Method for preparing silicon-based active material particles for secondary battery and silicon-based active material particles
11196042 · 2021-12-07
Inventors
- Young Tai Cho (Seo-gu Daejeon, KR)
- Yong Gil Choi (Yuseong-gu Daejeon, KR)
- Seung Chul Park (Yuseong-gu Daejeon, KR)
- Seon Park (Dong-gu Daejeon, KR)
- Hee Young Seo (Yuseong-gu Daejeon, KR)
- Jee Hye Park (Yuseong-gu Daejeon, KR)
- Yong Eui Lee (Gyeonggi-do, KR)
- Chul Hwan Kim (Daejeon, KR)
Cpc classification
H01M4/62
ELECTRICITY
C01P2004/80
CHEMISTRY; METALLURGY
C01P2004/62
CHEMISTRY; METALLURGY
Y02E60/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01M10/0525
ELECTRICITY
C01P2004/64
CHEMISTRY; METALLURGY
International classification
H01M4/36
ELECTRICITY
H01M4/62
ELECTRICITY
Abstract
The present invention relates to a method for preparing silicon-based active material particles for a secondary battery and silicon-based active material particles. The method for preparing silicon-based active material particles according to an embodiment of the present invention comprises the steps of: providing silicon powder; dispersing the silicon powder into an oxidant solvent to provide a mixture prior to grinding; fine-graining the silicon powder by applying mechanical compression and shear stress to the silicon powder in the mixture prior to grinding to produce silicon particles; producing a layer of chemical oxidation on the fine-grained silicon particles with the oxidant solvent while applying mechanical compression and shear stress to produce silicon-based active material particles; and drying the resulting product comprising the silicon-based active material particles to yield silicon-based active material particles.
Claims
1. Silicon-based active material particles, each of the particles comprising: a core of a silicon particle, wherein the core has a silicon crystal domain size of less than 50 nm; and a chemical oxidation layer formed on the core of the silicon particle, wherein the oxygen content of the silicon-based active material particles with respect to the total weight of the silicon-based active material particles is from 9 wt % to 20 wt %, and wherein an average particle size of the silicon-based active material particles is in a range of 30 nm to 300 nm.
2. The silicon-based active material particles of claim 1, wherein the average particle size of the silicon-based active material particles is in a range of 30 nm to 200 nm.
3. The silicon-based active material particles of claim 2, wherein a particle size of 90% of the silicon-based active material particles is 310 nm or less.
4. The silicon-based active material particles of claim 1, wherein a conductive layer is further formed on the chemical oxidation layer.
5. The silicon-based active material particles of claim 4, wherein the conductive layer is a carbon-based conductive layer.
6. The silicon-based active material particles of claim 5, wherein the carbon-based conductive layer has a larger mole fraction of sp.sup.2 carbon than sp.sup.3 carbon.
7. The silicon-based active material particles of claim 5, wherein the carbon-based conductive layer is a graphite layer, a soft carbon layer, a graphene layer, a crystalline carbon layer, or an amorphous carbon layer.
8. The silicon-based active material particles of claim 7, wherein the carbon-based conductive layer has a larger mole fraction of sp.sup.2 carbon than sp.sup.3 carbon.
9. The silicon-based active material particles of claim 1, wherein a thickness of the chemical oxidation layer is in a range of 2 nm to 30 nm.
10. The silicon-based active material particles of claim 1, wherein a thickness of the chemical oxidation layer is in a range of 3 nm to 15 nm.
11. The silicon-based active material particles of claim 1, wherein the silicon-based active material particles each have a flake-like shape.
12. The silicon-based active material particles of claim 1, wherein the chemical oxidation layer is formed by refining silicon powder by applying mechanical compression and shearing stresses and, simultaneously, wet-forming the chemical oxidation layer on the cores of the silicon particles by using an oxidant solvent.
13. The silicon-based active material particles of claim 1, wherein the oxygen content of the silicon-based active material particles with respect to a total weight of the silicon-based active material particles is from 14 wt % to 20 wt %.
14. The silicon-based active material particles of claim 1, wherein a circularity of the silicon-based active material particles is equal to or greater than 0.5 and less than or equal to 0.9, and the circularity is determined according to the equation:
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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MODE FOR CARRYING OUT THE INVENTION
(9) Hereinafter, exemplary embodiments will be described in detail with reference to accompanying drawings.
