CN209985213U - Pipeline formula photodissociation catalytic oxidation clarifier - Google Patents

Pipeline formula photodissociation catalytic oxidation clarifier Download PDF

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Publication number
CN209985213U
CN209985213U CN201920699688.5U CN201920699688U CN209985213U CN 209985213 U CN209985213 U CN 209985213U CN 201920699688 U CN201920699688 U CN 201920699688U CN 209985213 U CN209985213 U CN 209985213U
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pipeline
air inlet
air
ultraviolet lamp
purification unit
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CN201920699688.5U
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Chinese (zh)
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付宁
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Hebei Runde Environmental Engineering Co Ltd
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Hebei Runde Environmental Engineering Co Ltd
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Abstract

The utility model discloses a pipeline type photolysis catalytic oxidation purifier, which comprises a body, a plurality of purification units arranged in the body, and a re-purification unit arranged at the air outlet of the body; a pipeline is arranged in the body, one end of the pipeline is an air inlet, and the other end of the pipeline is an air outlet; an air quantity monitoring assembly is installed at the air inlet of the pipeline and can monitor the air inlet quantity of the air inlet in real time. The utility model discloses simple structure, reasonable in design utilizes above-mentioned structure can realize quick exhaust purification to utilize amount of wind monitor control to purify the work quantity of unit, realize the work under the different work condition.

Description

Pipeline formula photodissociation catalytic oxidation clarifier
Technical Field
The utility model relates to a waste gas purification device, specific pipeline formula photodissociation catalytic oxidation clarifier that utilizes UV ultraviolet ray and titanium dioxide photocatalyst cooperation to accomplish waste gas purification that says so.
Background
With the requirement of the country for environmental governance, certain requirements are imposed on the production and living waste gases of various industries, and a lot of waste gases are not allowed to be directly discharged into the atmosphere without being treated.
At present, the common methods for treating organic waste gas include adsorption method, absorption method, catalytic combustion method, biological treatment method, etc. Activated carbon adsorption is the immobilization of pollutants from the gas phase to itself and does not address elimination. When a plurality of gaseous pollutants coexist, the adsorption capacity of the activated carbon is reduced. Meanwhile, the activated carbon with saturated adsorption is abandoned and directly burnt or buried, so that resource waste is caused. Secondly, the regeneration is recycled, but the regeneration has some problems, such as a certain reduction of adsorption capacity after regeneration, excessive loss of a correction part in the regeneration process, secondary pollution of regeneration tail gas and the like.
The absorption method is physical transfer or chemical transfer of pollutants from gas phase to liquid phase, the gaseous pollutant liquid phase spraying is better for high-concentration organic waste gas or organic waste gas with large air quantity and low concentration, and the treatment efficiency for organic waste gas with low concentration and low air quantity needs to be further improved.
The catalytic combustion method is rigorous for selecting certain gas pollutant catalysts, and high temperature, high altitude and high steam partial pressure are required, so that the selected catalysts have high activity, high thermal stability, high hydrothermal stability and certain poisoning resistance. The method has strict requirements on process conditions, does not allow the waste gas to contain dust particles and fog drops which influence the service life and the treatment efficiency of the catalyst, and does not allow substances poisoned by the catalyst to prevent the catalyst from being poisoned.
The biological treatment method has selectivity, microorganisms have slow degradation speed to organic pollutants such as Phthalate Substances (PAEs), benzene substances and the like, mainly because molecules of polymers and compounds can resist biological degradation, and enzymes necessary for the microorganisms cannot approach and destroy sensitive reactions in the molecules of the compounds, so that the application of the biological method in the aspect of treating the gaseous substances is limited.
The treatment modes all have various obvious defects and cannot well meet the requirements of actual production and use.
In conclusion, the industry is in need of a waste gas purification device with low use cost, good effect and strong sustainability.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome the not enough that prior art exists, provide an utilize UV ultraviolet ray and titanium dioxide photocatalyst cooperation to accomplish exhaust purification's pipeline formula photodissociation catalytic oxidation clarifier.
In order to achieve the above object, the utility model adopts the following technical scheme: a pipeline type photolysis catalytic oxidation purifier comprises a body and a plurality of purification units arranged in the body; a pipeline is arranged in the body, one end of the pipeline is an air inlet, and the other end of the pipeline is an air outlet; an air quantity monitoring assembly is installed at an air inlet of the pipeline and can monitor the air inlet quantity of the air inlet in real time; a re-purification unit is arranged at the air outlet of the pipeline; the outer wall surface of the body is provided with a controller, the controller is connected with the air volume monitoring assembly through a cable, and monitoring data of the air volume monitoring assembly can be acquired through the cable; the purification unit is arranged in the pipeline; the purification unit comprises a UV ultraviolet lamp tube group and a titanium dioxide photocatalyst filter screen group; the UV ultraviolet lamp tube group comprises an annular lamp holder and a plurality of UV ultraviolet lamp tubes arranged on the annular lamp holder; the titanium dioxide photocatalyst filter screen group comprises three titanium dioxide photocatalyst filter screens which are mutually clamped together; the meshes of the second titanium dioxide photocatalyst filter screen are rhombic; the re-purification unit comprises at least 2 activated carbon filter screens which are close to each other; the controller is connected with and matched with the UV ultraviolet lamp tube group in the purification unit and used for controlling the work of the UV ultraviolet lamp tube group.
The utility model discloses during the implementation, whether utilize amount of wind monitoring subassembly monitoring pipeline air intake department to have waste gas to get into, the entering volume of monitoring waste gas simultaneously, the UV ultraviolet lamp nest of tubes in one or more purification unit is opened in the controller control, utilizes UV ultraviolet ray cooperation titanium dioxide photocatalyst to realize exhaust-gas purification.
The utility model discloses simple structure, reasonable in design utilizes above-mentioned structure can realize quick exhaust purification to utilize amount of wind monitor control to purify the work quantity of unit, realize the work under the different work condition.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic structural diagram of the UV ultraviolet lamp tube set of the present invention.
Detailed Description
In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like, indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are used merely for convenience of description and for simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention. Furthermore, the terms "first", "second", etc. are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first," "second," etc. may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless otherwise specified.
In the description of the present invention, it should be noted that unless otherwise explicitly stated or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may include, for example, a fixed connection, a detachable connection, an integral connection, a mechanical connection, an electrical connection, a direct connection, an indirect connection via an intermediate medium, and a connection between two elements. The specific meaning of the above terms in the present invention can be understood by those of ordinary skill in the art through specific situations.
For the convenience of further understanding, the present invention will be further explained by referring to the embodiments shown in the drawings.
Example (b):
as shown in fig. 1, the utility model comprises a body 1 and a plurality of purification units installed in the body; a pipeline 5 is arranged in the body 1, one end of the pipeline 5 is an air inlet 2, and the other end of the pipeline 5 is an air outlet 3; a re-purification unit 12 is arranged at the air outlet of the pipeline; an air quantity monitoring assembly 6 is installed at an air inlet of the pipeline, and the air quantity monitoring assembly 6 can monitor the air inlet quantity of the air inlet in real time; a controller 7 is installed on the outer wall surface of the body 1, the controller 7 is connected with the air volume monitoring assembly 6 through a cable, and monitoring data of the air volume monitoring assembly 6 can be acquired through the cable; the purification unit is installed in the pipeline 5; the purification unit comprises a UV ultraviolet lamp tube group 8 and a titanium dioxide photocatalyst filter screen group 9; the UV ultraviolet lamp tube group 8 comprises an annular lamp holder 10 and a plurality of UV ultraviolet lamp tubes 11 arranged on the annular lamp holder 10; the titanium dioxide photocatalyst filter screen group 9 comprises three titanium dioxide photocatalyst filter screens which are mutually clamped together; the meshes of the second titanium dioxide photocatalyst filter screen are rhombic; the re-purification unit 12 comprises at least 2 activated carbon filter screens which are close to each other; the controller 7 is coupled to and cooperates with the UV ultraviolet lamp tube group 8 in the purification unit 2 to control the operation of the UV ultraviolet lamp tube group 8.
The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (1)

