CN221141393U - Two-phase FT oxidation equipment - Google Patents
Two-phase FT oxidation equipment Download PDFInfo
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- CN221141393U CN221141393U CN202323213734.1U CN202323213734U CN221141393U CN 221141393 U CN221141393 U CN 221141393U CN 202323213734 U CN202323213734 U CN 202323213734U CN 221141393 U CN221141393 U CN 221141393U
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- oxidation
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- reposition
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- 230000003647 oxidation Effects 0.000 title claims abstract description 87
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 87
- 230000006837 decompression Effects 0.000 claims abstract description 28
- 238000005192 partition Methods 0.000 claims abstract description 12
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 10
- 239000003292 glue Substances 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 238000010030 laminating Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 12
- 238000012423 maintenance Methods 0.000 abstract description 10
- 238000004140 cleaning Methods 0.000 abstract description 5
- 238000007789 sealing Methods 0.000 abstract description 3
- 238000013024 troubleshooting Methods 0.000 abstract description 3
- 239000010865 sewage Substances 0.000 description 12
- 238000006056 electrooxidation reaction Methods 0.000 description 2
- 238000011835 investigation Methods 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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Abstract
The application discloses two-phase FT oxidation equipment, and belongs to the field of electrocatalytic oxidation. This two-phase FT oxidation equipment, including reposition of redundant personnel oxidation subassembly, independent partition mechanism and reposition of redundant personnel decompression mechanism, and the inside distribution of reposition of redundant personnel oxidation subassembly has independent partition mechanism, independent partition mechanism's both sides are connected with reposition of redundant personnel decompression mechanism, independent partition mechanism includes interior tank bracket, interior frid, draw-in groove, electrolysis trough, electrode plate, flexible glue frame and handle frame, and the top of interior tank bracket is provided with interior frid. The two-phase oxidation tank of the oxidation equipment structure is internally combined with the electrolytic tank through the three groups of distributed inner tank frames to form an electrocatalytic oxidation structure, and the electrolytic tank is only required to be pulled out during maintenance, so that the maintenance and troubleshooting process can be performed, the cleaning can be integrally dismantled, the operation is convenient and fast, and the flexible glue frame attached to the inner wall of the electrolytic tank can be kept stable in sealing when being combined with the inner tank plates, so that the oxidation process is convenient to use.
Description
Technical Field
The application relates to the technical field of electrochemical oxidation, in particular to a two-phase FT oxidation device.
Background
The two-phase FT oxidation is to provide electric energy through the two-phase electric access electrolytic tank, the electrochemical oxidation process is to put a solution or suspension of organic matters into the electrolytic tank, the organic matters are oxidized by taking electrons on the anode through direct current, or the low-valence metal is oxidized into high-valence metal ions first, then the high-valence metal ions oxidize the organic matters, in the wastewater treatment, the electron-withdrawing effect of the anode is often utilized to oxidize pollutants in the wastewater without secondary pollution, and the electrocatalytic oxidation equipment is adopted to finish the wastewater purification treatment.
The structure of the product can be referred to the electrocatalytic oxidation device disclosed in China patent document CN 214270326U.
The electrocatalytic oxidation equipment in the structure only carries out cleaning treatment on the positive electrode and the negative electrode inside the equipment electrolytic tank, but the electrode structure is positioned inside the electrolytic tank and only cleans the electrode structure, so that cleaning dirt residues still exist inside the electrolytic tank in the cleaning process, and potential safety hazards exist in long-term use.
There is no two-phase FT oxidation apparatus that can quickly separate the cell cleanup.
Disclosure of utility model
The summary of the application is provided to introduce a selection of concepts in a simplified form that are further described below in the detailed description. The summary of the application is not intended to identify key features or essential features of the claimed subject matter, nor is it intended to be used to limit the scope of the claimed subject matter.
The utility model aims to overcome the defects of the prior art, provides two-phase FT oxidation equipment, realizes a maintenance process capable of being quickly separated and detached by combining three groups of distributed inner groove frames with an electrolytic cell to form an electrocatalytic oxidation structure, and solves the problems that dirt residues remain in the electrolytic cell in the cleaning process of the equipment electrolytic cell and potential safety hazards exist in long-term use.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
This two-phase FT oxidation equipment, including reposition of redundant personnel oxidation subassembly, independent partition mechanism and reposition of redundant personnel decompression mechanism, and the inside distribution of reposition of redundant personnel oxidation subassembly has independent partition mechanism, independent partition mechanism's both sides are connected with reposition of redundant personnel decompression mechanism, independent partition mechanism includes interior tank bracket, interior frid, draw-in groove, electrolysis trough, electrode plate, flexible glue frame and handle frame, and the top of interior tank bracket is provided with interior frid, the inner wall of interior frid is provided with the draw-in groove, and the laminating of the inner wall of draw-in groove has the electrolysis trough, the inside of electrolysis trough is provided with the electrode plate, and is provided with flexible glue frame around the electrode plate, the top of electrolysis trough is provided with the handle frame.
