Artificial graphite negative-pole material, preparation method therefor and lithium-ion battery

An artificial graphite negative electrode and graphitization technology, applied in battery electrodes, secondary batteries, chemical instruments and methods, etc., can solve the problems of high preparation cost, low energy density, poor coating uniformity, etc., and improve the degree of anisotropy. High performance, excellent electrochemical performance, and easy quality control

Active Publication Date: 2020-01-03
贵州凯金新能源科技有限公司
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AI-Extracted Technical Summary

Problems solved by technology

Secondary particle coating carbonization can obtain high-capacity and high-rate materials, but there are problems such as poor coating uniformity, significant re-bonding phenomenon, and low yield, which seriously affect the processing performance of the material
[0004] In order to solve the above problems, the patent 201710683450.9 discloses a fast-charging graphite anode material and its preparation method, through mixing the graphite precursor with the coating material, low-temperature treatment and high-temperature graphitization treatment, but lacks the secondary granulation process and surface modification The improvement effect of ion diffusion path and interface is limited, the energy density is not high, and the improvement of fast charging performance i...
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Method used

In comparison, Comparative Example 1 and Comparative Example 2 are single-component components, and there are deficiencies in the fast filling of capacity and rate respectively. In Comparative Example 3, the primary particles are not coated, and the fast filling performance is serious weak. Combined with the samples in the examples, the primary particles are coated and compounded with the secondary particles, which can significantly improve the interface stability of the material and improve the comprehensive electrical properties of the material.
[0050] In conjunction with the electrical performance data of graphite negative electrode materials in Examples 1 to 6, it can be seen that the type of graphitized primary particle coating agent has a greater impact on the fast charge capability of the final graphite negative electrode. As can be seen from Table 1, the average ...
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Abstract

The invention discloses a preparation method for rate type artificial graphite negative-pole material with high energy density. The preparation method comprises the following steps: subjecting raw material cokes to coarse breaking and pulverizing directly or coarse breaking, high-temperature modifying and then pulverizing, and carrying out reshaping treatment, so as to obtain primary granules A; kneading the primary granules A and an organic carbon source, then, carrying out dynamic thermal coating, and carrying out screening, so as to obtain primary granules B; uniformly mixing the primary granules A with a binder, then, subjecting the mixture to granulating in a granulating reactor, and carrying out screening, so as to obtain secondary granules C; subjecting the primary granules B and the secondary granules C to graphitizing separately, and carrying out screening, so as to obtain graphitized primary granules B and graphitized secondary granules C; and uniformly mixing the graphitizedprimary granules B and the graphitized secondary granules C proportionally, and carrying out screening, thereby obtaining a finished product. The preparation method is simple in process and easy in quality control; and by applying the artificial graphite negative-pole material prepared by adopting the method to a lithium-ion battery, the lithium-ion battery is large in capacity, good in cycle andexcellent in quick charging performance.

Application Domain

Carbon compoundsCell electrodes +1

Technology Topic

ChemistryHigh energy +9

Image

  • Artificial graphite negative-pole material, preparation method therefor and lithium-ion battery

Examples

  • Experimental program(6)
  • Comparison scheme(3)
  • Effect test(1)

Example Embodiment

[0028] Example 1
[0029] The needle coke with a volatile content of 0.5% is crushed and shaped by a roller mill-shaping machine to obtain primary particles A, and the average particle size D50 of the primary particles A is controlled to 8 μm. Take part of the primary particles A and the pyrolysis oil coating agent into the vacuum kneader according to the mass ratio of 100:8, knead at 120°C at normal pressure for 2 hours, then switch to vacuum mode for kneading at 250°C for 4 hours, and put the kneaded material into the vertical In a reactor, under the protection of nitrogen, heat up at 5°C/min to 400°C for 2 hours, then heat up at 3°C/min to 550°C for 4 hours, and sieving after cooling to obtain primary particles B; Particle A and petroleum pitch with a softening point of 250°C and an average particle size of 7μm are mixed uniformly according to a mass ratio of 100:10, and then put into a drum furnace. Under the protection of nitrogen, the temperature is raised at 5°C/min to 600°C for 4 hours. Granules are reacted and sieved after cooling to obtain secondary granules C. The primary particles B and the secondary particles C are graphitized at 2800° C. for 24 hours, and then sieved to obtain graphitized primary particles B and graphitized secondary particles C. The graphitized primary particles B and the graphitized secondary particles C are uniformly mixed according to a mass ratio of 30:70, and then sieved again to obtain a high-energy density magnification type artificial graphite product.

Example Embodiment

[0030] Example 2
[0031] The needle coke with a volatile content of 1% is crushed and shaped by a roller mill-shaping machine to obtain primary particles A, and the average particle size D50 of the primary particles A is controlled to 8 μm. Take part of the primary particles A and the sucrose coating agent into the vacuum kneader at a mass ratio of 100:5, knead at 120°C for 2 hours at normal pressure, then switch to vacuum mode for kneading at 250°C for 4 hours, and put the kneaded material into the vertical type In the reactor, under the protection of nitrogen, heat up at 5°C/min to 400°C for 2 hours, then heat up at 3°C/min to 600°C for 2 hours. After cooling, sieving to obtain primary particles B; take part of the primary particles A and petroleum pitch with a softening point of 150°C and an average particle size of 7μm are mixed uniformly according to a mass ratio of 100:15 and then put into a drum furnace. Under the protection of nitrogen, the temperature is raised at 5°C/min to 600°C for 4 hours for granulation. After reaction, sieving after cooling to obtain secondary particles C. The primary particles B and the secondary particles C are graphitized at 2800° C. for 24 hours, and then sieved to obtain graphitized primary particles B and graphitized secondary particles C. The graphitized primary particles B and the graphitized secondary particles C are uniformly mixed according to a mass ratio of 40:60, and sieved again to obtain a high-energy-density-multiplying artificial graphite product.

Example Embodiment

[0032] Example 3
[0033] The needle coke with a volatile content of 5% is roughly broken to below 5 mesh, then modified and modified at a high temperature of 900°C for 4 hours, and then crushed and shaped by a roller mill-shaping machine to obtain primary particles A, and control the primary particle A The average particle size D50 is 8 μm. Take part of the primary particles A and the phenolic resin oil coating agent into the vacuum kneader at a mass ratio of 100:8, knead at 120°C under normal pressure for 2 hours, then switch to vacuum mode for kneading at 250°C for 4 hours, and put the kneaded material into it In the vertical reactor, under the protection of nitrogen, heat up at 5°C/min to 400°C for 2 hours, then heat at 3°C/min to 600°C for 2 hours. After cooling, sieving to obtain primary particles B; The primary particles A and the petroleum resin with a softening point of 150°C and an average particle size of 9μm are uniformly mixed according to a mass ratio of 100:12, and then put into the drum furnace. Under the protection of nitrogen, the temperature is raised at 5°C/min to 550°C for 4 hours. Granulation reaction, sieving after cooling to obtain secondary granules C. The primary particles B and the secondary particles C are graphitized at 2800° C. for 24 hours, and then sieved to obtain graphitized primary particles B and graphitized secondary particles C. The graphitized primary particles B and the graphitized secondary particles C are uniformly mixed according to a mass ratio of 50:50, and then sieved again to obtain a high-energy density magnification type artificial graphite product.

PUM

PropertyMeasurementUnit
Softening point250.0°C
The average particle size7.0µm
Softening point150.0°C

Description & Claims & Application Information

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