Non-equal electrode propulsion structure and method based on the characteristics of electrode erosion

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 the manufacture of 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, differences occur 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 each electrode block in the electrode are the same. Therefore, the interval between electrode blocks with less consumption in each pair of electrodes is narrowed, and 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 life of the entire 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] Conventional overall electrode propulsion systems (also called uniform electrode propulsion systems) have technical problems such as uneven current distribution in the electrodes and glass liquid, high wear of electrode blocks, and susceptibility of pool wall bricks near the electrodes to erosion. In contrast, a new electrode system exists that keeps the contact surface between the electrodes and glass liquid on the same plane at all times, uniformly distributes the current in the electrodes and glass liquid, achieves uniform melting of the glass liquid in the furnace, utilizes each electrode block with high efficiency, and extends the lifespan of the electrodes.

[0005] In other words, in conventional overall electrode propulsion systems, the current distribution between the electrodes and the glass liquid is uneven, leading to high consumption of electrode blocks and susceptibility to erosion of the pool wall bricks near the electrodes. [Means for solving the problem]

[0006] Therefore, in order to overcome the shortcomings of the above-mentioned prior art, the present invention aims to disclose a non-equal electrode propulsion structure and method based on the characteristics of electrode erosion, thereby solving the technical problems that exist in conventional uniform electrode propulsion methods, such as the non-uniform current distribution between the electrode and the glass liquid, the large consumption of electrode blocks, and the susceptibility of pool wall bricks near the electrodes to erosion.

[0007] To achieve the above objective, the present invention employs the following technical means. The present invention discloses an unequal electrode propulsion structure based on electrode erosion characteristics, comprising 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), wherein the electrode (1) is composed of a plurality of electrode blocks (1-1), and electrode blocks (1-1) with the same or similar amount of erosion constitute one electrode module (1-2), and different electrode modules (1-2) are each fitted with a corresponding silver plate module (2-2) and propulsion module (4).

[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), and 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), and when multiple electrode blocks (1-1) constitute one electrode module (1-2), the silver plate module (2-2) is a combination of multiple silver plate blocks (2-1).

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

[0011] Furthermore, the electrode block (1-1) is a rectangular parallelepiped with stepped grooves (1-11) around it, and the silver plate block (2-1) is fitted into the stepped 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 stepped 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 modules (1-2), with one end of the top screw (4-2) insulated and fixed to the electrode module top plate (4-1), and the other end of the top screw (4-2) connected to the propulsion bracket (4-3), which is fixed to the ground.

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

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

[0016] Furthermore, the present invention relates to a propulsion method for an unequal electrode propulsion structure based on the above-mentioned electrode erosion characteristics, and includes the steps of: step S1, constructing a model for calculating the amount of erosion 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 furnace with the analysis of the erosion characteristics of the electrode (1) by simulation of the flow field inside the furnace; and step S2, based on the total amount of erosion of each electrode block (1-1) obtained in step S1, configuring electrode blocks (1-1) with the same or similar amounts of erosion as one electrode module (1-2), designing corresponding silver plate modules (2-2) and propulsion modules (4) based on different electrode modules (1-2), optimally designing the length of each electrode block (1-1) according to the total amount of erosion of each electrode block (1-1), and The present invention discloses a method for propelling an unequal electrode propulsion structure based on electrode erosion characteristics, which includes the steps of: making the initial length of electrode block (1-1) longer and shortening the initial length of electrode block (1-1) with less erosion; as step S3, calculating the daily consumption of each electrode block (1-1) based on the operating life of the dismantled kiln and the total amount of erosion of each electrode block (1-1) obtained in step S1, correcting the calculated daily consumption of each electrode block (1-1) by combining it with electrode erosion characteristic analysis by kiln flow field simulation, setting the electrode propulsion cycle to N days, and calculating the electrode consumption of each electrode module (1-2) over N days; and as step S4, realizing differentiated propulsion of the electrode (1) using the propulsion module (4) of the electrode (1) based on the electrode consumption of each electrode module (1-2) over N days obtained in step S3. [Effects of the Invention]

