Patent Description:
Electrochemical device (for example, lithium-ion batteries) are widely used due to their environmental friendliness, high working voltage, high specific capacity, and long cycle life. They have become a more promising new green chemical power source in the world. Small-sized lithium-ion batteries are generally used as power sources for driving portable electronic communication devices (for example, camcorders, mobile phones, or notebook computers), especially high-performance portable devices. In recent years, medium- and large-sized lithium-ion batteries with high output have been developed and used in electric vehicles (EV) and large-scale energy storage systems (ESS). With widespread application of the lithium-ion batteries, their cycle performance has become a key technical issue to be addressed urgently. Improving an active material in an electrode is one of research directions to address the issue. <CIT> teaches a method for producing a negative electrode active material which has a high discharge capacity, a high charge-discharge efficiency, and excellent high-output characteristics, and which experiences only a small volume change during charging/discharging. The method for producing the negative electrode active material for a lithium secondary battery comprises a step for producing primary particles by crushing a carbon raw material containing <NUM> to <NUM> wt% of volatile components, a step for producing secondary particles by mixing the primary particles with a binder, and a step for producing a graphite material by graphitizing the secondary particles. <CIT> belongs to the technical field of lithium ion batteries and particularly relates to a graphite cathode material. According to a small-angle X-ray scattering method, the measured internal pore size distribution of the material is <NUM> to <NUM>, and the measured average pore size of the material is <NUM> to <NUM>; and with the adoption of polycrystalline silicon as an internal standard reference and according to an X-ray diffraction method, the measured d002 of powder of the material is <NUM> to <NUM>, and the measured C004/C110 of the material is <NUM> to <NUM>. Through limitation on parameters of the graphite material, the graphite cathode material can be ensured to have lower porosity, higher isotropy, higher reversible capacity and higher graphitization degree, the particles of the material have a compact internal structure, the good structure stability in a charge-discharge process can be maintained, and smooth lithium ion diffusion channels are formed on the surfaces and in the interior of the particles of the material. <CIT> teaches a nonaqueous secondary battery exhibiting a sufficiently small charge/discharge irreversible capacity in the initial cycle, exhibiting an excellent charge acceptance and excellent cycle characteristics, even when the negative electrode material-containing active material layer on a current collector is highly densified so as to obtain a high capacity. A composite graphite particle for nonaqueous secondary batteries, which is a composite graphite particle (B) obtained by forming a spherical graphite particle (A) and a graphitized product of graphitizable binder, wherein the spherical graphite particle (A) is a specific graphite particle or the composite graphite particle satisfies (a) and/or (b);.

In view of this, it is indeed necessary to provide an improved electrochemical device and an electronic device using a negative electrode active material.

This application provides an electrochemical device comprising a negative electrode active material, and an electronic device using the same, in an attempt to resolve, at least to some extent, at least one problem present in the related field.

According to an aspect of this application, this application provides an electrochemical device comprising a negative electrode, the negative electrode comprises a negative electrode current collector and a negative electrode active material layer, and the negative electrode active material layer comprises a negative electrode active material, where the negative electrode active material is graphite particles and has a median particle size D<NUM>v50; after being compressed under a pressure of <NUM> t, the negative electrode active material has a median particle size D<NUM>v50 as measured in accordance with China National Standard GB/T24533-<NUM>, and D<NUM>v50/D<NUM>v50 is greater than or equal to <NUM>, wherein D<NUM>v50 is <NUM> to <NUM>; D<NUM>v90 and D<NUM>v10 of the graphite particles satisfy that D<NUM>v90/D<NUM>v10 is less than <NUM>.

In some embodiments, D<NUM>v50/D<NUM>v50 of the negative electrode active material is greater than or equal to <NUM>. In some embodiments, D<NUM>v50/D<NUM>v50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>.

According to this embodiment of this application, the negative electrode active material has a specific surface area BET<NUM>, BET<NUM> is <NUM><NUM>/g to <NUM><NUM>/g; under a pressure of <NUM> t, the negative electrode active material has a specific surface area BET<NUM>; and (BET<NUM>-BET<NUM>)/BET<NUM>≤<NUM>. In some embodiments, BET<NUM> is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> is <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, or <NUM><NUM>/g.

