CN211536998U - A water film deduster for betaine crystallization pollutant - Google Patents

Abstract

The utility model relates to a water film dust collector for betaine crystallization pollutants; the method is characterized in that: the device comprises a tank body, a power device, a water flowing plate which is arranged in the tank body in a staggered manner from top to bottom, an exhaust device arranged at the outlet end of the tank body, a spraying device for spraying pure water, a blowing device for blowing pollutants into the tank body and a water pumping device for feeding the pure water in the tank body into the spraying device; the power device respectively drives the blowing device and the pumping device; the spraying device is arranged in the tank body and is positioned between the water flowing plate and the exhaust device. The problem of the pure water that current scheme caused and the unable abundant contact pollutant of pollutant can't get rid of totally, will mix with the pure water of pollutant discharge together can't utilize the pure water and the shower nozzle produces water smoke when spraying the pure water and the water smoke mixes with the pollutant and can pollute all ring edge borders etc is solved.

Description

A water-film dust collector for betaine crystalline pollutants

technical field

The utility model relates to a water-film dust collector, in particular to a water-film dust collector for betaine crystallization pollutants.

Background technique

Generally, betaine is an alkaloid with strong hygroscopic properties, so an anti-caking agent is often used in the production process. Its molecular structure and application effect have no obvious difference with natural betaine, which belongs to the equivalent of chemically synthesized natural products. At present, betaine is widely used in the fields of food processing, medicine, daily chemical industry and feed. Betaine will produce pollutants in the production process, and the direct discharge of pollutants will pollute the surrounding environment. However, the existing equipment cannot purify the pollutants and still pollutes the environment. How to solve this problem becomes crucial.

In the existing solution, a nozzle is used to spray pure water, and the pure water collects the pollutants. Such a scheme has the following problems: (1) the pure water cannot be fully contacted with the pollutants, and the pollutants cannot be removed cleanly; (2) the pure water mixed with pollutants is discharged together, and the pure water cannot be used; (3) the nozzle sprays When pure water is used, water mist is generated, and the contaminants in the water mist will pollute the surrounding environment.

Utility model content

Aiming at the deficiencies of the prior art, the utility model discloses a water film dust collector for betaine crystallization pollutants, so as to solve the problem that the pure water and the pollutants cannot fully contact the pollutants in the prior art, the pollutants cannot be removed cleanly, and the inclusions are polluted. The pure water of the material is discharged together, and the pure water cannot be used, and the water mist is generated when the nozzle sprays the pure water, and the water mist mixed with pollutants will pollute the surrounding environment and other problems.

The technical scheme adopted by the present utility model is as follows:

A water-film dust collector for betaine crystalline pollutants;

It includes a tank body, a power unit, a flow plate staggered in the tank body from top to bottom, an exhaust device arranged at the outlet end of the tank body, a spray device for spraying pure water, and blowing pollutants into the tank. A blowing device in the body and a water pumping device for sending pure water in the tank into the spraying device; a power device drives the blowing device and the water pumping device respectively; the spraying device is arranged in the tank, and the spraying device The shower device is located between the flow plate and the exhaust device.

A further technical solution is: the tank body is provided with a discharge device for discharging pollutants; the discharge device includes a first discharge valve, a second discharge valve and a material storage pipeline connected to the bottom of the tank body; the first discharge valve The second discharge valve is arranged at one end of the material storage pipeline close to the tank body; the second discharge valve is arranged at the end of the material storage pipeline away from the tank body.

A further technical solution is as follows: the exhaust device includes an exhaust device, a cone net and a cone groove frame arranged outside the cone net; the exhaust device is arranged on the upper end of the cone net.

A further technical solution is: the spray device includes a spray pipe embedded in the tank body and a rotary spray head for spraying the pure water; the rotary spray head is arranged at one end of the spray pipe embedded in the tank body.

A further technical solution is as follows: the blowing device is connected to the position of the bottom of the tank close to the flow plate; the blowing device is connected to the driving end of the power device through a belt.

A further technical solution is: the water inlet of the water pumping device is connected to the bottom of the tank body; the water outlet of the water pumping device is connected to the spray device through a conveying pipe; the water pumping device is connected to the power device through a belt. drive end.

A further technical solution is: the driving end of the power device is coaxially provided with a first transmission wheel and a second transmission wheel; the first transmission wheel is connected to the blowing device by a belt; the second transmission wheel is connected by a belt the pumping device.

