Silicon carbide / BDD rod-shaped row electrode electrolytic bath
By designing a silicon carbide/BDD rod-shaped electrode electrolytic cell, the contact area between the electrode rod and the organic wastewater is increased. By utilizing the high electron mobility and breakdown field strength of the silicon carbide electrode rod, the problem of limited active area of traditional electrodes is solved, and efficient organic wastewater degradation is achieved.
Patent Information
- Application Number
- CN202422763265.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-11-13
- Publication Date
- 2025-10-10
- Estimated Expiration
- 2034-11-13
AI Technical Summary
Traditional planar two-dimensional Si/BDD electrodes have a limited electrochemical active area, resulting in low efficiency in organic wastewater degradation.
A silicon carbide/BDD rod-shaped electrode electrolytic cell is used. By setting electrode modules and fixing mechanisms on the cell body, the contact area between the electrode rods and the organic wastewater is increased, and the electrode rods made of silicon carbide are used to improve the electron mobility and breakdown field strength.
The contact area between the organic wastewater and the electrode module is increased, the degradation efficiency of the organic wastewater is improved, and efficient organic wastewater treatment is achieved.
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Figure CN223422449U_ABST
Abstract
Description
Technical Field
[0001] The utility model belongs to the technical field of wastewater treatment, and in particular relates to a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell. Background Art
[0002] As an environmentally friendly treatment technology, the electrochemical advanced oxidation process is one of the most promising methods for treating highly difficult organic wastewater. The BDD thin film electrode is a third-generation electrode with excellent physicochemical stability, adsorption resistance and corrosion resistance. The potential window is as high as 3V, which is higher than the reaction potential of almost all organic matter. The low and stable background current requires a small voltage to produce the same redox current, and the energy consumption is low. When in service, it can produce highly oxidizing hydroxyl radicals (·OH), which can non-selectively oxidize most high-concentration, difficult-to-degrade organic wastewater. The development of an advanced oxidation treatment electrolytic cell device based on large-scale BDD thin film electrodes is the key to whether difficult-to-treat organic wastewater can be degraded efficiently and with low energy consumption.
[0003] Large-scale BDD thin-film electrode advanced oxidation treatment electrolyzers utilize several BDD thin-film electrodes grown on a flat, two-dimensional substrate (such as Si or metallic Nb) and integrated in a specific manner. This allows wastewater to circulate within the sealed electrolyzer, where organic matter is degraded into the end products CO2 and H2O by the strong oxidant ·OH. A problem with conventional flat, two-dimensional Si (or Nb) / BDD electrodes is their limited electrochemically active area, resulting in inefficient organic wastewater degradation. Utility Model Content
[0004] The utility model provides a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell to at least solve some of the above technical problems.
[0005] In order to achieve the above purpose, the technical solution adopted by the present utility model is as follows:
[0006] A silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, comprising a cell body, an electrode module disposed on the cell body for treating organic wastewater, and a fixing mechanism disposed between the cell body and the electrode module for sealing and fixing the electrode module; the cell body is provided with an electrolysis space adapted to the electrode module;
[0007] The electrode module includes a mounting plate arranged on the tank body, a number of electrode rods equidistantly distributed on the mounting plate and located in the electrolysis space, and a conductive column arranged on the mounting plate and connected to the electrode rods; a fixing mechanism is arranged between the mounting plate and the tank body.
[0008] Furthermore, a mounting hole adapted to the electrode rod is provided on the mounting plate, and the electrode rod passes through the mounting hole and is connected to the conductive column.
[0009] Further, the electrode rod is made of silicon carbide.
[0010] Further, the fixing mechanism comprises a first connecting flange arranged on the top of the groove body and connected with the mounting plate, and a sealing mechanism arranged between the first connecting flange and the mounting plate.
[0011] Further, the sealing mechanism comprises a sealing groove arranged on the first connecting flange, and a sealing ring embedded in the sealing groove.
[0012] Further, the mounting plate is provided with a second connecting flange matched with the first connecting flange, and the first connecting flange and the second connecting flange are connected through bolts.
[0013] Further, the first connecting flange is provided with a limiting groove, and the second connecting flange is provided with a limiting protrusion matched with the limiting groove, and the limiting protrusion is embedded in the limiting groove.
[0014] Further, the groove body is provided with a water inlet flange and a water outlet flange communicated with the electrolysis space, and the water inlet flange and the water outlet flange are located on both sides of the groove body.