According to the present invention, the negative electrode active material includes graphite particles, and the graphite particles satisfies the condition (c):
(c) according to an X-ray diffraction measurement, a grain size La of the graphite particles in a horizontal direction is <NUM> to <NUM>, and a grain size Lc of the graphite particles in a vertical direction is <NUM> to <NUM>.

In some embodiments, D<NUM>v50 of the graphite particles is <NUM> to <NUM>. In some embodiments, D<NUM>v50 of the graphite particles is <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>.

In some embodiments, D<NUM>v90/D<NUM>v10 of the graphite particles is less than <NUM>. In some embodiments, D<NUM>v90/D<NUM>v10 of the graphite particles is less than <NUM>. In some embodiments, D<NUM>v90/D<NUM>v10 of the graphite particles is less than <NUM>.

In some embodiments, according to an X-ray diffraction measurement, a grain size La of the graphite particles in a horizontal direction is <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>, and a grain size Lc of the graphite particles in a vertical direction is <NUM>, <NUM>, or <NUM>.

According to some embodiments of this application, the negative electrode active material layer satisfies at least one of conditions (d) and (f), wherein according to the present invention, the negative electrode active material layer satisfies condition (e):.

In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, or <NUM>:<NUM>.

In some embodiments, C004/C110 of the negative electrode active material layer is <NUM> to <NUM>. In some embodiments, C004/C110 of the negative electrode active material layer is <NUM> to <NUM>.

In some embodiments, a porosity of the negative electrode active material layer is <NUM>% to <NUM>%. In some embodiments, a porosity of the negative electrode active material layer is <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, or <NUM>%.

According to this embodiment of this application, when the electrochemical device is in a fully discharged state, as measured through an X-ray diffraction spectrum, a ratio C004'/C110' is <NUM> to <NUM>, C004' is a peak area of a (<NUM>) plane of the negative electrode active material layer, C110' is a peak area of a (<NUM>) plane of the negative electrode active material layer. In some embodiments, C004'/C110' of the negative electrode active material is <NUM> to <NUM>. In some embodiments, C004'/C110' of the negative electrode active material is <NUM> to <NUM>. In some embodiments, C004'/C110' of the negative electrode active material is <NUM> to <NUM>.

According to some embodiments of this application, when the electrochemical device is in a fully discharged state, the negative electrode active material has a median particle size Dav50; under a pressure of <NUM> t, the negative electrode active material has a median particle size Dbv50, and Dbv50/Dav50 is greater than or equal to <NUM>. In some embodiments, Dbv50/Dav50 of the negative electrode active material is greater than or equal to <NUM>. In some embodiments, Dbv50/Dav50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, or <NUM>.

According to some embodiments of this application, when the electrochemical device is in a fully discharged state, a median particle size Dav50 of the negative electrode active material is <NUM> to <NUM>. In some embodiments, Dav50 of the negative electrode active material is <NUM> to <NUM>. In some embodiments, Dav50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>.

According to some embodiments of this application, when the electrochemical device is in a fully discharged state, the negative electrode active material has a specific surface area BETa; under a pressure of <NUM> t, the negative electrode active material has a specific surface area BETb, and (BETb-BETa)/BETa<<NUM>.

According to still another aspect of this application, this application provides an electronic device, where the electronic device includes the electrochemical device according to this application.

Additional aspects and advantages of this application are partially described and presented in the later description, or explained by implementation of the embodiments of this application.

Drawings necessary for describing the embodiments of this application or the prior art are briefly described below, to help describe the embodiments of this application. It is obvious that the drawings described below are only some of the embodiments of this application. Those skilled in the art may still obtain drawings of other embodiments based on the results illustrated in these drawings without creative efforts.

Figure shows swelling percentages of lithium-ion batteries with a quantity of cycles at <NUM> according to Example <NUM> and Comparative Example <NUM> of this application.