[0017] The non-equal electrode propulsion structure based on the electrode erosion characteristics according to the present invention provides the following beneficial effects. This invention discloses an unequal electrode propulsion structure based on the law of electrode erosion, and includes: electrodes, silver plates placed between electrodes, and propulsion modules installed at the rear ends of the electrodes for propelling the electrodes. The electrodes are composed of multiple electrode blocks, and electrode blocks with the same or similar amount of erosion constitute one electrode module. Different electrode modules are provided with corresponding silver plate modules and propulsion modules, and different propulsion amounts are set for each different electrode module, making it possible to differentiate the propulsion of the electrode blocks within the electrode by unequal amounts. This makes it possible to keep the contact surface between the electrode and the glass liquid on the same plane and parallel to the pool wall, equalize the current distribution in the electrode and glass liquid, uniformly melt the glass liquid in the furnace, and extend the service life of the electrodes by efficiently utilizing each electrode block.

[0018] Furthermore, the electrode module can consist of a single electrode block or multiple electrode blocks, and adjacent electrode blocks with the same consumption rate can be propelled together.

[0019] Furthermore, the silver plate module is designed based on the electrode module. When a single electrode block constitutes one electrode module, the silver plate module becomes a single silver plate block. When multiple electrode blocks constitute one electrode module, the silver plate module becomes a combination of multiple silver plate blocks. This ensures uniformity of current distribution and mutual independence between electrode modules.

[0020] Furthermore, the electrode blocks are rectangular prisms with stepped grooves around their perimeter, and the silver plate blocks are fitted into the stepped grooves of two adjacent electrode blocks. All silver plate blocks are connected in series, ensuring that the front ends of all electrodes are in close contact.

[0021] Furthermore, the width of the silver plate block is smaller than the depth of the stepped groove, which increases the contact area between the cooling air and the electrodes, contributing to improved heat dissipation from the electrodes.

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

[0023] Furthermore, the electrode module top plates are used in combination with the electrode modules, and the propulsion module contains multiple electrode module top plates, which are independent of each other. During differentiated propulsion, each electrode module is designed not to interfere with the others when it is propelled.

[0024] Furthermore, an electrical flange is provided at the top edge of the silver plate, ensuring a uniform current distribution within the electrodes by having the silver plate evenly transmit the current within the electrical flange to each electrode module. Cooling air is placed near the electrodes, which improves heat dissipation from the electrode surface and its surroundings.

[0025] The present invention also discloses a propulsion method for a non-equivalent electrode propulsion structure based on the above-described law of electrode erosion. Based on the characteristics of electrode erosion obtained after decomposing 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 melts 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 similar erosion amounts are taken as one electrode module, and silver plate modules and propulsion modules are designed for different electrode modules, 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] It is a front view of a non-equivalent electrode propulsion structure based on the characteristics of electrode erosion according to the present invention. [Figure 2] It is a side view of a non-equivalent electrode propulsion structure based on the characteristics of electrode erosion according to the present invention. [Figure 3] It is a longitudinal sectional view of a non-equivalent electrode propulsion structure based on the characteristics of electrode erosion according to the present invention. [Figure 4] It is a schematic diagram of the structure of an electrode block according to the present invention. [Figure 5] It is a schematic diagram of the structure of a propulsion module according to the present invention. [Modes for carrying out the invention]

[0027] To make the technical solutions of the present invention more easily understandable to those skilled in the art, the technical means of the embodiments of the present invention will be described clearly and completely below with reference to the drawings of the embodiments. It is clear that the embodiments described are only a selection of embodiments of the present invention, and not all embodiments. All other embodiments that can be obtained by those skilled in the art without creative work based on the embodiments of the present invention are also within the scope of the protection of the present invention.

[0028] Furthermore, terms such as "first," "second," etc., in the specification and claims of the present invention, as well as in the drawings, are used to distinguish similar subjects and do not represent a specific order or sequence. Where appropriate, these terms are interchangeable, and embodiments of the present invention may be carried out in an order different from that described or illustrated herein. In addition, the terms "includes" and "has" and their variations are intended to be non-exclusive inclusions, for example, a process, method, system, product, or apparatus that includes multiple steps or elements may include other steps or elements not explicitly listed, or other steps or elements specific to those processes, methods, products, or apparatus.