(10) The present invention will now be described more fully with reference to the accompanying drawings, in which exemplary embodiments of the invention are shown. The invention may, however, be embodied in many different forms and should not be construed as being limited to the embodiments set forth herein; rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the concept of the invention to those skilled in the art.
(11) Also, in the drawings, thickness and size of each layer are exaggerated for convenience and clarity of explanation, and like reference numerals denote like elements in the drawings. As used herein, the term “and/or” includes any and all combinations of any of listed items.
(12) The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the singular forms “a”, “an” and “the” are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms “comprise” and/or “comprising,” when used in this specification, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof.
(13) In silicon-based active material particles, a reaction that lithium ions form a Li.sub.xSi compound through an electrochemical reaction with silicon of the silicon-based active material particles proceeds from surfaces of the silicon-based active material particle. In this case, there is a sharp interface between the interior of the silicon-based active material particles that is not yet reacted (pristine-Si) and the lithium compound (Li.sub.xSi) layer on the surface of the particles. As lithiation proceeds, the thickness and the volume of the lithium compound layer gradually increase and, when the silicon is completely consumed and the entire particles are changed to the Li.sub.xSi compound, the electrochemical reaction ends. However, if there is an interface between the lithium compound layer and the silicon interior that is not reacted during the lithiation process before the electrochemical reaction ends, a tensile hoop stress is formed in the lithium compound layer from a moment at which the lithium compound layer surrounds silicon particles therein. Generally, silicon particles exhibit high breaking strength against compression stress, but the tensile hoop stress is a major factor in the surface cracking and destruction of silicon particles.
(14) The inventors of the present invention have found that while a silicon-based active material has very low strength against elongation stress compared to compression stress, a chemical silicon oxide that is formed on or inside the cores of silicon particles simultaneously with a process for subdividing silicon powders by using compression stress and shearing stress may prevent or minimize tensile hoop stress on surfaces of silicon-based active material particles during lithiation and prevent surface cracks of the silicon particles by eliminating remaining stress, thus being very effective for controlling shape of silicon-based active material particles and controlling expansion rate thereof.
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(16) The grain-refined silicon particles SC have a potato-like shape as shown in
(17) The silicon particles SC refined by mechanical compression and shearing stress may be particles having irregular shapes. Furthermore, the refined silicon particles formed together with a chemical oxide by the shearing stress may have a low crystallinity or may easily become 20 nm or larger amorphous particles without a crystal domain. When the mechanical compression and shearing stresses are too small, it is difficult for the refined silicon particles to become spherical or may have a large crystal domain of 50 nm or larger. Furthermore, when the mechanical compression and shearing stress are too large, the silicon particles become too fine and are unable to obtain sufficient capacity as an active material. Therefore, it is necessary to control the shearing stress during a pulverizing operation.
(18) The grain-type particles shown in
(19) The silicon-based active material particles 100A_1 and 100A_2 according to an embodiment of the present invention include chemical oxidation layers CO formed on the cores of the silicon particles (SC), as shown in
(20) The thickness of the chemical oxidation layer CO is in the range of 2 nm to 30 nm and may be in the range of 3 nm to 15 nm. The chemical oxidation layers CO may be formed on the cores of the silicon particles SC as shown in
(21) In the silicon-based active material particles 100A_1 and 100A_2, oxygen content with respect to the total weight of the cores and the total weight of the chemical oxidation layer CO of the silicon particles SC is in the range of 9 wt % to 20 wt % and may be in the range of 14 wt % to 20 wt %. Both an initial charging rate and the capacity retention characteristic are maintained at 80% or higher within the range of the oxygen content, and thus a silicon-based active material particle suitable for commercialization may be provided. When the oxygen content exceeds 20 wt %, the initial charging rate is reduced by 20% or more. When the oxygen content is 9 wt % or higher, the capacity retention rate becomes 90% or more (refer to Table 2).