Embodiments of this application are described in detail below. The embodiments related to the accompanying drawings described herein are illustrative and diagrammatic, and are used to provide a basic understanding of this application. The embodiments of this application shall not be construed as a limitation on this application.

In the description of embodiments and claims, a list of items preceded by the term "at least one of" may mean any combination of the listed items. For example, if items A and B are listed, the phrase "at least one of A and B" means only A; only B; or A and B. In another example, if items A, B, and C are listed, the phrase "at least one of A, B, and C" means only A; only B; only C; A and B (exclusive of C); A and C (exclusive of B); B and C (exclusive of A); or all of A, B, and C. The item A may contain a single element or a plurality of elements. The item B may contain a single element or a plurality of elements. The item C may contain a single element or a plurality of elements.

As used herein, "Dv50" refers to a particle size of a negative electrode active material that reaches <NUM>% of a cumulative volume from a small particle size side in volume-based particle size distribution, that is, a volume of the negative electrode active material whose particle size is less than this particle size accounts for <NUM>% of a total volume of the negative electrode active material.

As used herein, "Dv10" refers to a particle size of a negative electrode active material that reaches <NUM>% of a cumulative volume from a small particle size side in volume-based particle size distribution, that is, a volume of the negative electrode active material whose particle size is less than this particle size accounts for <NUM>% of a total volume of the negative electrode active material.

As used herein, "Dv90" refers to a particle size of a negative electrode active material that reaches <NUM>% of a cumulative volume from a small particle size side in volume-based particle size distribution, that is, a volume of the negative electrode active material whose particle size is less than this particle size accounts for <NUM>% of a total volume of the negative electrode active material.

Dv50, Dv10, and Dv90 of the negative electrode active material may be measured by using a method known in the art, for example, measured by using a laser particle size analyzer (for example, a Malvern particle size tester).

As used herein, "fully discharged state" is a state in which an electrochemical device is constant-current discharged at a discharge current of <NUM> C (that is, a current that discharges a theoretical capacity completely within <NUM> hour) to a voltage of <NUM> V in a <NUM> environment.

Unless otherwise specified, the electrochemical device of this application is in a <NUM>% state of charge (SOC).

During cycling of the electrochemical device (a lithium-ion battery is used as an example below), intercalation of lithium ions causes the electrochemical device to swell, which is especially serious at high temperatures. Increasing a degree of recombination of a negative electrode active material (for example, graphite particles) is a way to improve cycle performance of lithium-ion batteries. Primary particles of a negative electrode active material can be recombined to form secondary particles by using a high-viscosity binder or increasing an amount of a binder. This application achieves a balance between high capacity and thickness swelling during cycling of the lithium-ion battery by enhancing strength of the secondary particles.

Specifically, this application provides an electrochemical device comprising a negative electrode active material, where the negative electrode active material has a median particle size D<NUM>v50; under a pressure of <NUM> t, the negative electrode active material has a median particle size D<NUM>v50, and D<NUM>v50/D<NUM>v50 is greater than or equal to <NUM>. In some embodiments, D<NUM>v50/D<NUM>v50 of the negative electrode active material is greater than or equal to <NUM>. In some embodiments, D<NUM>v50/D<NUM>v50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>. D<NUM>v50/D<NUM>v50 of the negative electrode active material may reflect a change rate of a particle size of the negative electrode active material after being compressed. A larger value of D<NUM>v50/D<NUM>v50 of the negative electrode active material leads to a lower particle crushing degree of the negative electrode active material after being compressed, a smaller quantity of crushed particles, a lower ratio of crushed particles to total particles of the negative electrode active material (that is, a particle crushing rate), and higher strength of the negative electrode active material, so that crushed surfaces of the negative electrode active material that are not coated with a binder due to compression are reduced. This can inhibit formation of a solid electrolyte interface (SEI) film and help to increase a capacity and an initial coulomb efficiency and reduce a post-cycling thickness swelling rate of a lithium-ion battery. When D<NUM>v50/D<NUM>v50 of the negative electrode active material falls within the foregoing range, the negative electrode active material has high strength, which helps to achieve a balance between a high gram capacity and a low post-cycling thickness swelling rate of the lithium-ion battery.