The beneficial effects of the utility model are as follows: The utility model designs a water-film dust collector for betaine crystallization pollutants, which uses pure water flowing on a running water plate to filter the pollutants. Use a drain to avoid draining pure water. The water film dust collector used for betaine crystallization pollutants brings the following effects: (1) the pollutants are filtered by flowing pure water on the flow plate, and the pollutants can be removed; (2) the discharge device is used to avoid the pure water The water is discharged, which is beneficial to the collection of pollutants; (3) the pure water is recycled by the pumping device, which saves water resources; (4) the water mist is collected by the exhaust device, so as to avoid the pollution of the surrounding environment by the water mist mixed with pollutants ; (5) The blowing device and the water pumping device share the power device, and the kinetic energy generated by the power device is rationally utilized, thereby reducing the manufacturing cost.

Description of drawings

Figure 1 is a schematic structural diagram of the utility model.

Fig. 2 is the driving schematic diagram of the power device of the present invention.

In the figure: 1, tank body; 2, flow plate; 3, exhaust device; 31, exhaust device; 32, cone net; 33, cone groove frame; 4, spray device; 41, spray pipe; 42, Rotary nozzle; 5. Air blowing device; 6. Water pumping device; 61. Conveying pipeline; 7. Power device; 71. First transmission wheel; 72. Second transmission wheel; 8. Exhaust device; 81. Material storage pipeline; 82, The first drain valve; 83, the second drain valve.

Detailed ways

The specific implementation of this embodiment will be described below with reference to the accompanying drawings.

Figure 1 is a schematic structural diagram of the utility model. Fig. 2 is the driving schematic diagram of the power device of the present invention. 1 and 2, the utility model discloses a water film dust collector for betaine crystal pollutants. The direction of X in the figure is the upper end of the structural schematic diagram of the present invention, and the direction of Y in the figure is the right end of the structural schematic diagram of the present invention. The water film dust collector for betaine crystallization pollutants includes a tank body 1, a power device 7, a flow plate 2 arranged in a staggered manner in the tank body 1 from top to bottom, an exhaust device 3 arranged at the outlet end of the tank body 1, a spray A spray device 4 for pure water, a blower device 5 for blowing pollutants into the tank body 1 , and a water pumping device 6 for sending pure water in the tank body 1 into the spray device 4 . The power device 7 drives the blowing device 5 and the water pumping device 6 respectively. The spray device 4 is arranged in the tank body 1 , and the spray device 4 is located between the flow plate 2 and the exhaust device 3 .

The tank body 1 is arranged vertically. The interior of the tank body 1 is a hollow structure.

The exhaust device 3 includes an exhaust device 31 , a cone mesh 32 and a cone groove frame 33 arranged outside the cone mesh 32 . The exhaust device 31 is arranged on the upper end of the cone mesh 32 .

The cone net 32 is a trapezoid extending outward from bottom to top. The tapered groove frame 33 is a trapezoid extending outward from bottom to top. The tapered groove frame 33 is arranged on the outer side of the tapered mesh 32 . When the spray device 4 sprays pure water, water mist will be generated, and the water mist and gas will be discharged through the outlet end of the tank body 1 . The exhaust device 3 can recover the water mist. The cone net 32 collects the water mist, and the water mist gathers into water droplets and falls along the cone groove frame 33 . The discharge of pollutants mixed in the water mist is also avoided by collecting the water mist.

Preferably, the exhaust device 31 is a fan. The exhaust device 31 is arranged on the upper end of the tank body 1 . The discharge of water mist and gas is accelerated by the exhaust air device 31 .

The exhaust device 31 is a fan, and the selection of the fan model belongs to common knowledge. Those skilled in the art can choose according to the working conditions of the device, for example, the fan of the model HY-380 can be selected.

The spray device 4 includes a spray pipe 41 embedded in the tank body 1 and a rotary spray head 42 for spraying pure water. The rotating spray head 42 is arranged at one end of the spray pipe 41 embedded in the tank body 1 .

The left end of the spray pipe 41 is embedded in the upper end of the tank body 1 . The left end of the spray pipe 41 is provided with a rotating spray head 42 . The pure water in the spray pipe 41 is sprayed out by the rotating nozzle 42 , and the pure water falls on the upper surface of the flow plate 2 . A part of the pure water sprayed by the rotary spray head 42 is discharged from the tank body 1 through the exhaust device 3 in the form of water mist.

Preferably, there are multiple flow plates 2 . The outer end of the flow plate 2 is connected to the inner surface of the tank body 1 . Since the flow plates 2 are staggered from top to bottom, pure water flows from top to bottom along the upper surface of the flow plates 2 .

The blowing device 5 communicates with the position of the bottom of the tank body 1 close to the flow plate 2 . The blower 5 is connected to the drive end of the power unit 7 through a belt.

Preferably, the blowing device 5 is a hair dryer. The pollutants enter the tank body 1 through the blowing device 5 . The pollutants enter the air blowing device 5 from the air inlet of the air blowing device 5 and then enter the tank body 1 from the air outlet of the air blowing device 5 . The air outlet of the blowing device 5 communicates with the bottom of the tank body 1 . The blowing device 5 generates gas to blow the pollutants into the tank body 1 .

