Utilization system for recycling lead sulfate

By introducing a lead mud filter press into the lead sulfate treatment system, the problems of low acid recovery rate, large waste of lead resources and serious environmental pollution in the prior art are solved, and efficient recycling and recycling of lead mud and acid are achieved, achieving the purpose of energy conservation and environmental protection.

CN222984244UActive Publication Date: 2025-06-17CHENZHOU NAIPU POWER SUPPLY CO LTD
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Patent Information

Application Number
CN202422022878.7
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-08-20
Publication Date
2025-06-17
Estimated Expiration
2034-08-20

AI Technical Summary

Technical Problem

The existing lead sulfate treatment methods have problems such as low acid recovery rate, large waste of lead resources and serious environmental pollution.

Method used

The system including a recycling box, a mixing tank, a lead mud filter press and an acid box is adopted. The lead mud filter press is used to carry out the filter press of lead sulfate to achieve effective separation and recycling of lead sludge and acid liquid.

Benefits of technology

The recovery rate of lead sludge and acid in lead sulfate is improved, resource waste and environmental pollution are reduced, and energy-saving and environmentally friendly results are achieved.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model provides a utilization system for recycling lead sulfate, which comprises a recycling box, a stirring tank, a lead slime filter press and an acid box, the recycling box is arranged at the positions of an acid spraying roller and a wringing roller of a plate coating machine, a lead slime feeding conveying pipe is arranged between the recycling box and the stirring tank, a lead slime conveying pump is fixed on the lead slime feeding conveying pipe, and the acid box is arranged on the stirring tank. Lead sulfate collected in the recycling box is pumped to the stirring tank through a lead slime conveying pump and a lead slime feeding conveying pipe, a lead slime discharging conveying pipe is arranged between the stirring tank and the lead slime filter press, a first diaphragm pump is fixed to the lead slime discharging conveying pipe, a material receiving barrel is placed below the lead slime filter press, and a second diaphragm pump is fixed to the material receiving barrel. Lead slime cakes obtained after filter pressing of the lead slime filter press fall into a material receiving barrel below the lead slime filter press, and an acid liquor conveying pipe is arranged between the lead slime filter press and the acid box. The lead slime utilization system is simple in component composition, ensures timely recovery of lead slime, reduces residence time of the lead slime in a production field, reduces waste of resources, and is not easy to cause lead pollution.
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Description

Technical Field

[0001] The utility model relates to the technical field of battery production, in particular to a utilization system for lead sulfate recovery. Background Art

[0002] During the process of acid drenching of battery plates, about 3% or less of the lead paste on the plate surface and the frame is washed away with the acid drenching. These washed-away lead sludges will generate a large amount of lead sulfate due to being soaked in dilute sulfuric acid.

[0003] In the prior art, the common treatment method for lead sulfate is usually to place a recovery box at the acid drenching roller to collect the waste acid and the lead sludges washed away by the acid during the acid drenching process. Since the lead sludges are soaked in dilute sulfuric acid, the mixture of dilute sulfuric acid and lead sludges in the recovery box is placed at room temperature and undergoes long-term precipitation in the recovery box. The upper-layer acid drenching liquid will be pumped away by the operator at any time for the recycling of dilute sulfuric acid. After the first precipitation is completed, the lead sulfate generated on the same day is fished up with acid-resistant tools and then handed over to a waste recycling unit with the qualification to dispose of lead-containing waste materials for treatment.

[0004] The existing treatment method for lead sulfate has the following deficiencies:

[0005] 1) When using the physical precipitation method, there will be excess acidic liquid that can be recycled in the lead sludges, the recovery rate of the acid liquid is low, and the acid liquid cannot be well treated;

[0006] 2) The existing treatment method wastes a large amount of lead. The lead sludges and acid liquid cannot be well treated, which also causes great waste of resources and increases the production cost of the manufacturer;

[0007] 3) The mixture of dilute sulfuric acid and lead sludges undergoes long-term precipitation in the recovery box, and the formed precipitate is solid waste acid-drenched lead sludges. The solid waste acid-drenched lead sludges are hazardous solid wastes, which are very easy to pollute the environment, and when handed over to the waste recycling unit, it is easy to pollute the environment during the loading, unloading and transportation processes. Content of the Utility Model

[0008] In view of this, to solve the technical problems existing in the prior art, the utility model provides a utilization system with simple component composition, which can ensure the timely recovery of lead sludges, reduce the residence time of lead sludges at the production site, and can make the waste acid and lead sludges be well separated and recycled by using a lead sludge filter press, so that the lead sludges and acid liquid in lead sulfate can be recycled, improve the recovery rate of lead sludges and acid liquid in lead sulfate, reduce waste of resources, and are not easy to cause lead pollution, with good energy-saving and environmental protection effects.

