Electrochemical reactor of spiral sheet electrode

By adopting the design of helical sheet anode and cathode in the electrochemical reactor, the shortcomings of the existing electrochemical reactor in the electrode structure improvement are solved, and more efficient water flow and mass transfer are achieved, simplifying the installation process.

CN222684380UActive Publication Date: 2025-03-28NANJING HUAGONG INNOVATION ENVIRONMENT RES INST CO LTD
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Patent Information

Application Number
CN202421030862.4
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-05-13
Publication Date
2025-03-28
Estimated Expiration
2034-05-13

AI Technical Summary

Technical Problem

Existing electrochemical reactors lack direct improvements to the electrode structure in improving the water flow rate on the electrode surface, resulting in poor mass transfer effect and low collision probability.

Method used

The electrochemical reactor design adopts a helical sheet anode and cathode, and the electrode sheet is maximized in the tubular space through a helical structure, and the water flow velocity on the electrode surface is enhanced by directional moving water flow.

Benefits of technology

It is achieved without adding additional structures to improve the water flow rate and mass transfer effect on the electrode surface, simplifying the installation process and reducing the land occupation requirement.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses an electrochemical reactor with a spiral sheet-shaped electrode, which relates to the technical field of water treatment and comprises a spiral sheet-shaped anode, a first flange sheet is welded at the upper end of the spiral sheet-shaped anode, an anode binding post is welded outside the first flange sheet, a spiral sheet-shaped cathode is arranged below the spiral sheet-shaped anode, and a second flange sheet is welded outside the spiral sheet-shaped cathode. A second flange piece is welded to the lower end of the spiral sheet-shaped cathode, and a cathode binding post is welded to the outer portion of the second flange piece. Through the spiral sheet type cathode and anode, the electrode sheet can be utilized to the greatest extent in the same tubular space, meanwhile, the spiral sheet type cathode and anode can realize directional movement of water flow, the water flow direction can be changed without additionally arranging structures such as a baffle plate, and the water flow direction can be directly connected to an existing pipeline in the mode, so that the installation is convenient and fast, and the cost is low. And additional field installation is not needed.
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Description

Technical Field

[0001] The utility model relates to the technical field of water treatment, in particular to an electrochemical reactor with spiral sheet electrodes. Background Art

[0002] Wastewater treatment has always been a research hotspot. The electrochemical method for treating sewage has the advantages of not needing to add oxidants, flocculants and other chemicals, small equipment size, small footprint, simple and flexible operation, etc., and is called a green treatment process.

[0003] At present, most electrochemical reactors in the field of water treatment are based on flat-plate electrodes because they are easy to process and install. However, flat-plate electrodes have poor mass transfer effects and are less likely to collide with organic pollutants. In order to increase the probability of collision, the flow rate of water on the electrode surface is generally increased by increasing the electrode area or adding baffles. However, there are few cases of direct improvement of the electrode structure. Utility Model Content

[0004] In view of the above problems existing in the existing electrochemical reactor, the present utility model is proposed.

[0005] Therefore, the purpose of the utility model is to provide an electrochemical reactor with spiral sheet electrodes, which solves the problem that the existing electrochemical reactors generally increase the electrode area or add baffles to enhance the flow rate of water on the electrode surface, but there are few cases of direct improvement of the electrode structure.

[0006] In order to achieve the above purpose, the utility model provides the following technical solutions:

[0007] An electrochemical reactor with a spiral sheet electrode comprises a spiral sheet anode, a first flange is welded to the upper end of the spiral sheet anode, an anode terminal is welded to the outside of the first flange, a spiral sheet cathode is arranged below the spiral sheet anode, a second flange is welded to the lower end of the spiral sheet cathode, and a cathode terminal is welded to the outside of the second flange.

[0008] Preferably, the outer surfaces of the spiral sheet-shaped anode and the spiral sheet-shaped cathode are jointly provided with a tubular shell.

[0009] Preferably, a water outlet is provided on one side of the upper end of the tubular shell.

[0010] Preferably, a water inlet is provided on one side of the lower end of the tubular housing.

[0011] Preferably, a water sealing line is provided on one side of the first flange and the second flange which are close to each other.

[0012] Preferably, an insulating gasket is provided between the first flange and the second flange.

[0013] In the above technical solution, the technical effects and advantages provided by the utility model are:

[0014] 1. The utility model uses spiral-plate anode and cathode to maximize the use of electrode sheets in the tubular space. At the same time, the spiral-plate anode and cathode can also realize the directional movement of water flow, without the need to add additional structures such as baffles to change the direction of water flow. Moreover, this method can be directly connected to the existing pipeline, which is convenient to install and does not require additional site installation.