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

[0030] Figure 1 is a front view of the non-equal electrode propulsion structure based on the electrode erosion characteristics according to the present invention. Figure 2 is a side view of the non-equal electrode propulsion structure based on the electrode erosion characteristics according to the present invention. Figure 3 is a longitudinal cross-sectional view of the non-equal electrode propulsion structure based on the electrode erosion characteristics according to the present invention. Figure 4 is a schematic diagram of the structure of the electrode block according to the present invention. As can be seen from these figures, the non-equal electrode propulsion structure based on the electrode erosion characteristics according to the present invention includes an electrode 1, a silver plate 2 arranged between the electrodes 1, and a propulsion module 4 provided at the rear end of the electrode 1. The electrode 1 includes several electrode blocks 1-1, each electrode block 1-1 being a rectangular parallelepiped, with stepped grooves 1-11 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, with one end of the top screw 4-2 fixed to the electrode module top plate 4-1 and the other end of the top screw 4-2 connected to the propulsion bracket 4-3. Electrode 1 includes multiple electrode blocks 1-1, where a single electrode block 1-1 may be used as one electrode module 1-2, or multiple electrode blocks 1-1 may be combined to form one electrode module 1-2. Stepped grooves 1-11 are provided around the electrode blocks 1-1, and silver plates 2 are fitted into the stepped grooves 1-11 of two electrode blocks 1-1, with all silver plates 2 connected in series. An electrical flange 3 is installed on the top of the silver plates 2, and the function of the silver plates 2 is to ensure uniformity of the current distribution within electrode 1 by evenly transmitting the current from the electrical flange 3 to each electrode module 1-2. Silver plates 2 include multiple silver plate blocks 2-1, and silver plate modules 2-1 are designed based on electrode modules 1-2. When a single electrode block 1-1 constitutes electrode module 1-2, the silver plate module 2-2 is a single silver plate block 2-1. On the other hand, when multiple electrode blocks 1-1 are combined to form an electrode module 1-2, the silver plate module 2-2 is composed of a combination of multiple 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 a combination of multiple silver plate blocks 2-1.The propulsion module 4 includes multiple electrode module top plates 4-1, each electrode module top plate 4-1 designed based on the size of electrode modules 1-2, and the multiple electrode module top plates 4-1 are independent of each other in the electrode propulsion structure. 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, which is fixed to the ground. Furthermore, cooling air is designed near the electrode 1, which plays a role in dissipating heat from the surface of the electrode 1 and its surroundings. The width of the silver plate 2 is designed to be smaller than the depth of the stepped groove 1-11 around the electrode block 1-1, thereby increasing the contact area between the cooling air and the electrode 1, and allowing for more effective heat dissipation of the electrode 1.

[0031] (Example 1) The non-equal electrode propulsion structure based on the electrode erosion characteristics of the present invention includes an electrode 1, a silver plate 2 placed 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 electrode blocks 1-1 with the same or similar amount of erosion constitute one electrode module 1-2. Different electrode modules 1-2 are each fitted with a corresponding silver plate module 2-2 and propulsion module 4.

[0032] (Example 2) The non-equal electrode propulsion structure based on the electrode erosion characteristics of the present invention includes an electrode 1, a silver plate 2 arranged 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 electrode blocks 1-1 with the same or similar amount of erosion constitute one electrode module 1-2. Different electrode modules 1-2 are fitted with corresponding silver plate modules 2-2 and propulsion modules 4. Electrode module 1-2 consists of a single electrode block 1-1, and silver plate module 2-2 is designed based on electrode module 1-2. Silver plate module 2-2 also consists of a single silver plate block 2-1. Electrode block 1-1 is a rectangular parallelepiped with stepped grooves 1-11 around its perimeter, and silver plate blocks 2-1 are fitted into the stepped grooves 1-11 of two adjacent electrode blocks 1-1, with all silver plate blocks 2-1 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, which are sequentially arranged at the rear ends of the electrode modules 1-2. One end of the top screw 4-2 is insulated and 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, which is fixed to the ground. Cooling air is installed near the electrode 1, and the cooling air further promotes heat dissipation from the surface of the electrode 1 and its surroundings. An electrical flange 3 is provided at the upper end of the silver plate 2, and by supplying current uniformly from the electrical flange 3 to each electrode module 1-2, uniformity of the current distribution within the electrode 1 is ensured.

