Non-equivalent electrode propulsion structure and method based on electrode corrosion

Abstract

To provide a propulsion structure of a non-equivalent electrode capable of prolonging a usage life of an electrode by efficiently utilizing each electrode block as well as always keeping a contact surface between an electrode and a glass liquid to a same plane, equalizing a current distribution in the electrode and the glass liquid by parallelizing to a pool wall, and melting the glass liquid in a furnace uniformly.SOLUTION: An electrode 1 is configured by multiple electrode blocks 1-1. A electrode module with a same or similar erosion amount constitutes an electrode module 1-2. A corresponding silver plate module 2-2 and a propulsion module are attached to a different electrode module to constitute a model for calculating an erosion amount of each electrode block under a different temperature condition, a total propulsion amount of each electrode block during operation is calculated, one electrode module is constituted by an electrode block with a same or similar erosion amount, and a silver module and a propulsion module are designed for a different electrode module each, promoting a differentiation of the electrode block in the electrode by non-equivalent amount.SELECTED DRAWING: Figure 1

Description

Technical Field

[0001] The present invention belongs to the technical field of manufacturing substrate glass, and specifically relates to a non-equivalent electrode propulsion structure and method based on the characteristics of electrode erosion.

Background Art

[0002] The kiln is one of the most important facilities in the manufacturing process of substrate glass. Its main role is to melt glass powder into high-quality glass liquid and manufacture substrate glass through other processes. Due to the existence and distribution of the flow field in the kiln, there are differences in the electrode erosion amounts in different regions of the same electrode. Specifically, the erosion amount at the upper part of the electrode is small, the erosion amount at the lower part is large, the erosion amount in the middle part is small, and the erosion amounts at both ends are large.

Summary of the Invention

Problems to be Solved by the Invention

[0003] However, in the conventional electrode propulsion method, the entire electrode is propelled, that is, the propulsion amounts of the electrode blocks in the electrode are the same. Therefore, the intervals between the electrode blocks with less consumption in each pair of electrodes are narrowed. The electrical resistance of the glass liquid decreases due to the shortening of the distance of this electrode block, and the electrode current concentrates on this electrode block. As a result, the current distribution in the electrode and the glass liquid becomes non-uniform, and finally the melting of the glass liquid becomes non-uniform. In addition, due to the uniform propulsion of the electrode, the insertion depth of the electrode block with less consumption into the glass becomes deeper, the consumption amount of this electrode block increases, and the overall life of the electrode becomes shorter. Furthermore, due to the uniform propulsion, the electrode and the pool wall are not on the same plane, so the erosion of the pool wall bricks near the electrode further progresses.

[0004] In the conventional overall electrode propulsion method (also referred to as the electrode uniform propulsion method), there are technical problems such as non-uniform current distribution of the electrodes and the glass liquid, large consumption of the electrode blocks, and easy erosion of the pool wall bricks near the electrodes. In contrast, keeping the contact surface between the electrodes and the glass liquid always in the same plane, uniformly distributing the current in the electrodes and the glass liquid, realizing uniform melting of the glass liquid in the furnace, efficiently using each electrode block, and extending the life of the electrodes, there is a problem that it is easy to be done in the new electric conventional one.

[0005] That is, in the conventional overall electrode propulsion method, the current distribution of the electrodes and the glass liquid is non-uniform, the consumption of the electrode blocks is large, and the pool wall bricks near the electrodes are easily eroded.

Means for Solving the Problems

[0006] Therefore, in order to overcome the above-mentioned drawbacks of the prior art, the present invention aims to disclose a non-equivalent electrode propulsion structure and method based on the characteristics of electrode erosion, and solves the technical problems existing in the conventional electrode uniform propulsion method, such as non-uniform current distribution of the electrodes and the glass liquid, large consumption of the electrode blocks, and easy erosion of the pool wall bricks near the electrodes.

[0007] In order to achieve the above object, the present invention adopts the following technical means. The present invention discloses a non-equivalent electrode propulsion structure based on the characteristics of electrode erosion, which includes an electrode (1), a silver plate (2) disposed between the electrodes (1), and a propulsion module (4) disposed at the rear end of the electrode (1). The electrode (1) is composed of a plurality of electrode blocks (1-1), and the electrode blocks (1-1) with the same or similar erosion amounts constitute one electrode module (1-2). Corresponding silver plate modules (2-2) and propulsion modules (4) are respectively attached to different electrode modules (1-2).