[0009] The utility model solves the above technical problems through the following technical solutions:

[0010] A utilization system for lead sulfate recovery, including a utilization system for lead sulfate recovery on the upper plate of a pasting machine. The utilization system includes a recovery tank, a stirring tank, a lead sludge filter press, and an acid tank;

[0011] The recovery tank is placed at the acid spraying roller and the water squeezing roller of the pasting machine, and the recovery tank is used to collect lead sulfate during the acid spraying process of the plate;

[0012] A lead sludge feeding and conveying pipe is arranged between the recovery tank and the stirring tank. A lead sludge conveying pump is fixed on the lead sludge feeding and conveying pipe. One end of the lead sludge feeding and conveying pipe is communicated with the recovery tank, and the other end of the lead sludge feeding and conveying pipe is communicated with the stirring tank. The lead sulfate collected in the recovery tank is pumped to the stirring tank through the lead sludge conveying pump and the lead sludge feeding and conveying pipe;

[0013] The stirring tank is used for stirring lead sulfate;

[0014] A lead sludge discharging and conveying pipe is arranged between the stirring tank and the lead sludge filter press. A first diaphragm pump is fixed on the lead sludge discharging and conveying pipe. One end of the lead sludge discharging and conveying pipe is communicated with the stirring tank, and the other end of the lead sludge discharging and conveying pipe is communicated with the lead sludge filter press;

[0015] A receiving bucket is placed below the lead sludge filter press. The lead sulfate after being stirred in the stirring tank is pumped to the lead sludge filter press for pressure filtration to obtain a lead sludge cake and acid liquor. The lead sludge cake obtained after the pressure filtration of the lead sludge filter press drops into the receiving bucket below it;

[0016] An acid liquor conveying pipe is arranged between the lead sludge filter press and the acid tank. One end of the acid liquor conveying pipe is connected with the lead sludge filter press, and the other end of the acid liquor conveying pipe is connected with the acid tank.

[0017] Further, the lead sludge filter press includes a frame and a pressing drive mechanism, a pressing plate, a plurality of pressing filter plates, and a thrust plate that are sequentially fixed on the frame from left to right. The plurality of pressing filter plates are spaced apart from each other. The pressing plate and the thrust plate are symmetrically distributed on both sides of the plurality of pressing filter plates. One end of the pressing drive mechanism is connected to the other side of the pressing plate. An inlet channel is arranged above the plurality of pressing filter plates, and an inlet hole is provided at the top of each pressing filter plate. The output end of the inlet channel is communicated with the inlet hole of the pressing filter plate.

[0018] Further, the pressing drive mechanism includes a drive motor and a hydraulic cylinder. The drive motor is connected with the hydraulic cylinder, and the telescopic arm of the hydraulic cylinder is connected with the pressing plate.

[0019] Further, a discharging cavity is formed inside each pressing filter plate. A through hole is provided in the middle of each pressing filter plate. Each pressing filter plate is sleeved on the telescopic arm of the hydraulic cylinder through the through hole in the middle. Liquid outlets are provided on both sides of each pressing filter plate. The lead sludge filter press includes a liquid outlet pipe, which is fixed to the frame and communicates with the liquid outlets on both sides of the pressing filter plate.

[0020] Further, the mixing tank includes a first stirring motor and a first stirring rod. The first stirring rod is fixed inside the mixing tank. The first stirring motor is fixed on the top of the mixing tank. The rotating end of the first stirring motor is arranged downward. The top end of the first stirring rod passes through the top of the mixing tank and is connected to the rotating end of the first stirring motor. A plurality of first stirring blades are fixed on the first stirring rod, and the plurality of first stirring blades are spaced apart from each other along the outer circumference of the first stirring rod.