[0033] (Example 3) The non-equal electrode propulsion structure based on the electrode erosion characteristics of the present invention includes an electrode 1, a silver plate 2 arranged 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 electrode blocks 1-1 with the same or similar amount of erosion constitute one electrode module 1-2. Different electrode modules 1-2 are fitted with corresponding silver plate modules 2-2 and propulsion modules 4. The electrode module 1-2 is composed of a plurality of electrode blocks 1-1, and 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 blocks 2-1 are installed. The electrode block 1-1 is a rectangular parallelepiped with stepped grooves 1-11 around its periphery, and the silver plate blocks 2-1 are fitted into the stepped grooves 1-11 of two adjacent electrode blocks 1-1, and all 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 stepped 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, which 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, and the other end of the top screw 4-2 is connected to the propulsion bracket 4-3, which is fixed to the ground. The electrode module top plate 4-1 is used in combination with the electrode module 1-2, and the propulsion module 4 includes multiple electrode module top plates 4-1, each top plate 4-1 being independent of the others. An electrical flange 3 is provided at the upper end of the silver plate 2, and cooling air is placed near the electrode 1 to further promote heat dissipation from the surface of the electrode 1 and its surroundings.

[0034] The method for propelling a non-equal 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 laws (characteristics) after disassembling the furnace, a computational model is constructed to calculate the amount of erosion of each electrode block 1-1 under different temperature conditions, by combining this with characteristic analysis of electrode erosion by simulation of the flow field inside the furnace. The total amount of erosion of each electrode block 1-1 during operation is then calculated, i.e., the total amount of propulsion is calculated.

[0036] 2) Based on the total amount of propulsion of each electrode block 1-1, electrode blocks 1-1 with the same or similar amount of erosion are configured as one electrode module 1-2, and silver plate modules 2-2 and propulsion modules 4 are designed to match the different electrode modules 1-2. At the same time, based on the total amount of erosion of each electrode block 1-1, the length of each electrode block 1-1 is optimally designed, that is, the initial length of electrode blocks 1-1 with high wear is made longer, and conversely, the initial length of those with low wear is made shorter.

[0037] 3) Based on the operating life of the dismantled kiln and the total erosion of each electrode block 1-1, the daily consumption of each electrode block 1-1 is calculated, and the calculated daily consumption of each electrode block 1-1 is corrected by combining this with electrode erosion characteristic analysis using kiln flow field simulation. The electrode propulsion cycle is set to N days, and the electrode consumption of each electrode module 1-2 within this cycle is calculated.

[0038] 4) The amount of cooling air is reduced, the temperature of the glass liquid around electrode 1 is increased, and differentiated propulsion of electrode 1 is achieved using electrode propulsion module 4 based on the amount of electrode wear within the cycle of each electrode module 1-2.

[0039] This invention combines the erosion characteristics of electrode 1 obtained after dismantling the furnace with the analysis of the erosion characteristics of electrode 1 by simulation of the flow field inside the furnace to construct an erosion calculation model for each electrode block 1-1 under different temperature conditions. Based on the established calculation model of the erosion amount of each electrode block 1-1 at different temperatures, the total propulsion amount of each electrode block 1-1 during operation is calculated. Furthermore, based on the established calculation model of the erosion amount of each electrode block 1-1 at different temperatures, the length of each electrode block 1-1 is optimally designed, with a longer initial length for electrode blocks 1-1 with high wear and a shorter initial length for electrode blocks 1-1 with low wear. Based on the calculation model of the erosion amount of each electrode block 1-1 at different temperatures, electrode blocks 1-1 with the same or similar erosion amounts are configured as one electrode module 1-2, and a silver plate module 2-2 and a propulsion module 4 are designed for each different electrode module 1-2 to differentiate the propulsion of the electrode modules 1-2, improving the propulsion efficiency of electrode 1 while always maintaining the contact surface between electrode 1 and glass liquid on the same plane.

