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Lead storage battery electrode plate preparation method and lead storage battery electrode plate

A technology of lead-acid batteries and plates, which is applied to the electrodes of lead-acid batteries, can solve the problems of reduced battery discharge time, slow separation of grid paste, and battery capacity attenuation, so as to prolong battery life, improve softening, and improve binding force. Effect

Inactive Publication Date: 2022-01-28
TIANNENG BATTERY GROUP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In the battery production process, plate manufacturing is the most critical process. The decrease in battery discharge time is mainly caused by the positive electrode. During the charge and discharge process of the positive plate, the binding force between the active material and the grid is getting worse and worse. Expansion and contraction increase, the positive plate softens, and the grid paste slowly separates, resulting in rapid battery capacity decay and short life

Method used

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  • Lead storage battery electrode plate preparation method and lead storage battery electrode plate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Put the positive grid to be coated at a temperature of 95°C for 5 hours, then cool it down to room temperature and start coating. The coating speed is 100 pieces / min, the surface drying kiln conveyor belt speed is 105 pieces / min, and the surface drying temperature is set at 150°C. , the outlet temperature of the low-temperature kiln is set at 1°C, and the wind speed of the cold air is controlled at 800m 3 / h, enter the surface drying kiln after coating, acid pouring, and overpressure rollers, and then enter the low-temperature kiln. After reaching 15°C, collect the film, put it on the shelf, and enter the curing room for curing and drying. The curing and drying control steps are as follows: the first step is at 65°C, the humidity is 99%, and the time is 20h; the second step is at 55°C and the humidity is 80%, the time is 10h, the temperature of the third step is 55°C, the humidity is 50%, the time is 8h, the temperature of the fourth step is 70°C, the humidity is 0%, th...

Embodiment 2

[0026] Place the negative grid to be coated at a temperature of 95°C for 5 hours, then cool to room temperature and start coating. The speed of coating is 100 pieces / min, the speed of the surface drying kiln conveyor belt is 105 pieces / min, and the surface drying temperature is set at 120°C. , the outlet temperature of the low-temperature kiln is set at 3°C, and the wind speed of the cold air is controlled at 800m 3 / h, after coating, acid spraying, and overpressure rollers, enter the surface drying kiln, and then enter the low-temperature kiln. After ℃, collect the film, put it on the shelf, and enter the curing room for curing and drying. The curing and drying control steps are as follows: the first step is at 50°C, the humidity is 99%, and the time is 24h; the second step is at 55°C, and the humidity is 80%. , the time is 6h, the temperature of the third step is 60°C, the humidity is 50%, the time is 6h, the temperature of the fourth step is 75°C, the humidity is 0%, and th...

Embodiment 3

[0034] Put the positive grid to be coated at a temperature of 95°C for 5 hours, then cool it down to room temperature and start coating. The coating speed is 100 pieces / min, the surface drying kiln conveyor belt speed is 105 pieces / min, and the surface drying temperature is set at 150°C. , the outlet temperature of the low-temperature kiln is set at 1°C, and the wind speed of the cold air is controlled at 800m 3 / h, enter the surface drying kiln after coating, acid pouring, and overpressure rollers, and then enter the low-temperature kiln. After reaching 15°C, collect the film, put it on the shelf, and enter the curing room for curing and drying. The curing and drying control steps are as follows: the first step is at 65°C, the humidity is 99%, and the time is 20h; the second step is at 55°C and the humidity is 80%, the time is 10h, the temperature in the third step is 55°C, the humidity is 50%, the time is 8h, the temperature in the fourth step is 70°C, the humidity is 0%, an...

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Abstract

The invention discloses a lead storage battery electrode plate preparation method and a lead storage battery electrode plate. The lead storage battery plate preparation method comprises the following steps: filling a battery grid with lead plaster, drying the surface of the battery grid, quickly cooling the battery grid in a low-temperature kiln, quickly cooling the surface of the battery plate which is just taken out of the surface drying kiln by up and down air cooling, quickly reducing the temperature of the battery grid to 15-20 DEG C, collecting the battery grid, and putting the battery grid on a curing chamber for curing. According to the electrode plate produced by thelead storage battery plate preparation method , the phenomena of fast water loss and low water content of lead paste, little corrosion of the surface of the cured grid and poor binding force of the lead paste and the grid caused by fast heat conducting and overhigh temperature of the grid after the electrode plate is subjected to high temperature in a surface drying kiln are improved; the phenomena of active substance softening, falling and grid paste separation in the charging and discharging process of the positive plate are improved, and the cracking phenomenon of the negative plate is improved; and the binding force between the grid and active substances is improved, the conductivity is enhanced, and the service life of the battery is prolonged.

Description

technical field [0001] The invention relates to the technical field of storage battery production, in particular to a preparation method for a lead storage battery pole plate and the lead storage battery pole plate. Background technique [0002] In recent years, electric vehicles for express delivery and food delivery in the market require higher motor power and higher current. According to GB / T22199-2017 "Valve-regulated lead-acid battery for electric moped vehicles", the battery adopts a 2-hour rate capacity of 0.5C 2 Discharge, but in fact, the actual current used by this type of electric vehicle is 0.6C 2 on, the start-up current reaches 1.5C 2 Above, the two kinds of working current are alternately carried out during use, which directly affects the service life of the battery. Under high current operation, the discharge time of the battery decreases more and more with the increase of the number of uses. After the returned battery was dissected, it was found that the ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): H01M4/14H01M4/16H01M4/20
CPCH01M4/14H01M4/16H01M4/20Y02E60/10
Inventor 张四平杨新明张利棒高根芳汤序锋
Owner TIANNENG BATTERY GROUP