Multi-stage generator oxidation tower capable of controlling efficiency

Abstract

The utility model discloses a multistage generator oxidation tower capable of controlling efficiency, which comprises a bottom plate, an oxidation tower body fixedly arranged at the upper end of the bottom plate, an air inlet fixedly arranged at one side of the oxidation tower body, and an air outlet arranged at the upper end of the oxidation tower body; the flow equalizing assembly is arranged in the oxidation tower body, and dismounting assemblies are arranged at the two ends of the surface of the flow equalizing assembly. According to the utility model, the plurality of groups of spraying assemblies are arranged and are uniformly distributed in the through holes of the flow equalizing assembly, so that the spraying assemblies can reasonably distribute airflow space to ensure that micro-nano bubbles are uniformly distributed in uniform airflow, and the original disordered airflow distribution can be limited at the bottom of the device; the interior of the flow equalizing assembly has a flow equalizing effect, the spraying assembly can be independently controlled, and the generator is arranged in a single channel for independent treatment, so that the advantage that the efficiency can be controlled is achieved.

Description

Technical Field

[0001] The utility model belongs to the technical field of oxidation towers, and in particular relates to a multi-stage generator oxidation tower capable of controlling efficiency. Background Art

[0002] By utilizing the special physical and chemical properties of micro-nano foam, high temperature and high pressure and photoelectric effect are generated at the moment of foam breaking to produce highly oxidizing hydroxyl free radicals, which are used to oxidize the organic molecules in the organic waste gas to decompose and degrade them or even mineralize them into carbon dioxide and water. Due to the oxidation destruction, the physical properties of the sticky particles change and lose their stickiness. This is another use of the oxidation device, which can be used as the main pre-treatment process for waste gas containing sticky particles in the coating industry. This technology is to add a uniform flow structure to the traditional water washing device to improve the airflow distribution mode, exert oxidation in the spatial structure that is most conducive to the distribution of nano foam, and provide sufficient oxidation time. The airflow and nano foam are in reverse contact, and the broken droplets are returned to the bottom of the oxidation device under the action of gravity for recycling.

[0003] However, there are some problems with the existing technology: the oxidation capacity of the existing device has not yet reached the capacity to treat waste gas with a concentration of more than 100 mg, and the equipment is large in size and cost due to the limitation of foam density limit, and still lacks competitive advantage. Because it is in the liquid and gas phase working space, the material is stainless steel, and only single-tube single control is available, the material cost is high, and the capacity is small. Therefore, we propose a multi-stage generator oxidation tower that can control efficiency. Utility Model Content

[0004] In view of the problems existing in the prior art, the purpose of the utility model is to provide a multi-stage generator oxidation tower with controllable efficiency. The oxidizing micro-nano foam water mist can be circulated and pumped into the spray component through the circulation component, so that the spray component can deodorize the gas in the flow equalization component, and by arranging several groups of spray components, several groups of spray components can control the effect of spraying efficiency.

[0005] The utility model is implemented as follows: a multi-stage generator oxidation tower with controllable efficiency comprises:

[0006] A bottom plate, an oxidation tower body is fixedly mounted on the upper end of the bottom plate, an air inlet is fixedly mounted on one side of the oxidation tower body, and an air outlet is opened at the upper end of the oxidation tower body;

[0007] A flow balancing component, the flow balancing component is arranged inside the oxidation tower body, and disassembly components are arranged at both ends of the surface of the flow balancing component;

[0008] A circulation component, wherein the circulation component is arranged on one side of the upper end of the bottom plate, and one end of the circulation component is connected to the oxidation tower body;

[0009] A spray assembly is arranged outside the oxidation tower body, one end of the spray assembly is connected to the circulation assembly, and the other end of the spray assembly passes through the oxidation tower body and is arranged in the flow equalization assembly.

[0010] Optionally, the flow equalizing assembly includes a limit plate and a flow equalizing tube, the limit plate is fixedly installed inside the oxidation tower body, and several groups of flow equalizing tubes are arranged, and several groups of flow equalizing tubes are fixedly installed at the lower end of the limit plate. Several groups of through holes are opened on the surface of the limit plate, and several groups of through holes are connected to the flow equalizing tube.