The negative electrode active material used in this application can be obtained by the following method: adding a high-viscosity additive to primary particles of the negative electrode active material to obtain a mixture, and sintering the mixture to obtain secondary particles of the negative electrode active material, where the high-viscosity additive includes at least one of oil-based high-temperature asphalt, coal-based high-temperature asphalt, or a resin polymer material, and a content percentage of the high-viscosity additive is not more than <NUM> wt% based on a total weight of the negative electrode active material.

According to the present invention, a median particle size D<NUM>v50 of the negative electrode active material is <NUM> to <NUM>. In some embodiments, D<NUM>v50 of the negative electrode active material is <NUM> to <NUM>. In some embodiments, D<NUM>v50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>.

According to this embodiment of this application, under a pressure of <NUM> t, a median particle size D<NUM>v50 of the negative electrode active material is <NUM> to <NUM> In some embodiments, D<NUM>v50 of the negative electrode active material is <NUM> to <NUM>. In some embodiments, D<NUM>v50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>.

According to the present invention, D<NUM>v90 and D<NUM>v10 of the negative electrode active material satisfy that D<NUM>v90/D<NUM>v10 is less than <NUM>. In some embodiments, D<NUM>v90/D<NUM>v10 of the negative electrode active material is less than <NUM>. In some embodiments, D<NUM>v90/D<NUM>v10 of the negative electrode active material is less than <NUM>. In some embodiments, D<NUM>v90/D<NUM>v10 of the negative electrode active material is less than <NUM>.

According to the present invention, the negative electrode active material includes crystal grains, and according to an X-ray diffraction measurement, a grain size La of the crystal grains in a horizontal direction is <NUM> to <NUM>, and a grain size Lc of the crystal grains in a vertical direction is <NUM> to <NUM>. In some embodiments, the negative electrode active material includes crystal grains, and according to an X-ray diffraction measurement, a grain size La of the crystal grains in a horizontal direction is <NUM> to <NUM>, and a grain size Lc of the crystal grains in a vertical direction is <NUM> to <NUM>. In some embodiments, according to an X-ray diffraction method, a grain size La of the graphite particles in a horizontal direction is <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>, and a grain size Lc of the graphite particles in a vertical direction is <NUM>, <NUM>, or <NUM>.

According to this embodiment of this application, the negative electrode active material includes graphite particles, and the graphite particles have the same D<NUM>v50, D<NUM>v50, D<NUM>v90, and D<NUM>v10 as the negative electrode active material. In some embodiments, the negative electrode active material is graphite particles.

According to this embodiment of this application, the negative electrode active material has a specific surface area BET<NUM>, BET<NUM> is <NUM><NUM>/g to <NUM><NUM>/g; under a pressure of <NUM> t, the negative electrode active material has a specific surface area BET<NUM>, and (BET<NUM>-BET<NUM>)/BET<NUM>≤<NUM>. When the negative electrode active material satisfies that (BET<NUM>-BET<NUM>)/BET<NUM>≤<NUM>, a growth rate of the specific surface area of the negative electrode active material after being compressed is less than or equal to <NUM>% compared with the negative electrode active material without being compressed. A lower growth rate of the specific surface area of the negative electrode active material leads to higher strength of the negative electrode active material, so that crushed surfaces of the negative electrode active material that are not coated with a binder due to compression are reduced, and a quantity of formed solid electrolyte interface (SEI) films is reduced. This helps to increase a capacity and an initial coulomb efficiency and reduce a post-cycling thickness swelling rate of a lithium-ion battery.

In some embodiments, BET<NUM> is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> is <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, or <NUM><NUM>/g.

According to this embodiment of this application, under a pressure of <NUM> t, the specific surface area BET<NUM> of the negative electrode active material is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> of the negative electrode active material is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> of the negative electrode active material is <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, or <NUM><NUM>/g.

Parameters of the negative electrode active material under the pressure of <NUM> t may be obtained by referring to the steps in China National Standard GB/T24533-<NUM>.