[0015] 2. The utility model can play a protective role through the tubular shell. At the same time, the tubular shell adopts a standard pipe diameter, which is convenient for later connection with conventional pipelines. At the same time, the spiral sheet anode and the spiral sheet cathode have the same structure, and the spiral direction is consistent with the water inlet direction. BRIEF DESCRIPTION OF THE DRAWINGS

[0016] In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings required for use in the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments recorded in the present utility model. For ordinary technicians in this field, other drawings can also be obtained based on these drawings.

[0017] Figure 1 It is a schematic diagram of the structure of the utility model;

[0018] Figure 2 For the utility model Figure 1 A three-dimensional image of the spiral sheet anode.

[0019] Description of reference numerals:

[0020] 1. Spiral sheet anode; 2. First flange; 3. Anode terminal; 4. Spiral sheet cathode; 5. Second flange; 6. Cathode terminal; 7. Tubular shell; 8. Water outlet; 9. Water inlet; 10. Water sealing line; 11. Insulating gasket. DETAILED DESCRIPTION

[0021] In order to enable those skilled in the art to better understand the technical solution of the present invention, the present invention will be further described in detail below in conjunction with the accompanying drawings.

[0022] The utility model embodiment discloses an electrochemical reactor with spiral sheet electrodes.

[0023] Embodiment 1

[0024] Reference Figure 1-2An electrochemical reactor with a spiral sheet electrode comprises a spiral sheet anode 1, a first flange 2 is welded to the upper end of the spiral sheet anode 1, an anode terminal 3 is welded to the outside of the first flange 2, a spiral sheet cathode 4 is arranged below the spiral sheet anode 1, a second flange 5 is welded to the lower end of the spiral sheet cathode 4, and a cathode terminal 6 is welded to the outside of the second flange 5.

[0025] The first flange 2 and the second flange 5 are both flanges of standard size. The outer surfaces of the first flange 2 and the second flange 5 are provided with threaded holes to facilitate subsequent installation. At the same time, the anode terminal 3 can be connected to the anode of the DC power supply, and the cathode terminal 6 can be connected to the cathode of the power supply.

[0026] Embodiment 2

[0027] Based on Example 1, refer to Figure 1 The outer surfaces of the spiral sheet anode 1 and the spiral sheet cathode are jointly provided with a tubular shell 7, a water outlet 8 is provided on one side of the upper end of the tubular shell 7, and a water inlet 9 is provided on one side of the lower end of the tubular shell 7.

[0028] The tubular housing 7 adopts a standard pipe diameter to facilitate the subsequent connection with conventional pipelines. At the same time, the spiral sheet anode 1 and the spiral sheet cathode 4 have the same structure, and the spiral direction is consistent with the water inlet direction.

[0029] Embodiment 3

[0030] Based on Example 1, refer to Figure 1 A water sealing line 10 is provided on the side where the first flange 2 and the second flange 5 are close to each other, and an insulating gasket 11 is provided between the first flange 2 and the second flange 5 .

[0031] The sealing property of the device can be improved by using the water sealing line 10 , and the insulation property of the device can be improved by using the insulating gasket 11 .

[0032] The above only describes some exemplary embodiments of the present invention by way of illustration. It is undoubted that those skilled in the art can modify the described embodiments in various ways without departing from the spirit and scope of the present invention. Therefore, the above drawings and descriptions are illustrative in nature and should not be construed as limiting the scope of protection of the claims of the present invention.

Claims

1. An electrochemical reactor with a spiral sheet electrode, comprising a spiral sheet anode (1), characterized in that: A first flange (2) is welded to the upper end of the spiral sheet anode (1), an anode terminal (3) is welded to the outside of the first flange (2), a spiral sheet cathode (4) is arranged below the spiral sheet anode (1), a second flange (5) is welded to the lower end of the spiral sheet cathode (4), and a cathode terminal (6) is welded to the outside of the second flange (5).

2. The electrochemical reactor of spiral sheet electrodes according to claim 1, characterized in that: The outer surfaces of the spiral sheet-shaped anode (1) and the spiral sheet-shaped cathode are jointly provided with a tubular shell (7).

3. The electrochemical reactor of spiral sheet electrodes according to claim 2, characterized in that: A water outlet (8) is provided on one side of the upper end of the tubular housing (7).

4. The electrochemical reactor of spiral sheet electrodes according to claim 2, characterized in that: A water inlet (9) is provided on one side of the lower end of the tubular housing (7).

5. The electrochemical reactor of spiral sheet electrodes according to claim 1, characterized in that: A water sealing line (10) is provided on one side of the first flange (2) and the second flange (5) that are close to each other.

6. The electrochemical reactor of spiral sheet electrodes according to claim 1, characterized in that: An insulating gasket (11) is provided between the first flange (2) and the second flange (5).