Further, the electrolytic tank forms a buckling structure with the inner groove plate through the clamping groove, and the soft rubber frame is attached along two side edges of the electrolytic tank.
Further, the inner groove frame is fixedly connected with the inner groove plate and the shunt oxidation assembly, and three groups of inner groove frames and inner groove plates are arranged.
Further, the reposition of redundant personnel oxidation subassembly is including advancing pipe, two-phase oxidation case, support, shunt tubes, exit tube and top cap, and advance the both sides of pipe and distribute there is two-phase oxidation case, two-phase oxidation case's bottom is provided with the support, and two-phase oxidation case's both sides distribute there is the shunt tubes, the one end of shunt tubes is connected with the exit tube, and two-phase oxidation case's top is provided with the top cap.
Further, the inlet pipe is communicated with the shunt pipe and the two-phase oxidation box, and the two-phase oxidation box is provided with two groups.
Further, reposition of redundant personnel decompression mechanism includes inner tube, decompression branch pipe, pressure taper hole and water collecting tank, and the bottom of inner tube is connected with the decompression branch pipe, the inside of decompression branch pipe is provided with pressure taper hole, and the bottom of decompression branch pipe is connected with the water collecting tank.
Further, the inner tube is communicated with the split oxidation assembly and the independent splitting mechanism, and the inner tube is connected with the decompression branch tube.
The application has the beneficial effects that: the two-phase FT oxidation equipment is convenient to separate and clean.
The two-phase oxidation tank of the oxidation equipment structure is internally combined with the electrolytic tank through three groups of distributed inner tank frames to form an electrocatalytic oxidation structure, and the electrolytic tank is only required to be pulled out during maintenance and detached, so that in the maintenance and troubleshooting process, the two-phase oxidation tank can be integrally removed and cleaned through targeted single investigation, the operation is convenient and quick, and a flexible rubber frame attached to the inner wall of the electrolytic tank can be kept stable in sealing when combined with the inner tank plates, thereby being convenient for use in the oxidation process;
the structure is characterized in that sewage introduced by the inlet pipe is matched with the shunt pipe to carry out shunt oxidation treatment through the two groups of two-phase oxidation boxes, so that the efficiency is improved, meanwhile, the top end of the two-phase oxidation boxes is provided with a top cover structure, the top cover can be opened to clean and maintain the internal electrolysis bin, the whole structure is stable, and the maintenance and the use are convenient;
The structure is provided with the pressure taper hole made of soft rubber material at the port of the pressure reducing branch pipe, when the pressure is too high during the drainage of the inner pipe, the inner wall of the pressure taper hole is pressed and expanded, and redundant water flows into the water collecting tank through the pressure reducing branch pipe, so that the phenomenon that the pressure is too high and the potential safety hazard exists in the unstable drainage of the inner pipe is avoided.
Drawings
The accompanying drawings, which are included to provide a further understanding of the application, are incorporated in and constitute a part of this specification. The drawings and their description are illustrative of the application and are not to be construed as unduly limiting the application.
In addition, the same or similar reference numerals denote the same or similar elements throughout the drawings. It should be understood that the figures are schematic and that elements and components are not necessarily drawn to scale.
In the drawings:
FIG. 1 is a schematic perspective view of the present application;
FIG. 2 is a schematic perspective view of an independent detaching mechanism according to the present application;
FIG. 3 is a schematic perspective view of an inner frame according to the present application;
FIG. 4 is a schematic perspective view of an electrolytic cell of the present application;
fig. 5 is a schematic side view of the split-flow pressure reducing mechanism of the present application.
Reference numerals:
1. A split oxidation assembly; 101. feeding a pipe; 102. a two-phase oxidation tank; 103. a bracket; 104. a shunt; 105. a pipe outlet; 106. and a top cover.
2. An independent detaching mechanism; 201. an inner tank rack; 202. an inner trough plate; 203. a clamping groove; 204. an electrolytic cell; 205. an electrode plate; 206. a soft rubber frame; 207. a handle frame.
3. A split-flow pressure reducing mechanism; 301. an inner tube; 302. a pressure reducing branch pipe; 303. a pressure taper hole; 304. a water collecting tank.
Detailed Description
Embodiments of the present disclosure will be described in more detail below with reference to the accompanying drawings. While certain embodiments of the present disclosure are shown in the drawings, it should be understood that the present disclosure may be embodied in various forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete. It should be understood that the drawings and embodiments of the present disclosure are for illustration purposes only and are not intended to limit the scope of the present disclosure.