The specific surface area of the negative electrode active material may be obtained by the following method:.

A specific surface area analyzer (for example, Tristar II <NUM>) is used to measure the specific surface area of the negative electrode active material by using a nitrogen adsorption/desorption method: drying a sample of the negative electrode active material in a vacuum drying oven, putting the sample into a sample tube, and measuring the sample in the analyzer. This application provides an electrochemical device, where the electrochemical device includes a negative electrode, and the negative electrode includes a negative electrode current collector and a negative electrode active material layer.

In the electrochemical device of this application, the negative electrode active material layer includes the negative electrode active material according to this application.

According to this embodiment of this application, the negative electrode active material layer includes the carbon element and the oxygen element, where a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM> to <NUM>:<NUM>. In some embodiments, a ratio of the carbon element content to the oxygen element content is <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, <NUM>:<NUM>, or <NUM>:<NUM>. When the ratio of the carbon element content to the oxygen element content in the negative electrode active material layer falls within the foregoing range, a particle size and a graphitization degree of particles of the negative electrode active material fall within a suitable range, which helps to increase a capacity and reduce a post-cycling thickness swelling rate of a lithium-ion battery.

According to the present invention, in the negative electrode active material layer, as measured through an X-ray diffraction spectrum, a ratio C004/C110 of the negative electrode active material layer is <NUM> to <NUM>, C004 is a peak area of a (<NUM>) plane of the negative electrode active material layer, C110 is a peak area of a (<NUM>) plane of the negative electrode active material layer. The C004/C110 value of the negative electrode active material layer measured through the X-ray diffraction spectrum may reflect anisotropy of the particles of the negative electrode active material. A smaller C004/C110 value leads to lower anisotropy, which helps to reduce the post-cycling thickness swelling rate of the lithium-ion battery. In some embodiments, C004/C110 of the negative electrode active material layer is <NUM> to <NUM>. In some embodiments, C004/C110 of the negative electrode active material layer is <NUM> to <NUM>.

According to this embodiment of this application, a porosity of the negative electrode active material layer is <NUM>% to <NUM>%. In some embodiments, the porosity of the negative electrode active material layer is <NUM>% to <NUM>%. In some embodiments, the porosity of the negative electrode active material layer is <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, or <NUM>%.

According to this embodiment of this application, when the electrochemical device is in a fully discharged state, as measured through an X-ray diffraction spectrum, a ratio C004'/C110' is <NUM> to <NUM>, C004' is a peak area of a (<NUM>) plane of the negative electrode active material, C110' is a peak area of a (<NUM>) plane of the negative electrode active material. In some embodiments, C004'/C110' of the negative electrode active material is <NUM> to <NUM>. In some embodiments, C004'/C110' of the negative electrode active material is <NUM> to <NUM>. In some embodiments, C004'/C110' of the negative electrode active material is <NUM> to <NUM>. When C004'/C110' of the negative electrode active material is <NUM> to <NUM>, the anisotropy of the particles of the negative electrode active material in the electrochemical device in a fully discharged state is still low, which can reflect that the negative electrode active material has high strength.

According to this embodiment of this application, when the electrochemical device is in a fully discharged state, the negative electrode active material has a median particle size Dav50, the negative electrode active material has a median particle size Dbv50 under a pressure of <NUM> t, and Dbv50/Dav50 is not less than <NUM>. Dbv50/Dav50 of the negative electrode active material may reflect the particle crushing degree of the negative electrode active material in the electrochemical device in the fully discharged state. A larger value of Dbv50/Dav50 of the negative electrode active material leads to a lower particle crushing degree of the negative electrode active material in the electrochemical device in the fully discharged state after being compressed, a smaller quantity of crushed particles, a lower ratio of crushed particles to total particles of the negative electrode active material (that is, a particle crushing rate), and higher strength of the negative electrode active material. When Dbv50/Dav50 of the negative electrode active material falls within the foregoing range, the negative electrode active material in the electrochemical device in the fully discharged state still has high strength, which helps to further increase the initial coulomb efficiency of the lithium-ion battery and reduce the post-cycling thickness swelling rate of the lithium-ion battery. In some embodiments, Dbv50/Dav50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, or <NUM>.