[0008] Furthermore, the electrode module (1-2) is composed of a single electrode block (1-1) or a plurality of electrode blocks (1-1).

[0009] Furthermore, the silver plate module (2-2) is designed based on the electrode module (1-2). When a single electrode block (1-1) constitutes one electrode module (1-2), the silver plate module (2-2) is a single silver plate block (2-1). When a plurality of electrode blocks (1-1) constitute one electrode module (1-2), the silver plate module (2-2) is a combination of a plurality of silver plate blocks (2-1).

[0010] Furthermore, in the central region of the silver plate module (2-2) composed of a plurality of silver plate blocks (2-1), no silver plate block (2-1) is installed.

[0011] Furthermore, the electrode block (1-1) is a cuboid, and a step groove (1-11) is provided around it. The silver plate block (2-1) is fitted into the step grooves (1-11) of two adjacent electrode blocks (1-1), and all the silver plate blocks (2-1) are connected in series.

[0012] Furthermore, the width of the silver plate block (2-1) is smaller than the depth of the step groove (1-11).

[0013] Furthermore, the propulsion module (4) includes an electrode module top plate (4-1), a top screw (4-2), and a propulsion bracket (4-3) sequentially arranged at the rear end of the electrode module (1-2). One end of the top screw (4-2) is fixed to the electrode module top plate (4-1) in an insulated state, the other end of the top screw (4-2) is connected to the propulsion bracket (4-3), and the propulsion bracket (4-3) is fixed to the ground.

[0014] Furthermore, the electrode module top plate (4-1) is used in combination with the electrode module (1-2). The propulsion module (4) includes a plurality of electrode module top plates (4-1), and each of them is independent of each other.

[0015] Furthermore, an electric flange (3) is provided at the upper end of the silver plate (2), and cooling air is installed around the electrode (1).

[0016] In addition, the present invention is a propulsion method for a non-equivalent electrode propulsion structure based on the characteristics of the above electrode erosion. As step S1, by combining the erosion characteristics of the electrode (1) obtained after disassembling the kiln furnace and the analysis of the erosion characteristics of the electrode (1) by the flow field simulation in the kiln furnace, a calculation model of the erosion amount of each electrode block (1-1) of the electrode (1) under different temperature conditions is constructed, and the total erosion amount of each electrode block (1-1) during operation is calculated; as step S2, based on the total erosion amount of each electrode block (1-1) obtained in step S1 above, the electrode blocks (1-1) with the same or similar erosion amount are configured as one electrode module (1-2), the corresponding silver plate module (2-2) and propulsion module (4) are designed based on different electrode modules (1-2), the length of each electrode block (1-1) is optimally designed according to the total erosion amount of each electrode block (1-1), the initial length of the electrode block (1-1) with a large erosion amount is made long, and the initial length of the electrode block (1-1) with a small erosion amount is made short; as step S3, based on the operating life of the disassembled kiln furnace and the total erosion amount of each electrode block (1-1) obtained in step S1 above, the daily consumption amount of each electrode block (1-1) is calculated, and by combining the analysis of the electrode erosion characteristics by the flow field simulation in the kiln furnace, the calculated daily consumption amount of each electrode block (1-1) is corrected, the propulsion cycle of the electrode is set to N days, and the electrode consumption amount of each electrode module (1-2) in N days is calculated; as step S4, based on the electrode consumption amount of each electrode module (1-2) in N days obtained in step S3 above, the differential propulsion of the electrode (1) is realized by using the propulsion module (4) of the electrode (1). A propulsion method for a non-equivalent electrode propulsion structure based on the characteristics of electrode erosion is disclosed.