The present disclosure will be described in detail below with reference to the accompanying drawings in conjunction with embodiments.
Referring to fig. 1, this two-phase FT oxidation equipment, including reposition of redundant personnel oxidation subassembly 1, independent disassembly mechanism 2 and reposition of redundant personnel decompression mechanism 3, and reposition of redundant personnel oxidation subassembly 1's inside distributes has independent disassembly mechanism 2, independent disassembly mechanism 2's both sides are connected with reposition of redundant personnel decompression mechanism 3, reposition of redundant personnel oxidation subassembly 1 is including advancing pipe 101, two-phase oxidation case 102, support 103, shunt tubes 104, exit tube 105 and top cap 106, and advance the both sides of pipe 101 to distribute two-phase oxidation case 102, the bottom of two-phase oxidation case 102 is provided with support 103, and two-phase oxidation case 102's both sides distribution has shunt tubes 104, the one end of shunt tubes 104 is connected with exit tube 105, and the top of two-phase oxidation case 102 is provided with top cap 106, advance and be linked together between pipe 101 and shunt tubes 104 and the two-phase oxidation case 102, and two-phase oxidation case 102 is provided with two sets of, in this oxidation equipment use, can be connected sewage and advance pipe 101, introduce shunt tubes 104 through advancing pipe 101, introduce sewage into shunt tubes 104, lead inside through two-phase oxidation case 102 shunt tubes 104 to carry out the electrolytic oxidation process, then, the sewage is discharged 105 through two-phase oxidation case 102 opposite side shunt tubes 104 connection's, and the top cap 106 is advanced through two-phase oxidation case 102, the top cap 106 is advanced to the maintenance structure is opened simultaneously, the top cap is convenient for the maintenance structure is carried out.
Referring to fig. 2 to 4, the split reducing mechanism 3 is connected to both sides of the independent splitting mechanism 2, the independent splitting mechanism 2 includes an inner tank frame 201, an inner tank plate 202, a clamping groove 203, an electrolytic tank 204, an electrode plate 205, a flexible glue frame 206 and a handle frame 207, the top end of the inner tank frame 201 is provided with the inner tank plate 202, the inner wall of the inner tank plate 202 is provided with the clamping groove 203, the inner wall of the clamping groove 203 is attached with the electrolytic tank 204, the inside of the electrolytic tank 204 is provided with the electrode plate 205, the flexible glue frame 206 is provided with the handle frame 207, the electrolytic tank 204 and the inner tank plate 202 form a buckle structure through the clamping groove 203, the flexible glue frame 206 is attached along both side ends of the electrolytic tank 204, the inner tank frame 201 is fixedly connected with the inner tank plate 202 and the split oxidizing assembly 1, and the inner tank frame 201 and the inner tank plate 202 are provided with three groups, after the oxidation equipment is used for a long time, a user can open top covers 106 at two sides of the top end of the two-phase oxidation tank 102, then hold a handle frame 207 to pull the whole electrolytic tank 204 upwards from a clamping groove 203 in an inner tank plate 202, separation of the whole electrolytic tank 204 can be completed, detachment and taking are completed simultaneously, then an operator can replace or maintain and clean the structure of the inside of the electrolytic tank 204 and the electrode plate 205, the whole structure is combined with the electrolytic tank 204 through three groups of distributed inner tank frames 201 to form an electrocatalytic oxidation structure, detachment during maintenance can be completed by only pulling out a single electrolytic tank 204, targeted single investigation can be completed in the maintenance and troubleshooting process, the operation is convenient and quick, and a flexible glue frame 206 attached to the inner wall of the electrolytic tank 204 can be kept stable in sealing when combined with the inner tank plate 202, so that the oxidation process is convenient to use.
Referring to fig. 5, the diversion and decompression mechanism 3 comprises an inner pipe 301, a decompression branch pipe 302, a pressure taper hole 303 and a water collecting tank 304, wherein the bottom end of the inner pipe 301 is connected with the decompression branch pipe 302, the pressure taper hole 303 is arranged in the decompression branch pipe 302, the bottom end of the decompression branch pipe 302 is connected with the water collecting tank 304, the inner pipe 301 is communicated with the diversion oxidation assembly 1 and the independent separation mechanism 2, and the inner pipe 301 is connected with the decompression branch pipe 302, when the sewage is oxidized, the middle inlet pipe 101 enters the sewage, the middle inlet pipe 101 is decompressed and discharged when the sewage pressure is too high, the middle inlet pipe 101 flows into the connected inner pipe 301 through the shunt pipe 104, the excessive water flow is discharged into the water collecting tank 304 connected with the bottom through the decompression branch pipe 302 connected with one side of the inner pipe 301, and then the water flow can be processed later.