(22) The oxygen content is measured by using an infrared detection technique using a commercial element analyzer (ELTRA ONH-2000). Specifically, oxygen in the samples is changed to carbon dioxide by using a sample of 2 mg to 10 mg, a calorie of 8 kW, and helium (purity of 99.995%) as a carrier gas, and an amount of oxygen is quantized by measuring the amount of the carbon dioxide. Therefore, oxygen content may be measured.
(23) The chemical oxidation layer CO may form a stable phase with minimal influence to crystal structures of silicon particles unlike a silicon oxide layer formed by a conventional thermal oxidation process or thin-film deposition process like a chemical vapor deposition process. Generally, in cases of thermal oxidation and chemical vapor deposition, a high processing temperature hinders amorphization of silicon particles. However, since the chemical oxide layer CO is formed at a low temperature and may be formed under high compression and shearing stresses, a silicon oxide layer may be formed with refinement of the silicon particles SC and, selectively, amorphization of the silicon particles SC. As a result, the charging/discharging efficiency of the silicon particles may be improved and service life thereof may be increased. Detailed description thereof will be given below.
(24) The degree of irregularity of shapes of the silicon-based active material particles 100A_1 and 100A_2 is determined based on the shape of the cores SC inside the silicon particles and depends on compression stress and shearing stress in a grain-refining process. An extent to which the shapes of the silicon-based active material particles 100A_1 and 100A_2 deviates from a spherical shape may be evaluated by the circularity as shown in Equation 1. The circularity is determined based on a ratio of an area to which particles are projected to a circumferential length of the particles. In case of a solid type, circularity may be measured by selecting a maximum length of particles and measuring based on an area of projection of the cross-section of a particle including the maximum length. In case of a hollow tube structure or a fiber structure, circularity may be measured based on an area of projection of a cross-section perpendicular to a direction in which a tube or a fiber extends, that is, the longer side direction.
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(26) Here, A denotes an area of projection of a 2-dimensionally projected silicon particle and P denotes the circumferential length of the 2-dimensionally projected silicon particle. The circularity of the silicon particle may be measured from an image obtained via a scanning electron microscope by using commercially available software like ImageJ®, e.g., ImageJ136. Alternatively, the circularity may be measured by using a flow particles image analyzer FPIA-3000® manufactured by SYSMEX (Kobe, Japan).
(27) Circularity of a silicon-based active material particle is equal to or greater than 0.5 and less than or equal to 0.9. Preferably, the circularity is equal to or greater than 0.6 and less than or equal to 0.8. The silicon-based active material particles having circularities less than 0.5 may be subdivided from relatively thin outer portions due to a plurality of number of times of charging and discharging, and thus service life thereof may be deteriorated. On the contrary, when the circularity exceeds 0.9, cracks or fractures easily occur due to tensile stress applied to a lithiation layer as described below. Due to the cracks or fractures, formation of a SEI layer on exposed surfaces of the cores of silicon particles is promoted, thereby deteriorating the service life of a battery.
(28) An average particle size of the silicon-based active material particles 100A_1 and 100A_2 may be in the range of 30 nm to 300 nm and may be in the range of 30 nm to 200 nm. When an average diameter of the silicon-based active material particles 100A_1 and 100A_2 is less than 30 nm, the relative proportion of a conductive layer or a particle-type conductive material in the active material slurry increase, and thus battery capacity decreases. When an average diameter of the silicon-based active material particles 100A_1 and 100A_2 exceeds 300 nm, circularity is increased to minimize surface energy or it becomes difficult to amorphize the silicon-based active material particles 100A_1 and 100A_2.
(29) According to some embodiments, since the chemical oxidation layer CO of the silicon-based active material particles 100A_1 and 100A_2 is electrically insulative, a conductive layer CS may be further formed on the silicon-based active material particles 100A_1 and 100A_2 in order to reduce contact resistance between the silicon-based active material particles 100A_1 and 100A_2 and to secure an electron moving path. The conductive layer CS may include a carbon-based conductive layer, such as a graphite layer, a soft carbon layer, or a graphene layer.