Effects of the Invention

[0017] The non-equal electrode propulsion structure based on the characteristics of electrode erosion according to the present invention has the following beneficial effects. The present invention discloses a non-equal electrode propulsion structure based on the law of electrode erosion, including: an electrode, a silver plate disposed between the electrodes, and a propulsion module for propelling the electrode installed at the rear end of the electrode. The electrode is composed of a plurality of electrode blocks, and the electrode blocks with the same or similar erosion amounts constitute one electrode module. Corresponding silver plate modules and propulsion modules are provided for different electrode modules, and different propulsion amounts are set for each different electrode module, so that the electrode blocks in the electrode can be differentially propelled in unequal amounts. Thereby, the contact surface between the electrode and the glass liquid can always be kept in the same plane and parallel to the pool wall, the current distribution in the electrode and the glass liquid can be made uniform, the glass liquid in the kiln can be uniformly melted, and the service life of the electrode can be extended by efficiently using each electrode block.

[0018] Furthermore, the electrode module can be composed of a single electrode block or a plurality of electrode blocks, and it is possible to collectively propel adjacent electrode blocks with the same consumption amount.

[0019] Also, the silver plate module is designed based on the electrode module. When a single electrode block is one electrode module, the silver plate module becomes a single silver plate block. When a plurality of electrode blocks constitute one electrode module, the silver plate module becomes a combination of a plurality of silver plate blocks. Thereby, the uniformity of the current distribution is ensured, and the mutual independence between the electrode modules is ensured.

[0020] Also, the electrode block is a rectangular parallelepiped, and a step groove is provided around it. The silver plate block is fitted into the step grooves of two adjacent electrode blocks. All the silver plate blocks are connected in series, and it is ensured that the front ends of all the electrodes are in close contact.

[0021] Furthermore, the width of the silver plate block is smaller than the depth of the step groove, which contributes to increasing the contact area between the cooling air and the electrode and promoting the heat dissipation of the electrode.

[0022] Furthermore, the propulsion module includes an electrode module top plate, top screws, and a propulsion bracket that are sequentially arranged at the rear end of the electrode module. One end of the top screw is fixed to the electrode module top plate and insulated, and the other end is connected to the propulsion bracket. Since the propulsion bracket is fixed to the ground, smooth propulsion of each electrode module is ensured.

[0023] Furthermore, the electrode module top plate is used in combination with the electrode module. The propulsion module includes a plurality of electrode module top plates that are independent of each other. During differential propulsion, when each electrode module is propelled, they do not interfere with each other.

[0024] Furthermore, an electrical flange is provided at the top of the silver plate. By ensuring that the silver plate evenly transmits the current within the electrical flange to each electrode module, the current distribution within the electrode is made uniform. Cooling air is arranged near the electrode, and the cooling air enables better heat dissipation from the surface of the electrode and its surroundings.

[0025] In addition, the present invention also discloses a propulsion method for a non-equivalent electrode propulsion structure based on the above-mentioned law of electrode erosion. Based on the characteristics of electrode erosion obtained after disassembling the kiln furnace and the characteristics of electrode erosion obtained by simulating the flow field in the kiln furnace, a model for calculating the erosion amount of each electrode block at different temperatures is constructed, and by calculating the propulsion amount of each electrode block during operation, the electrode blocks in the electrode are differentially propelled non-equivalently. In this way, the contact surface between the electrode and the glass liquid is always kept on the same plane and parallel to the pool wall, so that the current distribution in the electrode and the glass liquid is uniformized, and the glass liquid in the kiln furnace is melted uniformly. In addition, the erosion of the pool wall bricks near the electrode by the glass liquid can be further reduced. Based on the constructed model for calculating the erosion amount of each electrode block under different temperature conditions, the length of each electrode block is optimized, the initial length of the electrode block with a large consumption amount is increased, and the initial length of the electrode block with a small consumption amount is shortened, so as to realize the differential length design of the electrode blocks, achieve the efficient utilization of each electrode block, extend the service life of the electrode, and reduce costs. Also, based on the model for calculating the erosion amount of each electrode block under different temperature conditions, electrode blocks with the same or nearly the same erosion amount are taken as one electrode module, and a silver plate module and a propulsion module are designed for each different electrode module, so as to realize the differential propulsion of the electrode blocks and improve the efficiency of electrode propulsion while keeping the contact surface between the electrode and the glass liquid on the same plane at all times.

