Electrolyte distribution adjusting device for lead electrolytic cell

CN224798998UActive Publication Date: 2026-09-25YUNNAN ZHENXING IND GRP
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Patent Information

Application Number
CN202522364260.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-11-07
Publication Date
2026-09-25
Estimated Expiration
2035-11-07

AI Technical Summary

Technical Problem

[0004]为了弥补以上不足,本实用新型提供了一种铅电解洗槽用电解液分配调整装置,旨在解决现有技术中,电解槽中电解液成分波动的问题

Benefits of technology

本实用新型中,通过将中转槽分隔为四个相同的容积的小槽,分别进行编号,这样从电解槽输送到中转槽中的电解液能进行分别存放,通过测定电解液中各元素的含量,然后进行调整,调整完成以后输送回电解槽中。

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the field of lead smelting technology discloses a kind of electrolyte distribution adjustment devices for lead electrolysis washing tank, including base, electrolytic cell, its characterized is: electrolytic cell is arranged side by side, and one liquid distribution tank is fixed in the top of two adjacent electrolytic cells, and several liquid distribution pipes are arranged in the both sides of liquid distribution tank, and the other end of liquid distribution pipe is arranged in the upper portion of electrolytic cell, and the lower end of electrolytic cell is provided with drain main pipe, and several branch pipes are arranged on drain main pipe, and the other end of branch pipe is arranged in the lower portion of electrolytic cell and penetrates electrolytic cell, and drain main pipe is also provided with drain pump, and the other end of drain main pipe is arranged in the upper portion of transfer tank, and transfer tank is installed in the upper portion of base, and transfer tank is divided into four intervals with same volume by partition, and transfer tank is provided with liquid feeding pipe in one end, and liquid feeding pump is arranged on liquid feeding pipe, and the other end of liquid feeding pipe is arranged in the upper portion of liquid distribution tank, can effectively temporarily store electrolyte in electrolytic cell, and adjust element content therein.
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Description

Technical Field

[0001] This utility model relates to the field of lead smelting technology, and in particular to an electrolyte distribution and adjustment device for a lead electrolytic washing tank. Background Technology

[0002] As the electrolysis cycle extends, the anode mud at the bottom of the electrolytic cell gradually increases, which in turn affects the yield and quality of precipitated lead. Therefore, the wet process workshop will carry out a washing operation after a certain period of electrolysis. Generally, it is washed once every 3-5 months. The more anode mud falls into the cell, the shorter the cycle is, and the less it falls into the cell, the longer the cycle is. The washing time is generally about 10 days.

[0003] Due to the unstable source of crude lead, the antimony content in crude lead tends to be low. During the electrolysis process, the anode mud is not properly attached to the plate and falls into the tank too much, resulting in large fluctuations in the composition of the electrolyte, which in turn affects the quality of the deposited lead. Utility Model Content

[0004] To overcome the above deficiencies, this utility model provides an electrolyte distribution and adjustment device for lead electrolytic washing tanks, which aims to solve the problem of electrolyte composition fluctuation in electrolytic tanks in the prior art.

[0005] To achieve the above objectives, the present invention adopts the following technical solution: an electrolyte distribution and adjustment device for a lead electrolytic washing tank, comprising a base and an electrolytic tank, characterized in that: the electrolytic tanks are arranged side by side, a dispensing tank is fixed at the top of two adjacent electrolytic tanks, several dispensing pipes are arranged on both sides of the dispensing tank, the other end of the dispensing pipes is arranged at the upper part of the electrolytic tank, a main drain pipe is arranged at the lower end of the electrolytic tank, several branch pipes are arranged on the main drain pipe, the other end of the branch pipes is arranged at the lower part of the electrolytic tank and penetrates the electrolytic tank, a drain pump is also arranged on the main drain pipe, the other end of the main drain pipe is arranged at the upper part of the transfer tank, the transfer tank is installed on the upper part of the base, the transfer tank is divided into four sections of the same volume by a partition plate, a delivery pipe is arranged at one end of the transfer tank, a delivery pump is arranged on the delivery pipe, and the other end of the delivery pipe is arranged at the upper part of the dispensing tank.