[0021] Further, a guiding plate is fixed to the inner wall of the mixing tank. One end of the lead sludge discharging and conveying pipe communicates with the bottom of the mixing tank, and the other end of the lead sludge discharging and conveying pipe communicates with the lead sludge filter press.

[0022] Further, a float level controller is arranged inside the mixing tank. The float level controller includes a float and a connecting rod. One end of the connecting rod is connected to the float. A level induction switch is provided at the top end of the mixing tank. The level induction switch is arranged above the highest surface of the mixing tank. The level induction switch is electrically connected to the lead sludge delivery pump. The other end of the connecting rod is located below the level induction switch.

[0023] Further, the acid tank includes a second stirring motor and a second stirring rod. The second stirring rod is fixed inside the acid tank. The second stirring motor is fixed above the acid tank. The rotating end of the second stirring motor is arranged downward. The top end of the second stirring rod passes through the top of the acid tank and is connected to the rotating end of the second stirring motor. A plurality of second stirring blades are fixed on the second stirring rod, and the plurality of second stirring blades are spaced apart from each other along the outer circumference of the second stirring rod.

[0024] Compared with the prior art, the technical solution of the present utility model has at least the following beneficial effects:

[0025] The utilization system of the present utility model includes a recycling box, a stirring tank, a lead sludge filter press, and an acid tank. The recycling box is placed at the acid spraying roller of the plate coating machine. The recycling box is used to collect lead sulfate during the acid spraying process of the electrode plate. A lead sludge feeding and conveying pipe is arranged between the recycling box and the stirring tank, and a lead sludge conveying pump is fixed on the lead sludge feeding and conveying pipe. The lead sulfate collected in the recycling box is pumped to the stirring tank through the lead sludge conveying pump and the lead sludge feeding and conveying pipe. The stirring tank is used for stirring lead sulfate. A lead sludge discharging and conveying pipe is arranged between the stirring tank and the lead sludge filter press, and a first diaphragm pump is fixed on the lead sludge discharging and conveying pipe. A receiving bucket is placed below the lead sludge filter press, and the lead sludge cake obtained after the lead sludge filter press performs pressure filtration drops into the receiving bucket below it; an acid liquid conveying pipe is arranged between the lead sludge filter press and the acid tank. The utilization system of the present utility model has simple component composition, can ensure the timely recycling of lead sludge, reduce the residence time of lead sludge at the production site, and can make both waste acid and lead sludge be well separated and recycled by using the lead sludge filter press, enabling the lead sludge and acid liquid in lead sulfate to be recycled, improving the recovery rate of lead sludge and acid liquid in lead sulfate, reducing waste of resources, not easily causing lead pollution, and having good energy conservation and environmental protection effects.

[0026] The above description is only an overview of the technical solution of the present utility model. In order to be able to understand the technical means of the present utility model more clearly, it can be implemented according to the content of the specification. And in order to make the above and other purposes, features and advantages of the present utility model more obvious and understandable, the following is described in detail in combination with preferred embodiments and with reference to the drawings. Brief Description of the Drawings

[0027] Figure 1 It is a system diagram for the recovery of lead sulfate of the present utility model;

[0028] Figure 2 It is a detailed schematic diagram of the stirring tank of the present utility model;

[0029] Figure 3 It is a detailed schematic diagram of the acid tank of the present utility model;

[0030] Figure 4 It is a schematic diagram of the float liquid level controller of the present utility model touching the liquid level induction switch;

[0031] Figure 5 It is a structural schematic diagram of the lead sludge filter press of the present utility model;

[0032] Figure 6 It is a structural schematic diagram of the pressing filter plate of the present utility model.

[0033] In the figure: recovery tank 1, lead sludge feed conveying pipe 11, lead sludge conveying pump 12, mixing tank 2, first mixing motor 21, first mixing rod 22, first mixing blade 221, material guiding plate 23, lead sludge discharge conveying pipe 24, float level controller 25, float 251, connecting rod 252, inclined plane 253, liquid level induction switch 26, first diaphragm pump 27, lead sludge filter press 3, frame 31, pressing filter plate 32, feed hole 321, through hole 322, discharging cavity 323, feed channel 33, pressing drive mechanism 34, drive motor 341, hydraulic cylinder 342, liquid outlet pipe 35, pressing plate 36, thrust plate 37, receiving bucket 4, acid tank 5, second mixing motor 51, second mixing rod 52, second mixing blade 53, acid liquid discharge pipe 6, coating machine 7, acid spraying roller 71, water squeezing roller 72, acid liquid recovery pipe 8, second diaphragm pump 81. Detailed implementation mode

[0034] The present invention will be described in detail below in conjunction with the accompanying drawings. As a part of this specification, the principles of the present invention are illustrated through embodiments. Other aspects, features, and advantages of the present invention will become apparent through this detailed description. In the accompanying drawings referred to, the same or similar components in different figures are denoted by the same reference numerals.