[0011] Optionally, the disassembly assembly includes a fixture and a clamping plate, the fixture is fixedly mounted on one side of the upper end of the limit plate, the clamping plate is slidably mounted inside the fixture, clamping grooves are provided on both sides of the oxidation tower body, and one end of the clamping plate is arranged in the clamping groove.

[0012] Optionally, two groups of pressure springs are fixedly installed at one end inside the fixer, one end of the two groups of pressure springs are fixedly connected to the clamping plate, and protrusions are formed at both ends of the clamping plate.

[0013] Optionally, the circulation component includes a water tank and an aerosol pump, the water tank is fixedly installed at one end of the oxidation tower body, and the aerosol pump is provided in several groups, and the several groups of aerosol pumps are fixedly installed at one end of the water tank.

[0014] Optionally, the spray assembly includes a first pipe and a second pipe, the first pipe is provided in several groups, and the several groups of the first pipe are fixedly installed on the upper end of the aerosol pump, and the second pipe is provided in three groups, and the three groups of the second pipe are fixedly connected to the first pipe.

[0015] Optionally, a spray head is disposed in each through hole of the limiting plate, a third pipe is fixedly mounted on the upper end of the spray head, and the third pipe is fixedly connected to the second pipe.

[0016] Optionally, support rods are fixedly mounted on both ends of the spray head, and one end of the support rods is fixedly mounted on the inner wall of the through hole of the limiting plate.

[0017] Compared with the prior art, the beneficial effects of the utility model are:

[0018] 1. Through the cooperation of the bottom plate, the oxidation tower body, the air inlet, the air outlet, the flow equalizing component, the disassembly component, the circulation component and the spraying component, the gas can be transported to the bottom layer of the oxidation tower body through the air inlet during use, and the gas will flow into the flow equalizing component after being transported to the bottom layer of the oxidation tower body, and then the oxidizing micro-nano foam water mist in the circulation component can be extracted through the spraying component, so that the flow equalizing component can be sprayed after the spraying component is extracted, so that the gas in the flow equalizing component can be de-sticked, deodorized and purified, so that no auxiliary agents are used and no chemical additives are added, and only oxygen is used as the oxidant.

[0019] 2. Several groups of spray components are set up, and several groups of spray components are distributed in the through holes of the flow equalizing component, so that the spray components can reasonably distribute the airflow space to ensure that the micro-nano bubbles are evenly distributed in the uniform airflow, and the original turbulent airflow distribution can be limited to the bottom of the device. The flow equalizing component has the effect of equalizing the flow, and the spray components can be controlled separately. The generator is built into a single channel and processed independently, so as to achieve controllable efficiency, and can be combined to increase the capacity of the equipment.

[0020] 3. By installing a disassembly component on the flow balancing component, the flow balancing component can be disassembled from the oxidation tower body through the disassembly component, so that the flow balancing component can be easily taken out and replaced.

[0021] Other features and advantages of the present invention will become apparent from the following detailed description of exemplary embodiments of the present invention with reference to the accompanying drawings. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] Figure 1 It is a structural schematic diagram provided by the utility model;

[0023] Figure 2 It is a schematic diagram of a water storage tank provided by the utility model;

[0024] Figure 3 It is a schematic diagram of a sprinkler head provided by the utility model;

[0025] Figure 4 It is a schematic diagram of a fixer provided by the utility model.

[0026] In the figure: 1. bottom plate; 2. oxidation tower body; 3. air inlet; 4. air outlet; 5. flow equalizing assembly; 501. limit plate; 502. flow equalizing tube; 6. disassembly assembly; 601. fixer; 602. clamping plate; 603. pressure spring; 604. bump; 7. circulation assembly; 701. water storage tank; 702. aerosol pump; 8. spray assembly; 801. first pipeline; 802. second pipeline; 803. spray head; 804. third pipeline; 805. support rod. DETAILED DESCRIPTION

[0027] In order to further understand the content, features and effects of the utility model, the following embodiments are given as examples and described in detail with reference to the accompanying drawings.

[0028] Various exemplary embodiments of the present invention will now be described in detail with reference to the accompanying drawings. It should be noted that the relative arrangement of components and steps, numerical expressions and numerical values ​​set forth in these embodiments do not limit the scope of the present invention unless otherwise specifically stated.