Brief Description of the Drawings

[0026]

Figure 1

Figure 2

Figure 3

Figure 4

Figure 5

Best Mode for Carrying Out the Invention

[0027] For the convenience of those skilled in the art to better understand the technical solutions of the present invention, the technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention. It is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative labor shall also fall within the protection scope of the present invention.

[0028] It should be noted that the terms "first", "second", etc. in the specification, claims and drawings of the present invention are used to distinguish similar objects and do not represent a specific order or sequence. Where appropriate, these terms are interchangeable, and it should be understood that the embodiments of the present invention can be implemented in an order different from the order described or illustrated herein. Also, the terms "comprising" and "having" and their variants are intended to be inclusive rather than exclusive, for example, a process, method, system, product or device comprising a plurality of steps or elements can include other steps or elements not explicitly listed, or other steps or elements inherent to these processes, methods, products or devices.

[0029] The present invention will be described in more detail below with reference to the drawings.

[0030] Figure 1 is a front view of a non-equal electrode propulsion structure based on the characteristics of electrode erosion according to the present invention. Figure 2 is a side view of a non-equal electrode propulsion structure based on the characteristics of electrode erosion according to the present invention. Figure 3 is a longitudinal sectional view of a non-equal electrode propulsion structure based on the characteristics of electrode erosion according to the present invention. Figure 4 is a schematic view of the structure of an electrode block according to the present invention. As can be seen from these figures, the non-equal electrode propulsion structure based on the characteristics of electrode erosion according to the present invention includes an electrode 1, a silver plate 2 disposed between the electrodes 1, and a propulsion module 4 provided at the rear end of the electrode 1. The electrode 1 includes a plurality of electrode blocks 1-1. The electrode block 1-1 is a rectangular parallelepiped, and a stepped groove 1-11 is provided around the electrode block 1-1. The silver plate 2 includes a plurality of silver plate modules 2-2. The propulsion module 4 includes an electrode module top plate 4-1, a top screw 4-2, and a propulsion bracket 4-3. One end of the top screw 4-2 is fixed to the electrode module top plate 4-1, and the other end of the top screw 4-2 is connected to the propulsion bracket 4-3. The electrode 1 includes a plurality of electrode blocks 1-1. In some cases, a single electrode block 1-1 may be used as one electrode module 1-2, or a plurality of electrode blocks 1-1 may be combined to form one electrode module 1-2. A stepped groove 1-11 is provided around the electrode block 1-1, and the silver plate 2 is fitted into the stepped grooves 1-11 of two electrode blocks 1-1. All the silver plates 2 are connected in series. An electrical flange 3 is installed on the upper part of the silver plate 2. The function of the silver plate 2 is to evenly transmit the current from the electrical flange 3 to each electrode module 1-2, so as to ensure the uniformity of the current distribution in the electrode 1. The silver plate 2 includes a plurality of silver plate blocks 2-1, and the silver plate module 2-1 is designed based on the electrode module 1-2. When a single electrode block 1-1 constitutes the electrode module 1-2, the silver plate module 2-2 is a single silver plate block 2-1. On the other hand, when a plurality of electrode blocks 1-1 are combined to form the electrode module 1-2, the silver plate module 2-2 is composed of a combination of a plurality of silver plate blocks 2-1, and no silver plate 2 is installed in the central region of the silver plate module 2-2 composed of the combination of a plurality of silver plate blocks 2-1.The propulsion module 4 includes a plurality of electrode module top plates 4-1. Each electrode module top plate 4-1 is designed based on the size of the electrode module 1-2, and in the electrode propulsion structure, the plurality of electrode module top plates 4-1 are independent of each other. One end of the top screw 4-2 is insulated and in contact with the electrode module top plate 4-1, and the other end of the top screw 4-2 is connected to the propulsion bracket 4-3, and the propulsion bracket 4-3 is fixed to the ground. Furthermore, cooling air is designed near the electrode 1, which plays a role in dissipating heat from the surface and the surrounding of the electrode 1. The width of the silver plate 2 is designed to be smaller than the depth of the step groove 1-11 around the electrode block 1-1, thereby increasing the contact area between the cooling air and the electrode 1 and making the heat dissipation of the electrode 1 more effective.