According to this embodiment of this application, when the electrochemical device is in a fully discharged state, a median particle size Dav50 of the negative electrode active material is <NUM> to <NUM>. In some embodiments, Dav50 of the negative electrode active material is <NUM> to <NUM>. In some embodiments, Dav50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>.

According to this embodiment of this application, when the electrochemical device is in a fully discharged state, a median particle size Dbv50 of the negative electrode active material under a pressure of <NUM> t is <NUM> to <NUM>. In some embodiments, Dbv50 of the negative electrode active material is <NUM> to <NUM>. In some embodiments, Dbv50 of the negative electrode active material is <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>.

According to this embodiment of this application, when the electrochemical device is in a fully discharged state, the negative electrode active material has a specific surface area BETa; under a pressure of <NUM> t, the negative electrode active material has a specific surface area BETb, and (BETb-BETa)/BETa<<NUM>. When the negative electrode active material satisfies that (BETb-BETa)BETa<<NUM>, a growth rate of the specific surface area of the negative electrode active material after being compressed is less than <NUM>% compared with the negative electrode active material without being compressed. When the specific surface area of the negative electrode active material in the electrochemical device in the fully discharged state conforms to the foregoing relationship, it can reflect that strength of the negative electrode active material is relatively high.

According to this embodiment of this application, when the electrochemical device is in a fully discharged state, a specific surface area BETa of the negative electrode active material is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BETa of the negative electrode active material is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BETa of the negative electrode active material is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BETa of the negative electrode active material is <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, or <NUM><NUM>/g.

According to this embodiment of this application, when the electrochemical device is in a fully discharged state, under a pressure of <NUM> t, a specific surface area BETb of the negative electrode active material is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> of the negative electrode active material is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> of the negative electrode active material is <NUM><NUM>/g to <NUM><NUM>/g. In some embodiments, BET<NUM> of the negative electrode active material is <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, <NUM><NUM>/g, or <NUM><NUM>/g.

According to this embodiment of this application, the negative electrode current collector used for this application may be selected from copper foil, nickel foil, stainless steel foil, titanium foil, nickel foam, copper foam, a polymer base coated with conductive metal, and a combination thereof.

According to this embodiment of this application, the negative electrode further includes a conductive layer. In some embodiments, a conductive material of the conductive layer may include any conductive material that causes no chemical change. Non-limiting examples of the conductive material include: a carbon-based material (for example, natural graphite, artificial graphite, carbon black, acetylene black, Ketjen black, carbon fiber, carbon nanotubes, and graphene), a metal-based material (for example, metal powder, and metal fiber, such as copper, nickel, aluminum, and silver), a conductive polymer (for example, a polyphenylene derivative), and any mixture thereof.

According to this embodiment of this application, the negative electrode further includes a binder, and the binder is selected from at least one of the following: polyvinyl alcohol, carboxymethyl cellulose, hydroxypropyl cellulose, diacetyl cellulose, polyvinyl chloride, carboxylated polyvinyl chloride, polyvinyl fluoride, a polymer containing ethylene oxide, polyvinylpyrrolidone, polyurethane, polytetrafluoroethylene, poly(vinylidene fluoride), polyethylene, polypropylene, styrene-butadiene rubber, acrylic styrene-butadiene rubber, epoxy resin, or nylon.

According to this embodiment of this application, the negative electrode can be manufactured by any method known in the prior art. In some embodiments, the negative electrode can be formed by adding a binder and a solvent into the negative electrode active material, adding a thickener, a conductive material, and a filler as needed to make a slurry, coating the slurry on the current collector, and performing compression after drying.

According to this embodiment of this application, when the negative electrode includes an alloy material, the negative electrode active material layer can be formed by using methods such as vapor deposition method, sputtering method, and plating method.