(30) The conductive layer CS is a layer for electrical connection between the silicon-based active material particles contacting one another and reduces the internal resistance to a current collector (not shown). According to some embodiments, the carbon-based conductive layer may be a crystalline layer or at least a partially amorphous carbon film. When the carbon-based conductive layer has a high crystallinity, such as a graphite layer, the carbon-based conductive layer may react with an electrolytic solution. Therefore, a low crystalline or amorphous carbon film having chemical corrosion-resistance is preferable. Furthermore, the carbon-based conductive layer may have a mixture of a conductive graphite structure SP.sup.2 and an insulating diamond structure SP.sup.3. For the carbon-based conductive layer to have conductivity, the graphite structure SP.sup.2 may have a larger mole fraction than the diamond structure SP.sup.3, where the conductivities thereof may be controlled via a heat treatment process.
(31) The above-described carbon-based conductive layer is merely an example, and the present invention is not limited thereto. For example, the outermost portions of the silicon-based active material particles 100A_1, 100A_2 may include nanoscale particles of conductive metal oxides, such as antimony zinc oxide or antimony tin oxide, or layers including the same.
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(33) Referring to
(34) Referring to
(35) Regarding the stage C, referring to
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(37) Referring to
(38) The stress development profile shown in
(39) The volume expansion that occurs when the core SC of a silicon particle is lithiated may occur anisotropically. Specifically, volume expansion of silicon in a <1 1 0> direction is dominant during lithiation and volume expansion in a <1 1 1> direction is negligibly small. Although there is no clear theory regarding the phenomenon, it is presumed that a spreading path of lithium is related to a change of morphology based on the elasto-plastic deformation of silicon due to lithiation.
(40) According to these experimental results, volume expansion may occur more significantly in a direction in which lithium spreads rapidly. In a method of minimizing tensile hoop stress in a volume-expanding lithium layer, it is preferable that a dominant flat surface is a {110} surface and, quantitatively, the area of the {110} surface of the core SC of a silicon particle is larger than the area of another {100} surface and the area of a {111} surface.
(41) According to the embodiment of the present invention, by preparing silicon-based active material particles having a reduced circularity equal to or greater than 0.5 and less than or equal to 0.9, an irreversible reaction due to cracks or fractures of cores of silicon particles that occur while a battery is being charged may be suppressed or reduced. Furthermore, as the closer the circularity of the silicon-based active material particles is close to 1, the contacts between the silicon-based active material particles become substantially point-contacts. As a result, electronic conductivity between the silicon-based active material particles is lowered, and thus an output voltage may be reduced due to an increased internal resistance of a battery. However, according to an embodiment of the present invention, surface contacts may occur between the silicon-based active material particles, and thus an increased output of a battery may be expected due to a reduced internal resistance.
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(43) Referring to
(44) According to an embodiment, the oxidant solvent is for forming a chemical oxidation layer of silicon and may be water, de-ionized water, an alcoholic solvent, or a mixture of two or more thereof. The alcoholic solvent may be any one of ethyl alcohol, methyl alcohol, glycerol, propylene glycol, isopropyl alcohol, isobutyl alcohol, polyvinyl alcohol, cyclohexanol, octyl alcohol, decanol, hexatecanol, ethylene glycol, 1,2-octane diol, 1,2-dodecane diol, and 1,2-hexadecane diol, or a mixture thereof. Preferably, the alcoholic solvent is ethyl alcohol.
(45) The silicon power is grain-refined by applying mechanical compression and shearing stress to the silicon powder of the pre-pulverization mixture, thereby forming silicon particles to become the cores of the silicon-based active material particles (operation S30). Such a grain-refining process is effective for preparing amorphous silicon particles. The circularity of the silicon-based active material particles according to an embodiment of the present invention is equal to or greater than 0.5 and less than or equal to 0.9 and, preferably, the circularity is controlled to be equal to or greater than 0.6 and less than or equal to 0.8.
(46) According to some embodiments, application of mechanical compression and shearing stresses to the silicon powder may be achieved by grinding technique for providing the pre-pulverization mixture between a spinning abrasive plate and a fixed plate and performing pressing and polishing simultaneously. According to another embodiment, application of mechanical compression and shearing stress to the silicon powder may be performed by milling technique for putting the pre-pulverization mixture and abrasive particles in a cylindrical or conic container revolving around a center axis and revolving the container. The abrasive particles may be beads including ceramic particles, metal particles, or mixtures thereof, but the present invention is not limited thereto. The abrasive particles have an appropriate average size for a size of the silicon powder, thereby applying mechanical compression and shearing stress to the silicon powder.