[0031] (Example 1) The non-equivalent electrode propulsion structure based on the electrode erosion characteristics of the present invention includes an electrode 1, a silver plate 2 disposed between the electrodes 1, and a propulsion module 4 provided at the rear end of the electrode 1. The electrode 1 is composed of a plurality of electrode blocks 1-1, and the electrode blocks 1-1 with the same or similar erosion amounts constitute one electrode module 1-2. Corresponding silver plate modules 2-2 and propulsion modules 4 are respectively attached to different electrode modules 1-2.

[0032] (Example 2) The non-equivalent electrode propulsion structure based on the characteristics of electrode erosion of the present invention includes an electrode 1, a silver plate 2 disposed between the electrodes 1, and a propulsion module 4 provided at the rear end of the electrode 1. The electrode 1 is composed of a plurality of electrode blocks 1-1, and the electrode blocks 1-1 with the same or similar erosion amounts constitute one electrode module 1-2. Corresponding silver plate modules 2-2 and propulsion modules 4 are respectively attached to different electrode modules 1-2. The electrode module 1-2 is composed of a single electrode block 1-1, and the silver plate module 2-2 is designed based on the electrode module 1-2. The silver plate module 2-2 is also composed of a single silver plate block 2-1. The electrode block 1-1 is a cuboid, and step grooves 1-11 are provided around it. The silver plate block 2-1 is fitted into the step grooves 1-11 of two adjacent electrode blocks 1-1, and all the silver plate blocks 2-1 are connected in series. The propulsion module 4 includes an electrode module top plate 4-1, a top screw 4-2, and a propulsion bracket 4-3 that are sequentially arranged at the rear end of the electrode module 1-2. One end of the top screw 4-2 is insulated and fixed to the electrode module top plate 4-1, the other end of the top screw 4-2 is connected to the propulsion bracket 4-3, and the propulsion bracket 4-3 is fixed to the ground. Cooling air is installed near the electrode 1, and the cooling air promotes the heat dissipation on the surface of the electrode 1 and its surroundings more effectively. An electrical flange 3 is provided at the upper end of the silver plate 2, and by uniformly supplying current from the electrical flange 3 to each electrode module 1-2, the uniformity of the current distribution in the electrode 1 is ensured.

[0033] (Example 3) The non-equivalent electrode propulsion structure based on the characteristics of electrode erosion of the present invention includes an electrode 1, a silver plate 2 disposed between the electrodes 1, and a propulsion module 4 provided at the rear end of the electrode 1. The electrode 1 is composed of a plurality of electrode blocks 1-1, and the electrode blocks 1-1 with the same or similar erosion amounts constitute one electrode module 1-2. Corresponding silver plate modules 2-2 and propulsion modules 4 are respectively attached to different electrode modules 1-2. The electrode module 1-2 is composed of a plurality of electrode blocks 1-1. The silver plate module 2-2 is designed based on the electrode module 1-2, and the silver plate module 2-2 is also composed of a plurality of silver plate blocks 2-1. In the central region of the silver plate module 2-2 formed by combining a plurality of silver plate blocks 2-1, no silver plate block 2-1 is installed. The electrode block 1-1 is a rectangular parallelepiped, and a step groove 1-11 is provided around it. The silver plate block 2-1 is fitted into the step grooves 1-11 of two adjacent electrode blocks 1-1, and all the silver plate blocks 2-1 are connected in series. The width of the silver plate block 2-1 is designed to be smaller than the depth of the step groove 1-11. The propulsion module 4 includes an electrode module top plate 4-1, a top screw 4-2, and a propulsion bracket 4-3 that are sequentially arranged at the rear end of the electrode module 1-2. One end of the top screw 4-2 is insulated and fixed to the electrode module top plate 4-1, the other end of the top screw 4-2 is connected to the propulsion bracket 4-3, and the propulsion bracket 4-3 is fixed to the ground. The electrode module top plate 4-1 is used in combination with the electrode module 1-2. The propulsion module 4 includes a plurality of electrode module top plates 4-1, and each top plate 4-1 is independent of each other. An electrical flange 3 is provided at the upper end of the silver plate 2, and cooling air is arranged near the electrode 1 to further promote the heat dissipation on the surface and around the electrode 1.

[0034] The propulsion method of the non-equivalent electrode propulsion structure based on the characteristics of electrode erosion according to the present invention includes the following steps.