The gas drives the pollutants to move from bottom to top along the tank body 1 . When the gas drives the pollutants to move, the gas drives the pollutants to pass through the pure water flowing down on the flow plate 2 . The pure water adsorbs the pollutants in the gas, the pure water drives the pollutants to flow downward, and the pure water and the pollutants accumulate at the bottom of the tank body 1 . The gas flows to the upper end of the tank body 1 and is discharged through the exhaust device 3 .

The pollutants in the gas can be completely removed by pure water, so that the discharged gas will not pollute the surrounding environment.

The blowing device 5 is a blower, and the selection of the blower model belongs to common knowledge. Those skilled in the art can choose according to the working conditions of the device, for example, a hair dryer with a model of CF2A-0.37KW can be selected.

The water inlet of the water pumping device 6 is connected to the bottom of the tank body 1 ; the water outlet of the water pumping device 6 is connected to the spray device 4 through the conveying pipe 61 . The water pumping device 6 is connected to the driving end of the power device 7 through a belt.

Preferably, the water pumping device 6 is a water pump. The conveying pipe 61 is arranged vertically. The lower end of the conveying pipe 61 is connected to the water outlet of the water pumping device 6 . The upper end of the conveying pipe 61 communicates with the right end of the spray pipe 41 .

Pure water and contaminants accumulate at the bottom inside the tank 1 . Contaminants accumulate in the lower end of pure water. The water pumping device 6 flows the pure water at the inner bottom of the tank body 1 into the spraying device 4 . The pure water at the bottom of the tank 1 enters the water pumping device 6 through the water inlet of the water pumping device 6 .

The pure water at the inner bottom of the tank body 1 can be extracted by the water pumping device 6, thereby realizing the recycling of the pure water. The water pumping device 6 can save water resources and reduce the cost of treating pollutants.

The water pumping device 6 is a water pump, and the selection of the model of the water pump belongs to common knowledge. Those skilled in the art can choose according to the working conditions of the device, for example, the water pump of the model PB-H169EAH can be selected.

A first transmission wheel 71 and a second transmission wheel 72 are coaxially disposed at the driving end of the power device 7 . The first transmission wheel 71 is connected to the blowing device 5 through a belt. The second transmission wheel 72 is connected to the water pumping device 6 through a belt.

Preferably, the power device 7 is an electric motor. The blowing device 5 and the water pumping device 6 are arranged in parallel. The driving end of the power device 7 drives the blowing device 5 and the water pumping device 6 at the same time. The driving end of the power device 7 drives the first transmission wheel 71 to rotate and the second transmission wheel 72 to rotate. The rotation of the first transmission wheel 71 drives the blowing device 5 . The rotation of the second transmission wheel 72 drives the water pumping device 6 . By replacing the first transmission wheel 71 with different sizes, the power of the blowing device 5 can be adjusted. By replacing the second transmission wheel 72 with different sizes, the power of the water pumping device 6 can be adjusted.

The blowing device 5 and the water pumping device 6 are driven by the same power device 7, and the power generated by the power device 7 can be used reasonably. Reduced manufacturing cost of water film precipitators for betaine crystalline contaminants.

The tank 1 is provided with a discharge device 8 for discharging pollutants. The drain device 8 includes a first drain valve 82 , a second drain valve 83 and a material storage pipeline 81 communicating with the bottom of the tank body 1 . The first discharge valve 82 is disposed at one end of the material storage pipeline 81 close to the tank body 1 . The second drain valve 83 is disposed at one end of the material storage pipeline 81 away from the tank body 1 .

Preferably, the first drain valve 82 is an electric ball valve. Preferably, the second drain valve 83 is an electric ball valve. The drainage device 8 is arranged at the bottom of the tank body 1 . The first drain valve 82 is disposed at the upper end of the material storage pipe 81 . The second drain valve 83 is disposed at the lower end of the material storage pipe 81 . The upper end of the first drain valve 82 is connected to the bottom of the tank body 1 . The lower end of the first drain valve 82 is connected to the upper end of the material storage pipe 81 . The lower end of the material storage pipe 81 is connected to the upper end of the second drain valve 83 .

When it is necessary to discharge the pollutants into the tank body 1 , the first discharge valve 82 is opened first, and the pollutants enter the material storage pipeline 81 . When the pollutants are accumulated in the material storage pipeline 81 , the first drain valve 82 is closed first, and the pollutants are discharged after the first drain valve 82 is opened.

Since the contaminants accumulate at the lower end of the pure water, the pure water will not enter the material storage pipe 81 when the first drain valve 82 is opened. The pollutants can be effectively discharged through the discharge device 8, and the pure water will not be discharged, and the pure water will not be wasted.