Working principle: in the use of the oxidation equipment, sewage can be connected with the inlet pipe 101, the sewage is discharged to the split pipe 104 through the inlet pipe 101, the inside electrolytic oxidation process is caused by the split pipe 104 at the inner side of the two-phase oxidation tank 102, then the sewage is discharged through the outlet pipe 105 connected with the split pipe 104 at the other side of the two-phase oxidation tank 102, when the pressure of the sewage entering the middle inlet pipe 101 is overlarge, the sewage can be discharged under reduced pressure when flowing into the connected inner pipe 301 through the split pipe 104, the water with excessive pressure is discharged into the water collecting tank 304 connected with the bottom through the decompression branch pipe 302 connected with one side of the inner pipe 301, and then the water can be treated later.
The foregoing description of the preferred embodiments of the utility model is not intended to be limiting, but rather is intended to cover all modifications, equivalents, and alternatives falling within the spirit and principles of the utility model.
Claims (7)
1. A two-phase FT oxidation plant comprising: reposition of redundant personnel oxidation subassembly (1), independent partition mechanism (2) and reposition of redundant personnel decompression mechanism (3), its characterized in that: the inside distribution of reposition of redundant personnel oxidation subassembly (1) has independent partition mechanism (2), the both sides of independent partition mechanism (2) are connected with reposition of redundant personnel decompression mechanism (3), independent partition mechanism (2) are including inside groove frame (201), inside groove plate (202), draw-in groove (203), electrolysis trough (204), electrode plate (205), flexible glue frame (206) and handle frame (207), and the top of inside groove frame (201) is provided with inside groove plate (202), the inner wall of inside groove plate (202) is provided with draw-in groove (203), and the laminating of the inner wall of draw-in groove (203) has electrolysis trough (204), the inside of electrolysis trough (204) is provided with electrode plate (205), and is provided with flexible glue frame (206) around electrode plate (205), the top of electrolysis trough (204) is provided with handle frame (207).
2. The two-phase FT oxidation unit of claim 1 wherein: the electrolytic tank (204) and the inner groove plate (202) form a buckling structure through the clamping groove (203), and the soft rubber frames (206) are attached along the two side edges of the electrolytic tank (204).
3. The two-phase FT oxidation unit of claim 1 wherein: the inner groove frame (201) is fixedly connected with the inner groove plate (202) and the shunt oxidation assembly (1), and three groups of the inner groove frame (201) and the inner groove plate (202) are arranged.
4. The two-phase FT oxidation unit of claim 1 wherein: the shunt oxidation assembly (1) comprises a feeding pipe (101), two-phase oxidation boxes (102), a support (103), shunt pipes (104), a discharge pipe (105) and a top cover (106), wherein the two sides of the feeding pipe (101) are provided with the two-phase oxidation boxes (102), the bottom end of each two-phase oxidation box (102) is provided with the support (103), the two sides of each two-phase oxidation box (102) are provided with the shunt pipes (104), one end of each shunt pipe (104) is connected with the discharge pipe (105), and the top end of each two-phase oxidation box (102) is provided with the top cover (106).
5. The two-phase FT oxidation unit of claim 4 wherein: the inlet pipe (101) is communicated with the shunt pipe (104) and the two-phase oxidation box (102), and the two-phase oxidation box (102) is provided with two groups.
6. The two-phase FT oxidation unit of claim 1 wherein: the diversion decompression mechanism (3) comprises an inner pipe (301), a decompression branch pipe (302), a pressure taper hole (303) and a water collecting tank (304), wherein the bottom end of the inner pipe (301) is connected with the decompression branch pipe (302), the pressure taper hole (303) is arranged in the decompression branch pipe (302), and the bottom end of the decompression branch pipe (302) is connected with the water collecting tank (304).
7. The two-phase FT oxidation unit of claim 6 wherein: the inner tube (301) is communicated with the split-flow oxidation assembly (1) and the independent splitting mechanism (2), and the inner tube (301) is connected with the decompression branch tube (302).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323213734.1U CN221141393U (en) | 2023-11-28 | 2023-11-28 | Two-phase FT oxidation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323213734.1U CN221141393U (en) | 2023-11-28 | 2023-11-28 | Two-phase FT oxidation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221141393U true CN221141393U (en) | 2024-06-14 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202323213734.1U Active CN221141393U (en) | 2023-11-28 | 2023-11-28 | Two-phase FT oxidation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221141393U (en) |
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- 2023-11-28 CN CN202323213734.1U patent/CN221141393U/en active Active
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