[0035] As Figure 1-2 shown, Embodiment 1 of the present invention provides a utilization system for lead sulfate recovery, including a utilization system for upper plate lead sulfate recovery on the coating machine 7. This utilization system includes a recovery tank 1, a mixing tank 222, a lead sludge filter press 3, and an acid tank 5;

[0036] The recovery tank 1 is placed at the acid spraying roller 71 and the water squeezing roller 72 of the coating machine 7. The recovery tank 1 is used to collect lead sulfate during the acid spraying process of the plates.

[0037] A lead mud feeding and conveying pipe 11 is arranged between the recovery box 1 and the stirring tank 222, and a lead mud conveying pump 12 is fixed on the lead mud feeding and conveying pipe 11. One end of the lead mud feeding and conveying pipe 11 is connected with the recovery box 1, and the other end of the lead mud feeding and conveying pipe 11 is connected with the stirring tank 222. In specific implementation, a lead mud inlet is arranged at the top of the stirring tank 222, and the other end of the lead mud feeding and conveying pipe 11 is connected with the lead mud inlet of the stirring tank 222. The lead sulfate collected in the recovery box 1 is pumped to the stirring tank 222 through the lead mud conveying pump 12 and the lead mud feed conveying pipe 11; the stirring tank 222 of the utility model is used to stir the lead sulfate and suspend the lead sulfate, that is, to obtain the lead-containing suspended acid liquid, a lead mud discharge conveying pipe 24 is arranged between the stirring tank 222 and the lead mud filter press 3, a first diaphragm pump 27 is fixed on the lead mud discharge conveying pipe 24, one end of the lead mud discharge conveying pipe 24 is connected to the stirring tank 222, and the other end of the lead mud discharge conveying pipe 24 is connected to the stirring tank 222. It is connected with the lead mud filter press 3; a receiving bucket 4 is placed below the lead mud filter press 3, and the lead sulfate stirred in the stirring tank 222 is pumped to the lead mud filter press 3 for filtration to obtain lead mud cake and acid liquid, and the lead mud filter press 3 separates the acid liquid in the lead sulfate from the lead mud, and the lead mud cake obtained after filtration by the lead mud filter press 3 falls into the receiving bucket 4 below it; an acid liquid delivery pipe is provided between the lead mud filter press 3 and the acid tank 5, one end of the acid liquid delivery pipe is connected to the lead mud filter press 3, and the other end of the acid liquid delivery pipe is connected to the acid tank 5.

[0038] The utilization system of the utility model can recycle and reprocess the scrap lead sulfate generated by the plate coating machine 7. The utilization system is simple and reduces the investment of production cost. It not only realizes the recovery of lead sulfate, but also avoids secondary pollution of the environment, effectively reduces the pollution to the environment, and realizes green recovery. The lead sulfate is filtered by the lead mud filter press 3, which can effectively separate the useful lead components in the lead sulfate from the acid solution, greatly improve the recovery rate of lead sulfate, and can effectively solve the problems of environmental pollution caused by lead sulfate, high recovery cost and large floor space. The system is reasonably designed, which can improve the recovery rate of lead mud and acid solution and achieve the purpose of energy saving and environmental protection.

[0039] In specific implementation, the material receiving barrel 4 can be placed in the curing chamber, and the curing chamber dries the material receiving barrel 4 containing the lead mud cake. A grinder is set at the next station in the curing chamber, and a feeding belt is set between the grinder and the curing chamber. One end of the feeding belt is connected to the outlet of the curing chamber, and the other end of the feeding belt is connected to the grinder. The lead mud cake solidified in the curing chamber is sent to the grinder via the feeding belt, and is ground into lead powder by the grinder. The lead powder is sieved by a vibrating screen, and the vibrating screen is used to screen the lead powder within 100 mm. The qualified lead powder obtained after sieving is re-conveyed to the paste mixing machine and mixed with the lead powder to be used for lead paste, and the lead powder mixture is mixed into lead paste for use by the subsequent plate coating machine 7.