[0035] 1) Based on the electrode erosion rule (characteristics) after decomposing the kiln, in combination with the characteristic analysis of electrode erosion by simulating the flow field in the kiln, a calculation model is constructed to calculate the erosion amount of each electrode block 1-1 under different temperature conditions, and the total erosion amount of each electrode block 1-1 during operation is calculated, that is, the total propulsion amount is calculated.

[0036] 2) Based on the total propulsion amount of each electrode block 1-1, the electrode blocks 1-1 with the same or similar erosion amounts are configured as one electrode module 1-2, and the silver plate module 2-2 and the propulsion module 4 are designed according to different electrode modules 1-2. At the same time, based on the total erosion amount of each electrode block 1-1, the length of each electrode block 1-1 is optimally designed, that is, the initial length of the electrode block 1-1 with a large consumption amount is set long, and conversely, the initial length of the one with a small consumption amount is short.

[0037] 3) Based on the operating life of the disassembled kiln and the total erosion amount of each electrode block 1-1, the daily consumption amount of each electrode block 1-1 is calculated, and in combination with the analysis of electrode erosion characteristics by simulating the flow field in the kiln, the calculated daily consumption amount of each electrode block 1-1 is corrected. The propulsion cycle of the electrode is set to N days, and the electrode consumption amount of each electrode module 1-2 within this cycle is calculated.

[0038] 4) The amount of cooling air is reduced to increase the temperature of the glass liquid around the electrode 1, and based on the electrode consumption amount of each electrode module 1-2 within the cycle, the differential propulsion of the electrode 1 is realized using the propulsion module 4 of the electrode.

[0039] The present invention combines the erosion characteristics of the electrode 1 obtained after the kiln is disassembled with the analysis of the erosion characteristics of the electrode 1 by simulating the flow field in the kiln, constructs a calculation model for the erosion amount of each electrode block 1-1 under different temperature conditions, and calculates the total propulsion amount of each electrode block 1-1 during operation based on the established calculation model for the erosion amount of each electrode block 1-1 of the electrode 1 at different temperatures. Furthermore, based on the established calculation model for the erosion amount of each electrode block 1-1 of the electrode 1 at different temperatures, the length of each electrode block 1-1 is optimally designed, the initial length of the electrode block 1-1 with a large consumption amount is made long, and the initial length of the electrode block 1-1 with a small consumption amount is made short. Based on the calculation model for the erosion amount of each electrode block 1-1 of the electrode at different temperatures, the electrode blocks 1-1 with the same or similar erosion amounts are configured as one electrode module 1-2, and the silver plate module 2-2 and the propulsion module 4 are designed for each different electrode module 1-2 to differentially propel the electrode module 1-2, and improve the propulsion efficiency of the electrode 1 while keeping the contact surface between the electrode 1 and the glass liquid in the same plane.

[0040] The above are only preferred embodiments of the present invention and are not intended to limit the technical solutions of the present invention. Those skilled in the art can make simple modifications and substitutions to the technical solutions of the present invention without departing from the gist and principles of the present invention, and these modifications and substitutions are included within the scope of protection covered by the claims of the present invention.

Explanation of Reference Numerals

[0041] 1 Electrode 1-1 Electrode Block 1-2 Electrode Module 1-11 Step Groove 2 Silver Plate 2-1 Silver Plate Block 2-2 Silver Plate Module 3 Electric Flange 4 Propulsion Module 4-1 Electrode Module Top Plate 4-2 Top Screw 4-3 Propulsion Bracket

Claims

1. The device comprises electrodes (1), silver plates (2) disposed between the electrodes (1), and a propulsion module (4) disposed at the rear end of the electrodes (1), The electrode (1) is composed of a plurality of electrode blocks (1-1), and the electrode blocks (1-1) having the same or similar erosion amount constitute one electrode module (1-2); The different electrode modules (1-2) are respectively equipped with corresponding silver plate modules (2-2) and propulsion modules (4), and the non-equivalent electrode propulsion structure is based on the characteristics of electrode erosion.

2. The non-equal electrode propulsion structure based on the characteristics of electrode erosion as claimed in claim 1, wherein said electrode module (1-2) is composed of a single said electrode block (1-1) or a plurality of said electrode blocks (1-1).