[0029] The following description of at least one exemplary embodiment is merely illustrative in nature and is in no way intended to limit the invention, its application, or uses.

[0030] Technologies, methods, and equipment known to ordinary technicians in the relevant art may not be discussed in detail, but where appropriate, the technologies, methods, and equipment should be considered part of the specification.

[0031] In all examples shown and discussed herein, any specific values ​​should be interpreted as merely exemplary and not limiting. Therefore, other examples of the exemplary embodiments may have different values.

[0032] The structure of the utility model is described in detail below in conjunction with the accompanying drawings.

[0033] like Figures 1 to 4 As shown, the utility model embodiment provides a multi-stage generator oxidation tower with controllable efficiency, comprising:

[0034] A bottom plate 1, an oxidation tower body 2 is fixedly installed on the upper end of the bottom plate 1, an air inlet 3 is fixedly installed on one side of the oxidation tower body 2, and an air outlet 4 is opened at the upper end of the oxidation tower body 2;

[0035] A flow balancing component 5, which is arranged inside the oxidation tower body 2, and disassembly components 6 are arranged at both ends of the surface of the flow balancing component 5;

[0036] A circulation component 7, which is arranged on one side of the upper end of the bottom plate 1, and one end of the circulation component 7 is connected to the oxidation tower body 2;

[0037] A spray assembly 8 is arranged outside the oxidation tower body 2 , one end of the spray assembly 8 is connected to the circulation assembly 7 , and the other end of the spray assembly 8 passes through the oxidation tower body 2 and is arranged in the flow equalization assembly 5 .

[0038] The gas can be transported to the bottom layer of the oxidation tower body 2 through the air inlet 3, and after being transported to the bottom layer of the oxidation tower body 2, the gas will flow into the flow equalizing component 5, and then the oxidizing micro-nano foam water mist in the circulation component 7 can be extracted through the spraying component 8, so that the flow equalizing component 5 can be sprayed after the spraying component 8 is extracted, so that the gas in the flow equalizing component 5 can be de-sticked, deodorized and purified, so that no auxiliary agents are used and no chemical additives are added, and only oxygen is used as the oxidant.

[0039] Furthermore, several groups of spray components 8 are set, and the several groups of spray components 8 are distributed in the through holes of the flow equalizing component 5, so that the spray components 8 can reasonably distribute the airflow space to ensure that the micro-nano bubbles are evenly distributed in the uniform airflow, and the original turbulent airflow distribution can be limited to the bottom of the device. The flow equalizing component 5 has the effect of equalizing the flow, and the spray components 8 can be controlled separately, and the generator is built into a single channel and processed independently, so as to achieve controllable efficiency, and can be combined to increase the capacity of the equipment.

[0040] Furthermore, by installing the disassembly component 6 on the flow balancing component 5, the flow balancing component 5 can be disassembled from the oxidation tower body 2 through the disassembly component 6, so that the flow balancing component 5 can be easily taken out and replaced.

[0041] Specifically, the flow equalizing component 5 includes a limiting plate 501 and a flow equalizing tube 502. The limiting plate 501 is fixedly installed inside the oxidation tower body 2. The flow equalizing tube 502 is provided in several groups. The several groups of flow equalizing tubes 502 are all fixedly installed at the lower end of the limiting plate 501. Several groups of through holes are opened on the surface of the limiting plate 501, and the several groups of through holes are connected to the flow equalizing tube 502.

[0042] The limiting plate 501 and the flow equalizing tube 502 are installed in the lower layer inside the oxidation tower body 2, so that when the gas enters the lower layer inside the oxidation tower body 2, the gas will flow into the flow equalizing tube 502, and then the oxidizing micro-nano foam water mist will be sprayed in the through hole of the limiting plate 501 through the spraying component 8, so that the oxidizing micro-nano foam water mist can deodorize and purify the gas in the flow equalizing tube 502, and the purified gas can flow out from the air outlet 4 through the flow equalizing tube 502.