[0040] likeFigure 3 As shown in the figure, the acid tank 5 of the present utility model includes a second stirring motor 51 and a second stirring rod 52. The second stirring rod 52 is fixed inside the acid tank 5, and the second stirring motor 51 is fixed above the acid tank 5. The rotating end of the second stirring motor 51 is arranged downward. The top end of the second stirring rod 52 passes through the top of the acid tank 5 and is connected to the rotating end of the second stirring motor 51. A number of second stirring blades 53 are fixed on the second stirring rod 52, and the number of second stirring blades 53 are distributed at intervals along the outer circumference of the second stirring rod 52. The second stirring motor 51 above the acid tank 5 drives the second stirring rod 52 to rotate, thereby stirring the acid liquid in the acid tank 5. The stirring speed is 160 - 180 revolutions per minute, and the stirring time is 25 - 50 minutes. Specifically, a second diaphragm pump 81 is fixed on the acid liquid delivery pipe. One end of the acid liquid delivery pipe is connected to the acid tank 5, and the other end is connected to the coating machine 7. The second diaphragm pump 81 is used to pump the acid liquid formed after stirring in the acid tank 5 to the coating machine 7 for reuse.

[0041] Between the acid tank 5 and the acid spraying roller 71 of the coating machine 7 of the present utility model, there is an acid liquid recovery pipe 8 and a second diaphragm pump 81. The second diaphragm pump 81 is installed on the acid liquid recovery pipe 8. One end of the acid liquid recovery pipe 8 is connected to the acid tank 5, and the other end is connected to the coating machine 7. The second diaphragm pump 81 is used to pump the acid liquid formed after stirring in the acid tank 5 to the acid spraying roller 71 of the coating machine 7 for reuse.

[0042] As Figure 4 shown, specifically, a float level controller 25 is provided inside the stirring tank 222. The float level controller 25 includes a float 251 and a connecting rod 252. One end of the connecting rod 252 is connected to the float 251. A liquid level induction switch 26 is provided at the top of the stirring tank 222. The liquid level induction switch 26 is arranged above the highest surface of the stirring tank 222. The liquid level induction switch 26 is electrically connected to the lead sludge delivery pump 12. The other end of the connecting rod 252 is located below the liquid level induction switch 26. In this embodiment, the contact surface between the connecting rod 252 and the liquid level induction switch 26 is an inclined surface 253 with a higher left side and a lower right side. The higher left contact point corresponds to the energized state of the liquid level induction switch 26, and the lower right contact point corresponds to the de-energized state of the liquid level induction switch 26. The connecting rod 252 is extended to the top of the stirring tank 222. One end of the connecting rod 252 is connected to the float 251, and the other end of the connecting rod 252 is located below the liquid level induction switch 26. When lead sulfate enters the stirring tank 222, the float 251 moves upward as the level of lead sulfate rises. When the level inside the stirring tank 222 reaches a certain height, the other end of the connecting rod 252 on the float 251 will touch the liquid level induction switch 26. When a certain buoyancy is reached, the liquid level induction switch 26 will deflect under the action of the connecting rod 252 and then cut off the power, thereby controlling the lead sludge delivery pump 12 to stop delivering lead sulfate into the stirring tank 222.