[0015] Further, the electrolysis space comprises a plurality of cylindrical electrolytic cells arranged in the groove body, and adjacent two electrolytic cells are communicated with each other.
[0016] Compared with the prior art, the utility model has the advantages of the following:
[0017] The utility model discloses simple structure, scientific and reasonable in design, convenient to use, the utility model discloses electrode module is sealed and is installed on the groove body and is fixed through the fixing mechanism, thereby facilitating electrode module to the degradation of organic waste water in electrolysis space. When the organic waste water flows in the electrolysis space, because the electrolysis space side wall is arc-shaped, thereby making the contact area of organic waste water and electrode module increase, thereby facilitating electrode module to degrade organic waste water. BRIEF DESCRIPTION OF DRAWINGS
[0018] Figure 1 It is the structural schematic diagram of the utility model.
[0019] Figure 2 It is the sectional view of the utility model.
[0020] Figure 3 It is the schematic diagram of electrode module of the utility model.
[0021] Figure 4 It is the schematic diagram of the groove body of the utility model.
[0022] Figure 5 It is the schematic diagram of the mounting plate of the utility model.
[0023] Among them, the name corresponding to the reference sign is:
[0024] 1. Tank body; 2. Electrode module; 3. Electrolysis space; 4. Mounting plate; 5. Electrode rod; 6. Conductive column; 7. Mounting hole; 8. First connecting flange; 9. Second connecting flange; 10. Sealing groove; 11. Sealing ring; 12. Limiting groove; 13. Limiting protrusion; 14. Water inlet flange; 15. Water outlet flange; 16. Electrolytic tank. DETAILED DESCRIPTION
[0025] To make the purpose, technical solutions, and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings. It is apparent that the embodiments described herein are merely a portion of the embodiments of the present invention, and not all of them. All other embodiments derived by persons of ordinary skill in the art based on the embodiments of the present invention without inventive effort are also within the scope of protection of the present invention.
[0026] In the description of this utility model, it should be noted that the terms "center," "upper," "lower," "left," "right," "vertical," "horizontal," "inner," and "outer," etc., indicating orientations or positional relationships, are based on the orientations or positional relationships shown in the accompanying drawings and are intended solely to facilitate the description of this utility model and simplify the description. They do not indicate or imply that the devices or components referred to must have a specific orientation or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this utility model. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and should not be construed as indicating or implying relative importance.
[0027] In the description of this utility model, it should be noted that, unless otherwise expressly specified or limited, the terms "installed," "connected," and "connected" should be understood in a broad sense. For example, they can refer to fixed connections, detachable connections, or integral connections; of course, they can also refer to mechanical connections or electrical connections; in addition, they can also refer to direct connections, indirect connections through an intermediate medium, or internal connections between two components. For those skilled in the art, the specific meanings of the above terms in this utility model can be understood according to specific circumstances.
[0028] Example 1.
[0029] like Figure 1-5 As shown, the present invention provides a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, comprising a cell body 1, an electrode module 2 provided on the cell body 1 for treating organic wastewater, and a fixing mechanism provided between the cell body 1 and the electrode module 2 for sealing and fixing the electrode module 2; an electrolysis space 3 adapted to the electrode module 2 is provided on the cell body 1;
[0030] The electrode module 2 comprises a mounting plate 4 arranged on the groove body 1, a plurality of electrode rods 5 arranged equidistantly on the mounting plate 4 and located in the electrolysis space 3, and a conductive column 6 arranged on the mounting plate 4 and connected with the electrode rods 5; and the fixing mechanism is arranged between the mounting plate 4 and the groove body 1.
[0031] The electrode module 2 is sealed and mounted on the groove body 1 and fixed through the fixing mechanism, so that the electrode module 2 is convenient for degrading the organic wastewater in the electrolysis space 3.
[0032] The groove body 1 is of a rectangular structure.
[0033] The mounting plate 4 is of a rectangular structure, the electrode rods 5 are arranged equidistantly on the mounting plate 4 and located in the electrolysis space 3 after being mounted, the electrolysis space 3 is of a cylindrical structure, so that the organic wastewater can be fully contacted with the electrode rods 5 when passing through the electrode rods 5, and the cylindrical structure can increase the contact area of the electrode rods 5 and the organic wastewater, the conductive column 6 is arranged on the mounting plate 4 and connected with the electrode rods 5, the conductive column 6 can be connected with the power supply device outside, in use, the mounting plate 4 is mounted on the groove body 1 through the fixing mechanism, the conductive column 6 is connected with the power supply device outside, so as to supply power to the electrode rods 5, and the electrode rods 5 degrade the organic wastewater in the electrolysis space 3.