[0043] Specifically, the disassembly component 6 includes a fixture 601 and a clamping plate 602. The fixture 601 is fixedly installed on one side of the upper end of the limit plate 501. The clamping plate 602 is slidably installed inside the fixture 601. Clamping grooves are provided on both sides of the oxidation tower body 2. One end of the clamping plate 602 is arranged in the clamping groove. Two groups of pressure springs 603 are fixedly installed at one end inside the fixture 601. One end of the two groups of pressure springs 603 is fixedly connected to the clamping plate 602. Both ends of the clamping plate 602 are formed with protrusions 604.

[0044] Installers are fixedly installed on both sides of the upper end of the limit plate 501, so that the pressure spring 603 in the installer can push the clamping plate 602, so that the clamping plate 602 can be clamped in the clamping groove inside the oxidation tower body 2, thereby achieving the effect of facilitating the installation or removal of the limit plate 501 and the flow equalizing tube 502, and the protrusion 604 is driven by the movement of the clamping plate 602, so that the protrusion 604 moves to a certain position and can be limited in the fixer 601, thereby achieving the effect of limiting when the clamping plate 602 is clamped.

[0045] Specifically, the circulation component 7 includes a water tank 701 and an aerosol pump 702 . The water tank 701 is fixedly installed at one end of the oxidation tower body 2 . The aerosol pump 702 is provided in several groups, and the several groups of aerosol pumps 702 are all fixedly installed at one end of the water tank 701 .

[0046] The water tank 701 is connected to the oxidation tower body 2, so that the oxidizing micro-nano foam water mist sprayed on the bottom of the oxidation tower body 2 can flow into the water tank 701, and then the oxidizing micro-nano foam water mist is pumped into the spraying component 8 through the aerosol pump 702, so that the device can achieve the effect of recycling the oxidizing micro-nano foam water mist through the aerosol pump 702.

[0047] Specifically, the spray assembly 8 includes a first pipe 801 and a second pipe 802. The first pipe 801 is provided with several groups, and the several groups of first pipes 801 are fixedly installed on the upper end of the aerosol pump 702. The second pipe 802 is provided with three groups, and the three groups of second pipes 802 are fixedly connected to the first pipe 801. A spray head 803 is provided in the through hole of the limiting plate 501, and a third pipe 804 is fixedly installed on the upper end of the spray head 803. The third pipe 804 is fixedly connected to the second pipe 802. Support rods 805 are fixedly installed at both ends of the spray head 803, and one end of the support rod 805 is fixedly installed on the inner wall of the through hole of the limiting plate 501.

[0048] The oxidizing micro-nano foam water mist is pumped into the first pipe 801 through the aerosol pump 702, and the oxidizing micro-nano foam water mist in the first pipe 801 can flow into the second pipe 802 and the third pipe 804, and then the oxidizing micro-nano foam water mist is sprayed in the equalizing flow pipe 502 through the spray head 803, so that the oxidizing micro-nano foam water mist can deodorize the gas in the equalizing flow pipe 502, and the spray head 803 is arranged in several groups, and the several groups are distributed in the through holes of the limiting plate 501, so that the several groups of spray barrels can be controlled separately, and the generator is built into a single channel and processed independently, so as to achieve the effect of controlling efficiency, and the spray head 803 can be limited in the through hole of the limiting plate 501 by the support rod 805.

[0049] Working principle: The water tank 701 is connected with the oxidation tower body 2, so that the oxidation micro-nano foam water mist sprayed on the bottom of the oxidation tower body 2 can flow into the water tank 701, and then the oxidation micro-nano foam water mist is pumped into the spraying assembly 8 through the aerosol pump 702, so that the device can achieve the effect of recycling the oxidation micro-nano foam water mist through the aerosol pump 702, and then the oxidation micro-nano foam water mist is pumped into the first pipe 801 through the aerosol pump 702, and the oxidation micro-nano foam water mist in the first pipe 801 can flow into the second pipe 802 and In the third pipe 804, the oxidized micro-nano foam water mist is sprayed into the equalizing flow tube 502 through the spray head 803, so that the oxidized micro-nano foam water mist can deodorize the gas in the equalizing flow tube 502, and several groups of spray heads 803 are arranged, and the several groups are distributed in the through holes of the limiting plate 501, so that several groups of spray barrels can be controlled separately, and the generator is built into a single channel and processed independently, so as to achieve the effect of controlling efficiency, and the spray head 803 can be limited in the through hole of the limiting plate 501 by the support rod 805.