[0043] As Figure 5-6 shown, in specific implementation, the lead sludge filter press 3 of the present utility model includes a frame 31, a pressing drive mechanism 34, a pressing plate 36, a plurality of pressing filter plates 32, and a thrust plate 37 that are fixedly arranged on the frame 31 in sequence from left to right. The plurality of pressing filter plates 32 are distributed at intervals. The pressing plate 36 and the thrust plate 37 are symmetrically distributed on both sides of the plurality of pressing filter plates 32. One end of the pressing drive mechanism 34 is connected to the pressing plate 36. An inlet channel 33 is arranged above the plurality of pressing filter plates 32. An inlet hole is arranged at the top end of each pressing filter plate 32. The output end of the inlet channel 33 is communicated with the inlet hole of the pressing filter plate 32. The plurality of pressing filter plates 32 are sleeved on the pressing drive mechanism 34. Among them, the pressing drive mechanism 34 includes a drive motor 341 and a hydraulic cylinder 342. The drive motor 341 is connected to the hydraulic cylinder 342. The telescopic arm of the hydraulic cylinder 342 is connected to the pressing plate 36. The lead sulfate in the stirring tank 222 is transported to the inlet channel 33 through the first diaphragm pump 27 and the lead sludge discharge conveying pipe 24, and is transported to the plurality of pressing filter plates 32 by the inlet channel 33. The drive motor 341 drives the hydraulic cylinder 342 to extend. During the extension of the hydraulic cylinder 342, the pressing plate 36 will be pushed, and the plurality of pressing filter plates 32 will be squeezed together by the pressing plate 36, so as to press the lead-containing suspension acid liquid fed into the pressing filter plates 32 into lead sludge cakes, and the acid liquid is discharged, realizing the solid-liquid separation of the lead sludge and the acid liquid in the lead sulfate. After the pressure filtration is completed, the drive motor 341 drives the hydraulic cylinder 342 to retract, and then the adjacent two pressing filter plates 32 are separated, and the lead sludge cakes between the pressing filter plates 32 will fall into the receiving bucket 4.

[0044] In this embodiment, a discharge cavity 323 is formed inside each pressing filter plate 32. A through hole 322 is arranged in the middle of each pressing filter plate 32. Each pressing filter plate 32 is sleeved on the telescopic arm of the hydraulic cylinder 342 through the through hole 322 in the middle. Liquid outlets are arranged on both sides of each pressing filter plate 32. The lead sludge filter press 3 includes a liquid outlet pipe 35. The liquid outlet pipe 35 is fixed on the frame 31 and is communicated with the liquid outlets on both sides of each pressing filter plate 32. The other end of the liquid outlet pipe 35 is communicated with the acid liquid conveying pipe.

[0045] The stirring tank 222 of the present utility model includes a first stirring motor 21 and a first stirring rod 22. The first stirring rod 22 is fixed inside the stirring tank 222, the first stirring motor 21 is fixed on the top of the stirring tank 222, the rotating end of the first stirring motor 21 is arranged downward, the top end of the first stirring rod 22 passes through the top of the stirring tank 222 and is connected to the rotating end of the first stirring motor 21. A number of first stirring blades 221 are fixed on the first stirring rod 22, and the number of first stirring blades 221 are distributed at intervals along the outer circumference of the first stirring rod 22. The first stirring motor 21 above the stirring tank 222 is used to drive the first stirring rod 22 to rotate, so that the lead sulfate in the stirring tank 222 is stirred into a suspended state. The stirring speed is 180-200 revolutions per minute, and the stirring time is 25-60 minutes. A guide plate 23 is fixed on the inner wall of the stirring tank 222. One end of the lead sludge discharge conveying pipe 24 is communicated with the bottom of the stirring tank 222, and the other end of the lead sludge discharge conveying pipe 24 is communicated with the lead sludge filter press 3. During the process of the first diaphragm pump 27 pumping the lead-containing suspended acid solution, the lead-containing suspended acid solution will flow along the guide plate 23 to the lead sludge discharge conveying pipe 24 at the bottom of the stirring tank 222, improving the discharge efficiency of the lead-containing suspended acid solution.

[0046] The above is the preferred embodiment of the present utility model. It should be noted that for those of ordinary skill in the art, without departing from the principle of the present utility model, several improvements and refinements can be made, and these improvements and refinements are also regarded as the protection scope of the present utility model.