[0034] Embodiment 2.
[0035] As shown in Figure 1-5 The utility model discloses a silicon carbide / BDD rod-shaped continuous electrode electrolytic tank, including groove body 1, be arranged on groove body 1 for processing organic wastewater's electrode module 2 and be arranged between groove body 1 and electrode module 2 for sealing fixed electrode module 2's fixing mechanism, be equipped with with electrolysis space 3 of electrode module 2 adaptation on groove body 1,
[0036] The electrode module 2 comprises a mounting plate 4 arranged on the groove body 1, a plurality of electrode rods 5 arranged equidistantly on the mounting plate 4 and located in the electrolysis space 3, and a conductive column 6 arranged on the mounting plate 4 and connected with the electrode rods 5; and the fixing mechanism is arranged between the mounting plate 4 and the groove body 1.
[0037] The mounting plate 4 is provided with mounting holes 7 matched with the electrode rods 5, and the electrode rods 5 are connected with the conductive column 6 through the mounting holes 7.
[0038] This embodiment 2 provides a more preferred structure of the mounting plate 4 based on the embodiment 1, specifically: a mounting hole 7 adapted to the electrode rod 5 is opened on the mounting plate 4, and the electrode rod 5 passes through the mounting hole 7 and is connected to the conductive column 6.
[0039] The mounting hole 7 of the present invention can facilitate the installation of the electrode rod 5 . The electrode rod 5 passes through the mounting hole 7 and is connected to the conductive column 6 , which can facilitate the connection between the electrode rods 5 and the electrode rods 5 .
[0040] Example 3.
[0041] like Figure 1-5 As shown, the present invention provides a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, comprising a cell body 1, an electrode module 2 provided on the cell body 1 for treating organic wastewater, and a fixing mechanism provided between the cell body 1 and the electrode module 2 for sealing and fixing the electrode module 2; an electrolysis space 3 adapted to the electrode module 2 is provided on the cell body 1;
[0042] The electrode module 2 includes a mounting plate 4 arranged on the tank body 1, a number of electrode rods 5 equidistantly distributed on the mounting plate 4 and located in the electrolysis space 3, and a conductive column 6 arranged on the mounting plate 4 and connected to the electrode rods 5; a fixing mechanism is arranged between the mounting plate 4 and the tank body 1.
[0043] The electrode rod 5 is made of silicon carbide.
[0044] This embodiment 3 provides a more preferred structure of the electrode rod 5 based on the embodiment 1, specifically: the electrode rod 5 is made of silicon carbide.
[0045] The electrode rod 5 of the utility model is made of silicon carbide, which enables the electrode rod 5 to have excellent physical properties such as good electron mobility, high breakdown field strength and high thermal conductivity, thereby facilitating the electrode rod 5 to degrade organic wastewater.
[0046] Example 4.
[0047] like Figure 1-5 As shown, the present invention provides a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, comprising a cell body 1, an electrode module 2 provided on the cell body 1 for treating organic wastewater, and a fixing mechanism provided between the cell body 1 and the electrode module 2 for sealing and fixing the electrode module 2; an electrolysis space 3 adapted to the electrode module 2 is provided on the cell body 1;
[0048] The electrode module 2 includes a mounting plate 4 arranged on the tank body 1, a number of electrode rods 5 equidistantly distributed on the mounting plate 4 and located in the electrolysis space 3, and a conductive column 6 arranged on the mounting plate 4 and connected to the electrode rods 5; a fixing mechanism is arranged between the mounting plate 4 and the tank body 1.
[0049] The fixing mechanism includes a first connecting flange 8 provided on the top of the tank body 1 and connected to the mounting plate 4, and a sealing mechanism provided between the first connecting flange 8 and the mounting plate 4; the first connecting flange 8 and the mounting plate 4 are connected by bolts.