The positive electrode includes a positive electrode current collector and a positive electrode active material provided on the positive electrode current collector. The specific types of the positive electrode active material are not subject to specific restrictions, and can be selected according to requirements.

According to this embodiment of this application, the positive electrode active material includes a compound that reversibly intercalates and deintercalates a lithium ion. In some embodiments, the positive electrode active material may include a composite oxide, and the composite oxide contains lithium and at least one element selected from cobalt, manganese, and nickel. In still other embodiments, the positive electrode active material is selected from one or more of lithium cobalt oxide (LiCoO<NUM>), a lithium nickel manganese cobalt ternary material, lithium manganese oxide (LiMn<NUM>O<NUM>), lithium nickel manganese oxide (LiNi<NUM>Mn<NUM>O<NUM>), and lithium iron phosphate (LiFePO<NUM>).

According to this embodiment of this application, a positive electrode active material layer may have a coating on a surface, or may be mixed with another compound having a coating. The coating may include at least one compound of a coating element selected from oxides of the coating element, hydroxides of the coating element, oxyhydroxides of the coating element, oxycarbonates (oxycarbonate) of the coating element, and hydroxycarbonates (hydroxycarbonate) of the coating element. The compound used for coating may be amorphous or crystalline. The coating element contained in the coating may include Mg, Al, Co, K, Na, CA, Si, Ti, V, Sn, Ge, Ga, B, As, Zr, F, or a combination thereof. The coating may be applied by any method as long as the method does not adversely affect the performance of the positive electrode active material. For example, the method may include any coating method well known to those of ordinary skill in the art, for example, spraying and dipping.

According to this embodiment of this application, the positive electrode active material layer further includes a binder, and optionally, further includes a positive electrode conductive material.

The binder enhances binding between particles of the positive electrode active material, and binding between the positive electrode active material and the current collector. Non-limiting examples of the binder include: polyvinyl alcohol, hydroxypropyl cellulose, diacetyl cellulose, polyvinyl chloride, carboxylated polyvinyl chloride, polyvinyl fluoride, a polymer containing ethylene oxide, polyvinylpyrrolidone, polyurethane, polytetrafluoroethylene, poly(vinylidene fluoride), polyethylene, polypropylene, styrene-butadiene rubber, acrylic styrene-butadiene rubber, epoxy resin, and nylon.

The positive electrode active material layer includes the positive electrode conductive material, making the electrodes conductive. The positive electrode conductive material may include any conductive material that causes no chemical change. Non-limiting examples of the positive electrode conductive material include: a carbon-based material (for example, natural graphite, artificial graphite, carbon black, acetylene black, Ketjen black, and carbon fiber), a metal-based material (for example, metal powder, and metal fiber, including copper, nickel, aluminum, silver, and the like), a conductive polymer (for example, a polyphenylene derivative), and a mixture thereof.

The positive electrode current collector used in the electrochemical device according to this application may be, but is not limited to, aluminum (Al).