(47) Simultaneously as the mechanical compression and shearing stress are applied, a chemical oxidation layer is formed on the grain-refined silicon particles by using the oxidant solvent, thereby forming silicon-based active material particles (operation S40). The chemical oxidation layer includes a silicon oxide as described above. The thickness of the chemical oxidation layer is in the range of 2 nm to 30 nm and may be in the range of 3 nm to 15 nm.
(48) The silicon-based active material particles (see 100A_1 and 100A_2 in
(49) Thereafter, a result product including the silicon-based active material particles is dried, and thus silicon composite particles may be yielded (operation S50). Preferably, a subsequent operation, such as a distribution operation for destroying the yielded silicon composite particles, may be further performed.
(50) According to some embodiments, before the operation for drying the result product, an aging operation (operation S45) for reducing stress by additionally oxidizing the silicon-based active material particles by dispersing and stirring the result product in any one of the above-stated oxidant solvents or a mixture thereof may be further performed. Through the aging operation, the residual stress accumulated in the core and/or the chemical oxidation layer of the silicon particles during a refining process using compression stress and shearing stress is alleviated, and the chemical oxidation layer is additionally generated. As a result, the strength of the chemical oxidation layer is increased, and thus the chemical oxide layer may serve as a clamping layer capable of suppressing a volume change of the core of the silicon particles during charging and discharging.
(51) According to some embodiments, as described with reference to
(52) The following experimental examples are selected from the above-described embodiments and do not limit the same.
Experimental Example 1
(53) A commercially available polysilicon powder having an average diameter of about 5 μm was prepared, and the polysilicon powder was dispersed in an oxidant solvent of 100% ethanol to prepare a pre-pulverization mixture. Silicon-based active material particles having circularities of about 0.4, 0.5, 0.6, 0.7, 0.8, and 0.9 were prepared by repeating a mill-pulverizing operation with a controlled time for applying compression and shearing stresses to the pre-pulverization mixture for at least once. According to a comparative embodiment, a spherical silicon-based active material particle having a circularity of 0.95 or higher include a silicon oxide layer formed on a spherical commercial silicon particle by thermal oxidation.
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(57) Table 1 below shows initial efficiencies, capacities per weight, and capacity retentions of half cells evaluated after negative electrodes are fabricated by slurrying the silicon-based active material particles having the respective circularities. Capacity retention is a result evaluated after 50 charging/discharging cycles. The reference initial capacity is 4,200 mAh/g, which is the theoretical capacity of silicon.
(58) TABLE-US-00001 TABLE 1 Cell Characteristics Initial Capacity Retention at Circularity Efficiency Capacity per Weight 50 Times 0.4 81% 2,040 mAh/g 73% 0.5 84% 2,110 mAh/g 85% 0.6 88% 2,290 mAh/g 93% 0.7 89% 2,320 mAh/g 98% 0.8 90% 2,341 mAh/g 98% 0.9 90% 2,343 mAh/g 81% 0.95 90% 2,342 mAh/g 60%
(59) Referring to Table 1, the initial efficiency tends to gradually decrease as circularity decreases for circularities of 0.8 or less. However, initial efficiencies of 80% or higher, which are practical initial efficiencies, appear at all of circularities of 0.4 or higher. In terms of capacity retention, residual capacity was reduced to less than 80% due to increased irreversibility based on a volume expansion when the circularity was less than 0.5. However, at circularities within the range of 0.5 to 0.9, the residual capacity is maintained at 80% or higher, which is a practical level, and is maintained at 90% or higher at circularities in the range of 0.6 to 0.8.
Experimental Example 2
(60) Similar to the Experimental Example 1, poly-silicon powder having an average diameter of about 5 μm was prepared, and pre-pulverization mixtures were prepared by dispersing the poly-silicon powers in 100% mol of ethanol, a mixed solution of 75% mol of ethanol and 25% mol of water (distilled water), a mixed solution of 50% mol of ethanol and 50% mol of water, a mixed solution of 25% mol of ethanol and 75% mol of water, and 100% mol of water. Each of the pre-pulverization mixtures was subjected to time-controlled mill-pulverizing operation once to control the oxygen content thereof. The average circularity was 0.6. The samples prepared using the various above-stated oxidant solvents according to an embodiment of the present invention are sequentially referred to as samples a0, b0, c0, d0 and e0.
