing the bottom of the lower impact water tank 105 clean. After washing, the electric sewage discharge valve 106 is closed, and the water surface in the lower impact water tank 105 rises. When the water surface rises to the height required for dust removal, the continuous supply of water flow to the spray water inlet pipe 202 is cancelled, and the water supply is interrupted. The excess water in the box body is discharged through the overflow pipe 203: At this time, the dust collector can enter the working state.

[0029] As Figure 1 shown, four support feet 107 are installed outside the lower impact water tank 105, and the lower impact water tank 105 is supported by the four support feet 107.

[0030] As Figure 1 shown, an observation window 400 is installed outside the upper adsorption purification box 100. Through the setting of the observation window 400, the inside of the swirl air inlet chamber 108, the upper adsorption purification box 100, and the lower impact water tank 105 can be observed. The technical solutions in the embodiments of the present application at least have the following technical effects or advantages: Through the dual effects of the centrifugal separation of the row-connected swirl pipes 201 and the water impact of the lower impact water tank 105, the dust particles in the dust-containing gas can be effectively removed. The structural design of multiple row-connected swirl pipes 201 in parallel enables the dust collector to have a relatively small volume and a small floor area when dealing with a large gas volume, facilitating installation and use in various industrial sites. The present invention uses water as the dust removal medium, eliminating the need for expensive filter materials or complex electrostatic equipment, resulting in low operating costs. At the same time, due to the high dust removal efficiency, the cost of subsequent waste gas treatment is reduced, and it is easy to maintain: The structure is simple, without complex vulnerable parts. The daily maintenance mainly involves regularly cleaning the sewage outlet and checking the water level control system, with a small maintenance workload and low maintenance costs.

[0031] The above are only the preferred embodiments of the present invention and are not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and variations. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.

Claims

1. A novel high-efficiency dust collector, comprising an upper adsorption purification box (100), a cyclone air inlet bin (108) and a lower impact water tank (105), wherein the upper adsorption purification box (100) is connected to the upper part of the cyclone air inlet bin (108), and the lower impact water tank (105) is connected to the lower part of the cyclone air inlet bin (108), characterized in that: A cyclone (103) is installed outside the cyclone air inlet bin (108), and the external dust-carrying gas is connected to the air inlet of the cyclone (103). The cyclone (103) is connected to a spray pipe (104), and the water outlet end of the spray pipe (104) passes through the outer wall of the cyclone (103). A baffle plate (109) is fixedly connected inside the cyclone air inlet bin (108), and the baffle plate (109) is located above the air outlet of the cyclone (103). A cyclone water body dust removal structure is installed inside the cyclone air inlet bin (108), and dust removal water is stored inside the lower impact water tank (105), and the lower end of the cyclone water body dust removal structure is inserted into the dust removal water.

2. A novel high-efficiency dust collector according to claim 1, characterized in that: The cyclone dust removal structure comprises a manifold wind box (200), the manifold wind box (200) being installed inside the cyclone air inlet bin (108), a row of cyclone tubes (201) being installed below the manifold wind box (200), and the lower air outlets of the row of cyclone tubes (201) being inserted into the dust removal water.

3. A novel high-efficiency dust collector according to claim 1, characterized in that: A spray water inlet pipe (202) is installed inside the lower impact water tank (105), and a plurality of spray holes are opened outside the spray water inlet pipe (202).

4. A novel high-efficiency dust collector according to claim 3, characterized in that: The interior of the lower impact water tank (105) is connected to an overflow pipe (203), the water outlet of the overflow pipe (203) penetrates the outer wall of the lower impact water tank (105), and the water inlet of the overflow pipe (203) is located higher than the spray water inlet pipe (202).

5. A novel high-efficiency dust collector according to claim 1, characterized in that: The bottom of the lower impact water tank (105) is connected to an electric sewage valve (106).

6. A novel high-efficiency dust collector according to claim 5, characterized in that: A liquid level meter (300) is installed on the electric sewage valve (106).

7. A novel high-efficiency dust collector according to claim 1, characterized in that: A demister (500) is installed inside the upper adsorption purification box (100).

8. A novel high-efficiency dust collector according to claim 1, characterized in that: The outside of the upper adsorption purification box (100) is connected to a purification air outlet pipe (101), and one end of the purification air outlet pipe (101) away from the upper adsorption purification box (100) is connected to a negative pressure fan (102).

9. A novel high-efficiency dust collector according to claim 1, characterized in that: An observation window (400) is installed on the outside of the upper adsorption purification box (100).

10. A novel high-efficiency dust collector according to claim 1, characterized in that: Four supporting legs (107) are installed outside the lower impact water box (105).