[0050] This embodiment 4 provides a more preferred structure of the fixing mechanism based on embodiment 1, specifically: the fixing mechanism includes a first connecting flange 8 provided at the top of the trough body 1 and connected to the mounting plate 4, and a sealing mechanism provided between the first connecting flange 8 and the mounting plate 4; the first connecting flange 8 and the mounting plate 4 are connected by bolts.
[0051] The first connecting flange 8 of the utility model is arranged at the top of the trough body 1, and the first connecting flange 8 and the trough body 1 are an integrated structure, and the first connecting flange 8 and the mounting plate 4 are connected by bolts. At the same time, a sealing mechanism is provided between the first connecting flange 8 and the mounting plate 4. The sealing mechanism can seal the connection between the first connecting flange 8 and the mounting plate 4 to prevent leakage of organic wastewater in the electrolysis space 3. A plurality of bolt holes are respectively provided on the first connecting flange 8 and the mounting plate 4, and the bolt holes on the first connecting flange 8 correspond one-to-one to the bolt holes on the mounting plate 4. The bolts are threadedly connected to the two threaded holes, thereby facilitating the connection between the first connecting flange 8 and the second connecting flange 9.
[0052] Example 5.
[0053] like Figure 1-5 As shown, the present invention provides a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, comprising a cell body 1, an electrode module 2 provided on the cell body 1 for treating organic wastewater, and a fixing mechanism provided between the cell body 1 and the electrode module 2 for sealing and fixing the electrode module 2; an electrolysis space 3 adapted to the electrode module 2 is provided on the cell body 1;
[0054] The electrode module 2 includes a mounting plate 4 provided on the tank body 1, a plurality of electrode rods 5 equidistantly distributed on the mounting plate 4 and located in the electrolysis space 3, and a conductive column 6 provided on the mounting plate 4 and connected to the electrode rods 5; a fixing mechanism is provided between the mounting plate 4 and the tank body 1
[0055] The fixing mechanism includes a first connecting flange 8 provided on the top of the tank body 1 and connected to the mounting plate 4, and a sealing mechanism provided between the first connecting flange 8 and the mounting plate 4; the first connecting flange 8 and the mounting plate 4 are connected by bolts.
[0056] The sealing mechanism includes a sealing groove 10 provided on the first connecting flange 8 and a sealing ring 11 embedded in the sealing groove 10 .
[0057] This embodiment 5 provides a more preferred structure of the sealing mechanism based on the embodiment 4. Specifically, the sealing mechanism includes a sealing groove 10 provided on the first connecting flange 8 and a sealing ring 11 embedded in the sealing groove 10.
[0058] The sealing groove 10 of the utility model is arranged on the first connecting flange 8, and the sealing ring 11 is embedded in the sealing groove 10. When the first connecting flange 8 and the mounting plate 4 are connected, the bottom surface of the mounting plate 4 is tightly pressed against the sealing ring 11, thereby sealing the connection between the first connecting flange 8 and the mounting plate 4, thereby preventing leakage of organic wastewater.
[0059] Example 6.
[0060] like Figure 1-5 As shown, the present invention provides a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, comprising a cell body 1, an electrode module 2 provided on the cell body 1 for treating organic wastewater, and a fixing mechanism provided between the cell body 1 and the electrode module 2 for sealing and fixing the electrode module 2; an electrolysis space 3 adapted to the electrode module 2 is provided on the cell body 1;
[0061] The electrode module 2 includes a mounting plate 4 arranged on the tank body 1, a number of electrode rods 5 equidistantly distributed on the mounting plate 4 and located in the electrolysis space 3, and a conductive column 6 arranged on the mounting plate 4 and connected to the electrode rods 5; a fixing mechanism is arranged between the mounting plate 4 and the tank body 1.
[0062] The fixing mechanism includes a first connecting flange 8 provided on the top of the trough body 1, a second connecting flange 9 provided on the bottom surface of the electrode module 2 and adapted to the first connecting flange 8, and a sealing mechanism provided between the first connecting flange 8 and the second connecting flange 9; the first connecting flange 8 and the second connecting flange 9 are connected by bolts.
[0063] A limiting groove 12 is provided on the first connecting flange 8 , and a limiting protrusion 13 adapted to the limiting groove 12 is provided on the second connecting flange 9 . The limiting protrusion 13 is located in the limiting groove 12 .
[0064] Based on Example 4, this Example 6 provides a more preferred structure for the first connecting flange 8, specifically: a limiting groove 12 is provided on the first connecting flange 8, and a limiting protrusion 13 adapted to the limiting groove 12 is provided on the second connecting flange 9, and the limiting protrusion 13 is located in the limiting groove 12.