[0006] As a further description of the above technical solution: The transfer tank is coated with an anti-corrosion paint layer inside, and reinforced with ribs on the outside. A sludge discharge pipe is installed at the bottom of the transfer tank, and a sludge discharge pump is installed at the top of the sludge discharge pipe.

[0007] As a further description of the above technical solution: The base is fixedly equipped with columns around its perimeter, with a canopy on top of the columns, and a cofferdam on the outside of the base.

[0008] As a further description of the above technical solution: The transfer trough measures 8.5 meters, 8 meters, and 1.5 meters, with two overflow outlets located in the middle of the transverse partition plate.

[0009] This utility model has the following beneficial effects: In this invention, the transfer tank is divided into four smaller tanks of the same volume and numbered accordingly. This allows the electrolyte transported from the electrolytic cell to the transfer tank to be stored separately. The content of each element in the electrolyte is measured and then adjusted. After adjustment, the electrolyte is transported back to the electrolytic cell. Attached Figure Description

[0010] Figure 1 This is a schematic diagram of the structure of this utility model; Figure 2 This is a schematic diagram of the liquid preparation tank structure of this utility model; Figure 3 This is a schematic diagram of the transfer trough structure of this utility model; Figure 4 This is a schematic diagram of the transfer trough partition structure of this utility model; Figure 5 This is a schematic diagram of the reinforcing rib structure of the transfer trough in this utility model. Detailed Implementation

[0011] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.

[0012] Reference Figure 1 — Figure 5This utility model provides an embodiment of an electrolyte distribution and adjustment device for a lead electrolytic washing tank, comprising a base 13 and an electrolytic tank 1. The electrolytic tanks 1 are arranged side-by-side, with a dispensing tank 4 fixed to the top of each adjacent electrolytic tank 1. Several dispensing pipes 12 are arranged on both sides of the dispensing tank 4, with the other end of each dispensing pipe 12 positioned above the electrolytic tank 1. A main drain pipe 3 is located at the lower end of the electrolytic tank 1, with several branch pipes 2 arranged on the main drain pipe 3. The other end of each branch pipe 2 is positioned below the electrolytic tank 1 and penetrates it. A drain pump 5 is also installed on the main drain pipe 3, with the other end of the main drain pipe 3 positioned above a transfer tank 6. The transfer tank 6 is mounted on the upper part of the base 13. Divided into four equal-volume sections by partition 18, the transfer tank 6 is equipped with a liquid delivery pipe 10 at one end, a liquid delivery pump 11 on the liquid delivery pipe 10, and the other end of the liquid delivery pipe 10 is located on the upper part of the liquid distribution tank 4. The interior of the transfer tank 6 is coated with an anti-corrosion paint layer 17, and the exterior of the transfer tank 6 is equipped with reinforcing ribs 7. The lower part of the transfer tank 6 is equipped with a sludge discharge pipe 8, and the upper part of the sludge discharge pipe 8 is equipped with a sludge discharge pump 9. The base 13 is fixedly equipped with columns 15 around its perimeter, and a canopy 16 is provided on the top of the columns 15. A dike 14 is provided on the outside of the base 13. The dimensions of the transfer tank 6 are 8.5 meters * 8 meters * 1.5 meters. Two overflow ports 19 are opened in the middle of the transverse partition 18 of the transfer tank 6.

[0013] During construction, the foundation 13 was poured first. The foundation has an area of ​​110 square meters and a load-bearing capacity of 110 tons. A transfer trough 6 was welded onto the foundation 13, and reinforcing ribs 7 were welded onto the exterior of the transfer trough 6 using channel steel. After the transfer trough 6 was completed, pipelines were laid and equipment was installed. The transfer trough 6, measuring 8.5 meters * 8 meters * 1.5 meters, was constructed on the foundation 13, divided into four equal sections: temporary storage tanks #1, #2, #3, and #4. Each tank has a capacity of 25 m³, for a total capacity of 100 m³, used to transfer the electrolyte used for daily tank washing.