The first drain valve 82 is an electric ball valve, and the selection of the model of the electric ball valve belongs to common knowledge. Those skilled in the art can choose according to the working conditions of the device, for example, the electric ball valve of the model Q941F-16P can be selected.

The second drain valve 83 is an electric ball valve, and the selection of the model of the electric ball valve belongs to common knowledge. Those skilled in the art can choose according to the working conditions of the device, for example, the electric ball valve of the model Q941F-16P can be selected.

In this embodiment, the described air exhaust device 31 is a fan, but it is not limited to this, and may be other air exhaust devices within the scope of its function.

In this embodiment, the described blower 5 is a blower, but it is not limited to this, and may be other blowers within the scope of its function.

In this embodiment, the described water pumping device 6 is a water pump, but it is not limited to this, and may be other water pumping devices within the range that can exert its function.

In this embodiment, the described power plant 7 is a motor, but it is not limited to this, and may be other power plants within the range that can exert its function.

In this embodiment, the described first drain valve 82 is an electric ball valve, but it is not limited to this, and may be other drain valves within the range that can exert its function.

In this embodiment, the described second drain valve 83 is an electric ball valve, but it is not limited to this, and may be other drain valves within the range that can exert its function.

In addition, in this specification, words, such as a "trapezoid", are used, and they are not a precise "trapezoid", but may be in a state of a "substantially trapezoid" within the range where the function can be exhibited.

In addition, in this specification, although the quantity, such as "a plurality of", is used, it is not limited to this, The other quantity within the range which can exhibit the function may be sufficient.

In the description of the embodiments of the present utility model, it should also be noted that, unless otherwise expressly specified and limited, the terms "arrangement" and "connection" should be understood in a broad sense, for example, it may be a fixed connection or a Removable connection, or integral connection; can be mechanical connection, can also be electrical connection; can be directly connected, can also be indirectly connected through an intermediate medium, can be internal communication between two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood in specific situations.

The above description is an explanation of the present utility model, not a limitation of the utility model. For the limited scope of the present utility model, refer to the claims. The present utility model can be modified in any form without violating the basic structure of the present utility model.

Claims (7)

1. a water-film precipitator for betaine crystallization pollutants, is characterized in that: comprise tank body (1), power unit (7), top-down staggered arrangement in described tank body (1) A flow plate (2), an exhaust device (3) arranged at the outlet end of the tank body (1), a spray device (4) for spraying pure water, and a blower for blowing pollutants into the tank body (1) A device (5) and a water pumping device (6) for feeding the pure water in the tank (1) into the spray device (4); a power device (7) drives the blowing device (5) and the water pumping device respectively (6); the spray device (4) is arranged in the tank body (1), and the spray device (4) is located between the flow plate (2) and the exhaust device (3) . 2. The water-film dust collector for betaine crystallization pollutants according to claim 1, characterized in that: the tank body (1) is provided with a discharge device (8) for discharging pollutants; the discharge device (8) comprising a first drain valve (82), a second drain valve (83) and a material storage pipeline (81) communicating with the bottom of the tank body (1); the first drain valve (82) is arranged on the material storage The pipe (81) is close to one end of the tank body (1); the second discharge valve (83) is arranged at the end of the material storage pipe (81) away from the tank body (1). 3. The water-film dust collector for betaine crystallization pollutants according to claim 1, wherein the exhaust device (3) comprises an exhaust device (31), a cone net (32) and a The cone groove frame (33) outside the cone net (32); the air exhaust device (31) is arranged on the upper end of the cone net (32). 4. The water-film dust collector for betaine crystallization pollutants according to claim 1, wherein the spray device (4) comprises a spray pipe (41) embedded in the tank body (1) ) and a rotary spray head (42) for spraying the pure water; the rotary spray head (42) is arranged at one end of the spray pipe (41) embedded in the tank body (1). 5. The water-film dust collector for betaine crystallization pollutants according to claim 1, characterized in that: the blower (5) communicates with the bottom of the tank (1) and is close to the flow plate (2) position; the blowing device (5) is connected to the driving end of the power device (7) through a belt. 6. The water film precipitator for betaine crystallization pollutants according to claim 1, characterized in that: the water inlet of the water pumping device (6) communicates with the bottom of the tank body (1); the water pumping The water outlet of the device (6) is connected to the spray device (4) through a conveying pipe (61); the water pumping device (6) is connected to the driving end of the power device (7) through a belt. 7. The water-film precipitator for betaine crystallization pollutants according to claim 1, characterized in that: the drive end of the power device (7) is coaxially provided with a first transmission wheel (71) and a second A transmission wheel (72); the first transmission wheel (71) is connected to the blowing device (5) through a belt; the second transmission wheel (72) is connected to the water pumping device (6) through a belt.

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