[0040] The foregoing are merely 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 spirit and principles of the present invention, and such modifications and substitutions are within the scope of the protection covered by the claims of the present invention. [Explanation of Symbols]

[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 Electrical flange 4. Propulsion Module 4-1 Electrode Module Top Plate 4-2 Top Screw 4-3 Propulsion bracket

Claims

1. It 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), the amount of wear of the electrode blocks (1-1) is defined as the amount of erosion, and electrode blocks (1-1) with the same or similar amount of erosion constitute one electrode module (1-2). One electrode module (1-2) is composed of one or more electrode blocks (1-1), and one electrode (1) is composed of multiple electrode modules (1-2), The silver plate (2) consists of a plurality of silver plate modules (2-2), one or more silver plate blocks (2-1) constitute one silver plate module (2-2), one electrode (1) has a plurality of silver plate modules (2-2) attached to it, the silver plate blocks (2-1) are connected in series, and an electrical flange (3) is provided at the upper end of the silver plate (2). One electrode (1) has multiple propulsion modules (4) attached to it. One electrode module (1-2) is fitted with one silver plate module (2-2) and one propulsion module (4), respectively. A non-equal electrode propulsion structure characterized by the following:

2. The silver plate module (2-2) is designed based on the electrode module (1-2), When a single electrode block (1-1) constitutes a single electrode module (1-2), the silver plate module (2-2) is a single silver plate block (2-1), The non-equal electrode propulsion structure according to claim 1, wherein when a plurality of the electrode blocks (1-1) constitute a single electrode module (1-2), the silver plate module (2-2) is a combination of a plurality of the silver plate blocks (2-1).

3. The non-equal electrode propulsion structure according to claim 2, wherein no silver plate block (2-1) is installed in the central region of the silver plate module (2-2) which is composed of a plurality of silver plate blocks (2-1).

4. The electrode block (1-1) is a rectangular parallelepiped, and stepped grooves (1-11) are provided around it. The non-equal electrode propulsion structure according to claim 1, wherein the silver plate block (2-1) is fitted into the stepped grooves (1-11) of two adjacent electrode blocks (1-1).

5. The non-equal electrode propulsion structure according to claim 4, wherein the width of the silver plate block (2-1) is smaller than the depth of the stepped groove (1-11).

6. The non-equal electrode propulsion structure according to 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 modules (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.

7. The electrode module top plate (4-1) is used in combination with the electrode module (1-2). The non-equal electrode propulsion structure according to claim 6, wherein the propulsion module (4) includes a plurality of electrode module top plates (4-1), each of which is independent of the others.

8. The non-equal electrode propulsion structure according to claim 1, wherein cooling air is provided around the electrode (1).

9. A method for propelling a non-equal electrode propulsion structure according to any one of claims 1 to 8, Step S1 involves combining the erosion characteristics of the electrode (1) obtained after dismantling the kiln with the analysis of the erosion characteristics of the electrode (1) by simulation of the flow field inside the kiln to construct a model for calculating the amount of erosion of each electrode block (1-1) of the electrode (1) under different temperature conditions, and calculating the total amount of erosion of each electrode block (1-1) during operation. Step S2 involves configuring electrode blocks (1-1) with the same or similar erosion amounts as one electrode module (1-2) based on the total erosion amount of each electrode block (1-1) obtained in step S1, designing corresponding silver plate modules (2-2) and propulsion modules (4) based on different electrode modules (1-2), optimally designing the length of each electrode block (1-1) according to the total erosion amount of each electrode block (1-1), making the initial length of electrode blocks (1-1) with a large amount of erosion longer and the initial length of electrode blocks (1-1) with a small amount of erosion shorter, Step S3 involves calculating the daily consumption of each electrode block (1-1) based on the operating life of the dismantled kiln and the total erosion amount of each electrode block (1-1) obtained in step S1, correcting the calculated daily consumption amount of each electrode block (1-1) by combining it with electrode erosion characteristic analysis by kiln flow field simulation, setting the electrode propulsion cycle to N days, and calculating the electrode consumption amount of each electrode module (1-2) over N days. A method for propelling an unequal electrode propulsion structure, comprising step S4, which is to realize differentiated propulsion of electrode (1) using the propulsion module (4) of electrode (1) based on the electrode consumption amount of each electrode module (1-2) obtained in step S3 over N days.

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