[0065] The limiting groove 12 of the utility model is opened on the first connecting flange 8, and the limiting protrusion 13 is set on the second connecting flange 9, and the limiting protrusion 13 and the second connecting flange 9 are an integrated structure. When in use, the limiting protrusion 13 is placed in the limiting groove 12, which can facilitate the limiting and guiding of the first connecting flange 8 and the second connecting flange 9, thereby facilitating the fixing of the electrode module 2 on the top of the tank body 1.
[0066] Example 7.
[0067] like Figure 1-5 As shown, the present invention provides a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, comprising a cell body 1, an electrode module 2 provided on the cell body 1 for treating organic wastewater, and a fixing mechanism provided between the cell body 1 and the electrode module 2 for sealing and fixing the electrode module 2; an electrolysis space 3 adapted to the electrode module 2 is provided on the cell body 1;
[0068] The electrode module 2 includes a mounting plate 4 arranged on the tank body 1, a number of electrode rods 5 equidistantly distributed on the mounting plate 4 and located in the electrolysis space 3, and a conductive column 6 arranged on the mounting plate 4 and connected to the electrode rods 5; a fixing mechanism is arranged between the mounting plate 4 and the tank body 1.
[0069] The tank body 1 is provided with a water inlet flange 14 and a water outlet flange 15 which are in communication with the electrolysis space 3 . The water inlet flange 14 and the water outlet flange 15 are located on both sides of the tank body 1 , respectively.
[0070] This embodiment 7 provides a more preferred structure of the tank body 1 based on embodiment 1, specifically: the tank body 1 is provided with a water inlet flange 14 and a water outlet flange 15 connected to the electrolysis space 3, and the water inlet flange 14 and the water outlet flange 15 are respectively located on both sides of the tank body 1.
[0071] The water inlet flange 14 of the utility model is arranged at the bottom of one side of the tank body 1, and the water inlet flange 14 is connected with the electrolysis space 3, so as to facilitate the entry of organic wastewater into the electrolysis space 3. The water outlet flange 15 is arranged at the top of the other side of the tank body 1. After the electrode rod 5 degrades the organic wastewater in the electrolysis space 3, the degraded organic wastewater is discharged through the water outlet flange 15. During use, a large number of bubbles will be generated when the electrode rod 5 degrades the organic wastewater. The bubbles will adhere to the electrode rod 5 and affect the degradation efficiency of the electrode rod 5. Since the organic wastewater enters through the bottom of the electrolysis space 3, the rising direction of the bubbles is consistent with the flow direction of the wastewater, so that the bubbles on the electrode rod 5 will be discharged from the electrolysis space 3 through the water outlet flange 15 along with the water flow, thereby improving the degradation efficiency of the electrolysis space 3.
[0072] Example 8.
[0073] like Figure 1-5 As shown, the present invention provides a silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, comprising a cell body 1, an electrode module 2 provided on the cell body 1 for treating organic wastewater, and a fixing mechanism provided between the cell body 1 and the electrode module 2 for sealing and fixing the electrode module 2; an electrolysis space 3 adapted to the electrode module 2 is provided on the cell body 1;
[0074] The electrode module 2 includes a mounting plate 4 arranged on the tank body 1, a number of electrode rods 5 equidistantly distributed on the mounting plate 4 and located in the electrolysis space 3, and a conductive column 6 arranged on the mounting plate 4 and connected to the electrode rods 5; a fixing mechanism is arranged between the mounting plate 4 and the tank body 1.
[0075] The electrolysis space 3 includes a plurality of cylindrical electrolytic cells 16 disposed in the cell body 1 ; two adjacent electrolytic cells 16 are connected to each other.
[0076] This embodiment 8 provides a more preferred structure of the cell body 1 based on the embodiment 1, specifically: the electrolysis space 3 includes a plurality of cylindrical electrolytic cells 16 arranged in the cell body 1; and two adjacent electrolytic cells 16 are connected to each other.