[0050] It should be noted that, in this article, relational terms such as first and second, etc. are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Moreover, the terms "include", "comprise" or any other variants thereof are intended to cover non-exclusive inclusion, so that a process, method, article or device including a series of elements includes not only those elements, but also other elements not explicitly listed, or also includes elements inherent to such process, method, article or device.

[0051] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A multi-stage generator oxidation tower with controllable efficiency, characterized in that: include: A bottom plate (1), an oxidation tower body (2) is fixedly mounted on the upper end of the bottom plate (1), an air inlet (3) is fixedly mounted on one side of the oxidation tower body (2), and an air outlet (4) is provided at the upper end of the oxidation tower body (2); A flow balancing component (5), the flow balancing component (5) being arranged inside the oxidation tower body (2), and disassembly components (6) being arranged at both ends of the surface of the flow balancing component (5); A circulation component (7), wherein the circulation component (7) is arranged on one side of the upper end of the bottom plate (1), and one end of the circulation component (7) is connected to the oxidation tower body (2); A spray assembly (8), wherein the spray assembly (8) is arranged outside the oxidation tower body (2), one end of the spray assembly (8) is connected to the circulation assembly (7), and the other end of the spray assembly (8) passes through the oxidation tower body (2) and is arranged in the flow equalization assembly (5).

2. A multi-stage generator oxidation tower with controllable efficiency according to claim 1, characterized in that: The flow balancing component (5) comprises a limit plate (501) and a flow balancing tube (502), wherein the limit plate (501) is fixedly mounted inside the oxidation tower body (2), and the flow balancing tube (502) is provided in a plurality of groups, wherein the plurality of groups of flow balancing tubes (502) are fixedly mounted at the lower end of the limit plate (501), and a plurality of groups of through holes are provided on the surface of the limit plate (501), and the plurality of groups of through holes are connected to the flow balancing tube (502).

3. A multi-stage generator oxidation tower with controllable efficiency according to claim 2, characterized in that: The disassembly assembly (6) comprises a fixer (601) and a clamping plate (602), wherein the fixer (601) is fixedly mounted on one side of the upper end of the limiting plate (501), and the clamping plate (602) is slidably mounted inside the fixer (601), and clamping grooves are provided on both sides of the inside of the oxidation tower body (2), and one end of the clamping plate (602) is arranged in the clamping groove.

4. A multi-stage generator oxidation tower capable of controlling efficiency according to claim 3, characterized in that: Two groups of pressure springs (603) are fixedly installed at one end inside the fixer (601), and one end of the two groups of pressure springs (603) is fixedly connected to the clamping plate (602), and protrusions (604) are formed at both ends of the clamping plate (602).

5. The multi-stage generator oxidation tower with controllable efficiency according to claim 1, characterized in that: The circulation component (7) comprises a water storage tank (701) and an aerosol pump (702), wherein the water storage tank (701) is fixedly mounted on one end of the oxidation tower body (2), and the aerosol pump (702) is provided in a plurality of groups, wherein the plurality of groups of aerosol pumps (702) are all fixedly mounted on one end of the water storage tank (701).

6. A multi-stage generator oxidation tower capable of controlling efficiency according to claim 5, characterized in that: The spray assembly (8) comprises a first pipe (801) and a second pipe (802), wherein the first pipe (801) is provided in a plurality of groups, and the plurality of groups of the first pipe (801) are fixedly mounted on the upper end of the aerosol pump (702), and the second pipe (802) is provided in three groups, and the three groups of the second pipe (802) are fixedly connected to the first pipe (801).

7. A multi-stage generator oxidation tower capable of controlling efficiency according to claim 2, characterized in that: A spray head (803) is arranged in each through hole of the limiting plate (501), a third pipe (804) is fixedly installed on the upper end of the spray head (803), and the third pipe (804) is fixedly connected to the second pipe (802).

8. A multi-stage generator oxidation tower capable of controlling efficiency according to claim 7, characterized in that: Support rods (805) are fixedly mounted at both ends of the spray head (803), and one end of the support rod (805) is fixedly mounted on the inner wall of the through hole of the limiting plate (501).

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