3. The silver plate module (2-2) is designed based on the electrode module (1-2), When a single electrode block (1-1) constitutes one electrode module (1-2), the silver plate module (2-2) is a single silver plate block (2-1); The non-equal electrode propulsion structure based on the characteristics of electrode erosion as described in claim 2, wherein when a plurality of the electrode blocks (1-1) constitute one of the electrode modules (1-2), the silver plate module (2-2) is a combination of a plurality of the silver plate blocks (2-1).

4. The non-equal electrode propulsion structure based on the characteristics of electrode erosion according to claim 3, wherein the silver plate module (2-2) composed of a plurality of the silver plate blocks (2-1) has no silver plate blocks (2-1) installed in the central region.

5. The electrode block (1-1) is a rectangular parallelepiped, and a stepped groove (1-11) is provided around the periphery thereof. The non-equal electrode propulsion structure based on the characteristics of electrode erosion according to claim 1, wherein the silver plate block (2-1) is fitted into the step grooves (1-11) of two adjacent electrode blocks (1-1), and all the silver plate blocks (2-1) are connected in series.

6. 6. The non-equal electrode propulsion structure based on the characteristics of electrode erosion as claimed in claim 5, wherein the width of said silver plate block (2-1) is smaller than the depth of said step groove (1-11).

7. The non-equal electrode propulsion structure based on the characteristics of electrode erosion as described in claim 1, wherein the propulsion module (4) includes an electrode module top plate (4-1), a top screw (4-2), and a propulsion bracket (4-3) sequentially arranged at the rear end of the electrode module (1-2), one end of the top screw (4-2) is fixed to the electrode module top plate (4-1) in an insulating state, the other end of the top screw (4-2) is connected to the propulsion bracket (4-3), and the propulsion bracket (4-3) is fixed to the ground.

8. The electrode module top plate (4-1) is used in combination with the electrode module (1-2), 8. The non-equivalent electrode propulsion structure based on the characteristics of electrode erosion as claimed in claim 7, wherein said propulsion module (4) includes a plurality of said electrode module top plates (4-1), each of which is independent of each other.

9. The non-equal electrode propulsion structure based on the characteristics of electrode erosion as claimed in claim 1, wherein an electrical flange (3) is provided on the upper end of the silver plate (2), and cooling air is provided around the electrode (1).

10. A method for propulsion of a non-equivalent electrode propulsion structure based on the characteristics of electrode erosion according to any one of claims 1 to 9, comprising: Step S1 is a step of constructing an erosion amount calculation model of each electrode block (1-1) of the electrode (1) under different temperature conditions by combining the erosion characteristics of the electrode (1) obtained after dismantling the kiln and the erosion characteristics analysis of the electrode (1) by simulating the flow field in the kiln, and calculating the total erosion amount of each electrode block (1-1) during operation; In step S2, based on the total amount of erosion of each of the electrode blocks (1-1) obtained in step S1, the electrode blocks (1-1) having the same or similar amount of erosion are configured as one electrode module (1-2), corresponding silver plate modules (2-2) and propulsion modules (4) are designed based on the different electrode modules (1-2), and the length of each of the electrode blocks (1-1) is optimally designed according to the total amount of erosion of each of the electrode blocks (1-1), and the initial length of the electrode block (1-1) having a large amount of erosion is made longer and the initial length of the electrode block (1-1) having a small amount of erosion is made shorter; Step S3: based on the operating life of the dismantled furnace and the total erosion amount of each of the electrode blocks (1-1) obtained in step S1, calculate the daily wear amount of each of the electrode blocks (1-1), combine this with an electrode erosion characteristic analysis using a flow field simulation in the furnace to correct the calculated daily wear amount of each of the electrode blocks (1-1), set the electrode thrust cycle to N days, and calculate the electrode wear amount of each of the electrode modules (1-2) for N days; A propulsion method for a non-equal electrode propulsion structure based on the characteristics of electrode erosion, comprising: step S4: realizing differentiated propulsion of the electrode (1) using the propulsion module (4) of the electrode (1) based on the electrode wear amount of each of the electrode modules (1-2) over N days obtained in step S3.

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