(61) Next, an aging operation for placing these samples in a fresh oxidant solvent of the same kind as that of the oxidant solvent applied to these samples and dispersing and stirring the same for 24 hours and 48 hours was performed. The aged samples were respectively labelled as samples a1, b1, c1, d1, and e1 and samples a2, b2, c2, d2, and e2 and were evaluated for oxygen content changes and cell characteristics. Table 2 shows a result of evaluating the changes of the oxygen content of the samples according to an embodiment of the present invention and the initial efficiencies, capacities per weight, and capacity retentions of fabricated half cells.
(62) TABLE-US-00002 TABLE 2 Cell Characteristics Oxidant Solvent Capacity (% Mole Aging Oxygen Initial Capacity per Retention at Sample Concentration) Time (Hr) Content Efficiency Weight 50 Times Sample a0 Ethanol 100% 0 10.1 88.0% 2290 mAh/g 93.0% Sample b0 Ethanol 75%:Water 0 11.8 88.2% 2199 mAh/g 94.0% 25% Sample c0 Ethanol 50%:Water 0 12.3 88.1% 2170 mAh/g 94.1% 50% Sample d0 Ethanol 25%:Water 0 13.7 86.3% 1989 mAh/g 95.1% 75% Sample e0 Water 100% 0 18.8 82.1% 1782 mAh/g 97.8% Sample a1 Ethanol 100% 24 11.4 88.5% 2187 mAh/g 94.6% Sample b1 Ethanol 75%:Water 24 13.1 86.4% 2163 mAh/g 94.4% 25% Sample c1 Ethanol 50%:Water 24 13.7 86.7% 2111 mAh/g 95.9% 50% Sample d1 Ethanol 25%:Water 24 14.6 84.5% 1932 mAh/g 96.8% 75% Sample e1 Water 100% 24 20.8 79.5% 1701 mAh/g 97.2% Sample a2 Ethanol 100% 48 13.1 87.1% 2092 mAh/g 93.4% Sample b2 Ethanol 75%:Water 48 14.5 85.5% 2007 mAh/g 93.9% 25% Sample c2 Ethanol 50%:Water 48 15.7 84.1% 1946 mAh/g 96.9% 50% Sample d2 Ethanol 25%:Water 48 17.4 82.1% 1801 mAh/g 97.2% 75% Sample e2 Water 100% 48 23.5 77.8% 1603 mAh/g 98.8%
(63) Referring to Table 2, water has the highest oxygen content. Furthermore, when the aging operation is performed for 24 hours and 48 hours, oxygen content further increases. The reason thereof is that the silicon-based active material particles are further oxidized through the aging operation. Furthermore, the oxidation during the aging operation eliminates residual stress of the silicon particles accumulated during the process of grain-refinement of the silicon powder, thereby preventing the silicon-based active particles from being rapidly refined due to the residual stress during charging and discharging. As a result, durability of the silicon-based active material particles may be improved. In relation, thereto, in case of an aged sample, although the capacity per weight and the initial efficiency are comparatively lower than an sample not subjected to an aging operation, but the residual capacity of the aged sample is improved. Therefore, it is clear that an aging operation improves service life of a cell employing silicon-based active material particles as a negative electrode active material.
(64) While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it will be understood by those of ordinary skill in the art that various changes in form and details may be made therein without departing from the spirit and scope of the present invention as defined by the following claims.
INDUSTRIAL APPLICABILITY
(65) According to an embodiment of the present invention, there may be provided a method of preparing silicon-based active material particles by refining silicon powders by applying mechanical compression and shearing stresses and, simultaneously, wet-forming a silicon oxide film (hereinafter referred to as a chemical oxidation layer) on the cores of silicon particles by using an oxidant solvent or controlling oxygen contents of the silicon particles, preventing excessive expansion of the cores of the silicon particles during charging/discharging of a cell, preventing refinement due to the expansion, and contributing to increased service life of the silicon-based active material particles by causing stable formation of a solid electrolyte interface (SEI).