1. The utility model provides a pipeline formula photodissociation catalytic oxidation clarifier which characterized in that: comprises a body, a plurality of purification units arranged in the body and a re-purification unit arranged at an air outlet of the body; a pipeline is arranged in the body, one end of the pipeline is an air inlet, and the other end of the pipeline is an air outlet; an air quantity monitoring assembly is installed at an air inlet of the pipeline and can monitor the air inlet quantity of the air inlet in real time; the outer wall surface of the body is provided with a controller, the controller is connected with the air volume monitoring assembly through a cable, and monitoring data of the air volume monitoring assembly can be acquired through the cable; the purification unit is arranged in the pipeline; the purification unit comprises a UV ultraviolet lamp tube group and a titanium dioxide photocatalyst filter screen group; the UV ultraviolet lamp tube group comprises an annular lamp holder and a plurality of UV ultraviolet lamp tubes arranged on the annular lamp holder; the titanium dioxide photocatalyst filter screen group comprises three titanium dioxide photocatalyst filter screens which are mutually clamped together; the meshes of the second titanium dioxide photocatalyst filter screen are rhombic; the re-purification unit comprises at least 2 activated carbon filter screens which are close to each other; the controller is connected with and matched with the UV ultraviolet lamp tube group in the purification unit and used for controlling the work of the UV ultraviolet lamp tube group.
CN201920699688.5U 2019-05-16 2019-05-16 Pipeline formula photodissociation catalytic oxidation clarifier Active CN209985213U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920699688.5U CN209985213U (en) 2019-05-16 2019-05-16 Pipeline formula photodissociation catalytic oxidation clarifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920699688.5U CN209985213U (en) 2019-05-16 2019-05-16 Pipeline formula photodissociation catalytic oxidation clarifier

Publications (1)

Publication Number Publication Date
CN209985213U true CN209985213U (en) 2020-01-24

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201920699688.5U Active CN209985213U (en) 2019-05-16 2019-05-16 Pipeline formula photodissociation catalytic oxidation clarifier

Country Status (1)

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CN (1) CN209985213U (en)

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