[0077] The utility model has a plurality of cylindrical electrolytic cells 16 on the cell body 1, and two adjacent electrolytic cells 16 are interconnected, which can facilitate the flow of organic wastewater in the electrolytic cell 16, thereby facilitating the electrode rod 5 to degrade the organic wastewater in the electrolytic cell 16. The cylindrical electrolytic cell 16 can make the organic wastewater flow along the inner wall of the electrolytic cell 16 and can make the organic wastewater flow along the outer wall of the electrode rod 5, thereby increasing the contact area between the electrode rod 5 and the organic wastewater, thereby improving the degradation efficiency of the electrode rod 5.
[0078] The diameter of the electrode rod 5 of the utility model is smaller than that of the electrolysis space 3, so as to facilitate the flow of organic wastewater. The number of electrode rods 5 corresponds to the number of electrolytic cells 16, and the number of conductive columns 6 corresponds to the number of electrode rods 5.
[0079] Finally, it should be noted that the above embodiments are merely preferred embodiments of the present invention and are intended to illustrate the technical solutions of the present invention, rather than to limit them, and certainly not to limit the patent scope of the present invention. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or make equivalent replacements for some or all of the technical features therein. These modifications or replacements do not deviate the essence of the corresponding technical solutions from the scope of the technical solutions of the embodiments of the present invention. In other words, any changes or embellishments made to the main design concept and spirit of the present invention that have no substantive significance, provided that the technical problems they solve are still consistent with those of the present invention, should be included in the protection scope of the present invention. In addition, the direct or indirect application of the technical solutions of the present invention in other related technical fields should also be included in the patent protection scope of the present invention.
Claims
1. A silicon carbide / BDD rod-shaped continuous electrode electrolytic cell, characterized in that: The invention comprises a tank body (1), an electrode module (2) provided on the tank body (1) for treating organic wastewater, and a fixing mechanism provided between the tank body (1) and the electrode module (2) for sealing and fixing the electrode module (2); an electrolysis space (3) adapted to the electrode module (2) is provided on the tank body (1); The electrode module (2) comprises a mounting plate (4) arranged on the tank body (1), a plurality of electrode rods (5) equidistantly distributed on the mounting plate (4) and located in the electrolysis space (3), and a conductive column (6) arranged on the mounting plate (4) and connected to the electrode rods (5); a fixing mechanism is arranged between the mounting plate (4) and the tank body (1).
2. The silicon carbide / BDD rod-shaped continuous electrode electrolytic cell according to claim 1, characterized in that: The mounting plate (4) is provided with a mounting hole (7) adapted to the electrode rod (5), and the electrode rod (5) passes through the mounting hole (7) and is connected to the conductive column (6).
3. The silicon carbide / BDD rod-shaped continuous electrode electrolytic cell according to claim 1, characterized in that: The electrode rod (5) is made of silicon carbide.
4. The silicon carbide / BDD rod-shaped continuous electrode electrolytic cell according to claim 1, characterized in that: The fixing mechanism comprises a first connecting flange (8) provided on the top of the trough body (1) and connected to the mounting plate (4), and a sealing mechanism provided between the first connecting flange (8) and the mounting plate (4).
5. The silicon carbide / BDD rod-shaped continuous electrode electrolytic cell according to claim 4, characterized in that: The sealing mechanism comprises a sealing groove (10) provided on the first connecting flange (8) and a sealing ring (11) embedded in the sealing groove (10).
6. The silicon carbide / BDD rod-shaped continuous electrode electrolytic cell according to claim 4, characterized in that: A second connecting flange (9) adapted to the first connecting flange (8) is provided on the mounting plate (4), and the first connecting flange (8) and the second connecting flange (9) are connected via bolts.
7. The silicon carbide / BDD rod-shaped continuous electrode electrolytic cell according to claim 6, characterized in that: The first connecting flange (8) is provided with a limiting groove (12), and the second connecting flange (9) is provided with a limiting protrusion (13) adapted to the limiting groove (12), and the limiting protrusion (13) is embedded in the limiting groove (12).
8. The silicon carbide / BDD rod-shaped continuous electrode electrolytic cell according to claim 1, characterized in that: The tank body (1) is provided with a water inlet flange (14) and a water outlet flange (15) which are connected to the electrolysis space (3). The water inlet flange (14) and the water outlet flange (15) are respectively located on both sides of the tank body (1).
9. The silicon carbide / BDD rod-shaped continuous electrode electrolytic cell according to claim 1, characterized in that: The electrolysis space (3) includes a plurality of cylindrical electrolysis cells (16) arranged in the cell body (1); two adjacent electrolysis cells (16) are connected to each other.