[0014] The electrolyte from the daily washing of the electrolysis tanks in workshops #1 and #3, along with the anode mud, is pumped to temporary storage tank #2. After the electrolyte in temporary storage tank #2 is clarified, the supernatant is pumped to temporary storage tank #1. The electrolyte in temporary storage tank #1 is pumped to low-level tank #1 and returned to the electrolysis system. The anode mud at the bottom of temporary storage tank #2 is pumped to the anode mud cylinder and fed into the filter press.

[0015] Similarly, the electrolyte from the daily washing of the electrolysis tanks in workshops #2 and #4, along with the anode mud, is pumped to temporary storage tank #3. After the electrolyte in temporary storage tank #3 is clarified, the supernatant is pumped to temporary storage tank #4. The electrolyte in temporary storage tank #4 is pumped to low-level tank #2 and returned to the electrolysis system. The anode mud at the bottom of temporary storage tank #3 is pumped to the anode mud cylinder and fed into the filter press.

[0016] Meanwhile, in order to keep the electrolyte in the electrolysis system clean, filter racks are added above the No. 1 and No. 4 temporary storage tanks. The filter racks are lined with filter cotton to filter particulate impurities in the electrolyte. The electrolyte from the No. 1 and No. 2 low-level cells is pumped through the filter racks to the No. 1 and No. 4 temporary storage tanks respectively. The filtered electrolyte is then pumped to the No. 1 and No. 2 high-level cells and returned to the electrolysis system.

[0017] Finally, it should be noted that the above description is only a preferred embodiment of the present utility model and is not intended to limit the present utility model. Although the present utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions described in the foregoing embodiments or make equivalent substitutions for some of the technical features. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present utility model should be included within the protection scope of the present utility model.

Claims

1. An electrolyte distribution and adjustment device for a lead electrolytic washing tank, comprising a base (13) and an electrolytic tank (1), characterized in that: Electrolytic cells (1) are arranged side by side. A liquid distribution tank (4) is fixed on the top of two adjacent electrolytic cells (1). Several liquid distribution pipes (12) are arranged on both sides of the liquid distribution tank (4). The other end of the liquid distribution pipe (12) is arranged on the upper part of the electrolytic cell (1). A main drain pipe (3) is arranged at the lower end of the electrolytic cell (1). Several branch pipes (2) are arranged on the main drain pipe (3). The other end of the branch pipe (2) is arranged at the lower part of the electrolytic cell (1) and passes through the electrolytic cell (1). A drain pump (5) is also installed on the drain main pipe (3). The other end of the drain main pipe (3) is located on the upper part of the transfer tank (6). The transfer tank (6) is installed on the upper part of the base (13). The transfer tank (6) is divided into four sections of the same volume by the partition plate (18). A liquid delivery pipe (10) is installed on one end of the transfer tank (6). A liquid delivery pump (11) is installed on the liquid delivery pipe (10). The other end of the liquid delivery pipe (10) is located on the upper part of the liquid distribution tank (4).

2. The electrolyte distribution and adjustment device for a lead electrolytic washing tank according to claim 1, characterized in that: The transfer tank (6) is coated with an anti-corrosion paint layer (17) inside, and is provided with reinforcing ribs (7) on the outside of the transfer tank (6). A mud discharge pipe (8) is provided at the bottom of the transfer tank (6), and a mud discharge pump (9) is provided at the top of the mud discharge pipe (8).

3. The electrolyte distribution and adjustment device for a lead electrolytic washing tank according to claim 1, characterized in that: The base (13) is fixedly provided with columns (15) around its perimeter, with a canopy (16) on the top of the columns (15) and a cofferdam (14) on the outside of the base (13).

4. The electrolyte distribution and adjustment device for a lead electrolytic washing tank according to claim 1, characterized in that: The transfer trough (6) has dimensions of 8.5m*8m*1.5m. Two overflow ports (19) are opened in the middle of the transverse partition plate (18) of the transfer trough (6). The width of the overflow ports (19) is 50cm.