Claims

1. A lead sulfate recovery system, characterized in that: It includes a utilization system for recovering lead sulfate from the upper plate of a coating machine, and the utilization system includes a recovery tank, a mixing tank, a lead mud filter press, and an acid tank; The recovery box is placed at the acid spraying roller and the water squeezing roller of the plate coating machine, and is used to collect lead sulfate in the plate acid spraying process; A lead sludge feed conveying pipe is provided between the recovery box and the stirring tank, a lead sludge feed conveying pipe is fixed with a lead sludge feed conveying pump, one end of the lead sludge feed conveying pipe is connected to the recovery box, and the other end of the lead sludge feed conveying pipe is connected to the stirring tank, and the lead sulfate collected in the recovery box is pumped to the stirring tank through the lead sludge feed conveying pump and the lead sludge feed conveying pipe; The stirring tank is used for stirring lead sulfate; A lead mud discharge conveying pipe is arranged between the stirring tank and the lead mud filter press, a first diaphragm pump is fixed on the lead mud discharge conveying pipe, one end of the lead mud discharge conveying pipe is connected to the stirring tank, and the other end of the lead mud discharge conveying pipe is connected to the lead mud filter press; A material receiving bucket is placed below the lead mud filter press, and the lead sulfate stirred in the stirring tank is pumped to the lead mud filter press for filtration to obtain lead mud cakes and acid solution. The lead mud cakes obtained after filtration by the lead mud filter press fall into the material receiving bucket below it; An acid liquid delivery pipe is arranged between the lead mud filter press and the acid box, one end of the acid liquid delivery pipe is connected to the lead mud filter press, and the other end of the acid liquid delivery pipe is connected to the acid box.

2. The lead sulfate recovery system according to claim 1, wherein: The lead mud filter press includes a frame and a compression drive mechanism, a compression plate, a plurality of compression filter plates, and a thrust plate fixed on the frame from left to right. The plurality of compression filter plates are spaced apart from each other, and the compression plate and the thrust plate are symmetrically distributed on both sides of the plurality of compression filter plates. One end of the compression drive mechanism is connected to the other side of the compression plate. A feed channel is provided above the plurality of compression filter plates, and a feed hole is provided at the top of each compression filter plate. The output end of the feed channel is connected to the feed hole of the compression filter plate.

3. The lead sulfate recovery system according to claim 2, wherein: The clamping drive mechanism comprises a driving motor and a hydraulic cylinder. The driving motor is connected to the hydraulic cylinder, and a telescopic arm of the hydraulic cylinder is connected to a clamping plate.

4. The lead sulfate recovery system according to claim 3, characterized in that: A discharge cavity is formed inside each compression filter plate, a through hole is provided in the middle of each compression filter plate, each compression filter plate is sleeved on the telescopic arm of the hydraulic cylinder through the through hole in the middle, and liquid outlets are provided on both sides of each compression filter plate. The lead mud filter press includes a liquid outlet pipe, which is fixed on the frame and communicated with the liquid outlets on both sides of the compression filter plate.

5. The lead sulfate recovery system according to claim 1, characterized in that: The stirring tank includes a first stirring motor and a first stirring rod, the first stirring rod is fixed inside the stirring tank, the first stirring motor is fixed to the top of the stirring tank, the rotating end of the first stirring motor is set downward, the top end of the first stirring rod passes through the top of the stirring tank and is connected to the rotating end of the first stirring motor, and a plurality of first stirring blades are fixed on the first stirring rod, and the plurality of first stirring blades are distributed along the outer circumference of the first stirring rod.

6. The lead sulfate recovery system according to claim 5, characterized in that: A material guide plate is fixed to the inner wall of the stirring tank, one end of the lead mud discharge conveying pipe is connected to the bottom of the stirring tank, and the other end of the lead mud discharge conveying pipe is connected to the lead mud filter press.

7. The lead sulfate recovery system according to claim 6, characterized in that: A float liquid level controller is provided inside the mixing tank, and the float liquid level controller includes a float and a connecting rod, one end of the connecting rod is connected to the float, and a liquid level sensing switch is provided at the top of the mixing tank, and the liquid level sensing switch is placed above the highest surface of the mixing tank. The liquid level sensing switch is electrically connected to the lead mud delivery pump, and the other end of the connecting rod is located below the liquid level sensing switch.

8. The lead sulfate recovery system according to claim 1, characterized in that: The acid box includes a second stirring motor and a second stirring rod, the second stirring rod is fixed inside the acid box, the second stirring motor is fixed above the acid box, the rotating end of the second stirring motor is arranged downward, the top end of the second stirring rod passes through the top of the acid box and is connected to the rotating end of the second stirring motor, and a plurality of second stirring blades are fixed on the second stirring rod, and the plurality of second stirring blades are distributed along the outer circumference of the second stirring rod at intervals from each other.