An electrolytic solution which can be used in the embodiments of this application may be an electrolytic solution known in the prior art. An electrolyte that can be used in the electrolyte solution of the embodiments of this application includes, but is not limited to: inorganic lithium salts, such as LiClO<NUM>, LiAsF<NUM>, LiPF<NUM>, LiBF<NUM>, LiSbF<NUM>, LiSO<NUM>F, and LiN(FSO<NUM>)<NUM>; fluorine-containing organic lithium salts, such as LiCF<NUM>SO<NUM>, LiN(FSO<NUM>)(CF<NUM>SO<NUM>), LiN(CF<NUM>SO<NUM>)<NUM>, LiN(C<NUM>F<NUM>SO<NUM>)<NUM>, cyclic <NUM>,<NUM>-hexafluoropropane disulfonimide lithium, cyclic <NUM>,<NUM>-tetrafluoroethane disulfonimide lithium, LiN(CF<NUM>SO<NUM>)(C<NUM>F<NUM>SO<NUM>), LiC(CF<NUM>SO<NUM>)<NUM>, LiPF<NUM>(CF<NUM>)<NUM>, LiPF<NUM>(C<NUM>F<NUM>)<NUM>, LiPF<NUM>(CF<NUM>SO<NUM>)<NUM>, LiPF<NUM>(C<NUM>F<NUM>SO<NUM>)<NUM>, LiBF<NUM>(CF<NUM>)<NUM>, LiBF<NUM>(C<NUM>F<NUM>)<NUM>, LiBF<NUM>(CF<NUM>SO<NUM>)<NUM>, and LiBF<NUM>(C<NUM>F<NUM>SO<NUM>)<NUM>; lithium salts containing dicarboxylic acid complex, such as bis(oxalato) lithium borate, difluorooxalato lithium borate, tris(oxalato) lithium phosphate, difluorobis (oxalato) lithium phosphate, and tetrafluoro(oxalato) lithium phosphatee. In addition, the above electrolyte may be used alone, or two or more electrolytes may be used simultaneously. For example, in some embodiments, the electrolyte includes a combination of LiPF<NUM> and LiBF<NUM>. In some embodiments, the electrolyte includes a combination of an inorganic lithium salt such as LiPF<NUM> or LiBF<NUM> and a fluorine-containing organic lithium salt such as LiCF<NUM>SO<NUM>, LiN(CF<NUM>SO<NUM>)<NUM>, and LiN(C<NUM>F<NUM>SO<NUM>)<NUM>.

In some embodiments, a concentration of the electrolyte falls within a range of <NUM> mol/L to <NUM> mol/L, for example, a range of <NUM> mol/L to <NUM> mol/L, a range of <NUM> mol/L to <NUM> mol/L, a range of <NUM> mol/L to <NUM> mol/L, for another example, <NUM> mol/L, <NUM> mol/L, <NUM> mol/L, <NUM> mol/L, <NUM> mol/L, or <NUM> mol/L.

A solvent that can be used in the electrolyte solution of the embodiments of this application includes, but is not limited to, a carbonate compound, an ester-based compound, an ether-based compound, a ketone-based compound, an alcohol-based compound, an aprotic solvent, or a combination thereof.

An example of the carbonate compound includes, but is not limited to, a linear carbonate compound, a cyclic carbonate compound, a fluorocarbonate compound, or a combination thereof.

An example of the linear carbonate compound includes, but is not limited to, diethyl carbonate (DEC), dimethyl carbonate (DMC), dipropyl carbonate (DPC), methyl propyl carbonate (MPC), ethylene propyl carbonate (EPC), ethyl methyl carbonate (MEC), or a combination thereof. An example of the cyclic carbonate compound is ethylene carbonate (EC), propylene carbonate (PC), butylene carbonate (BC), vinyl ethylene carbonate (VEC), or a combination thereof. An example of the fluorocarbonate compound is fluoroethylene carbonate (FEC), <NUM>,<NUM>-difluoro-<NUM>,<NUM>-dioxolan-<NUM>-one, <NUM>,<NUM>-difluoro-<NUM>,<NUM>-dioxolan-<NUM>-one, <NUM>,<NUM>,<NUM>-trifluoro-<NUM>,<NUM>-dioxolan-<NUM>-one, <NUM>,<NUM>,<NUM>,<NUM>-tetrafluoro-<NUM>,<NUM>-dioxolan-<NUM>-one, <NUM>-fluoro-<NUM>-methyl-<NUM>,<NUM>-dioxolan-<NUM>-one, <NUM>-fluoro-<NUM>-methyl-<NUM>,<NUM>-dioxolan-<NUM>-one, <NUM>,<NUM>-difluoro-<NUM>-methyl-<NUM>,<NUM>-dioxolan-<NUM>-one, <NUM>,<NUM>,<NUM>-trifluoro-<NUM>-methyl-<NUM>,<NUM>-dioxolan-<NUM>-one, <NUM>-(trifluoromethyl)-<NUM>,<NUM>-dioxolan-<NUM>-one, or a combination thereof.

An example of the carboxylate compound includes, but is not limited to, methyl acetate, ethyl acetate, n-propyl acetate, tert-butyl acetate, methyl propionate, ethyl propionate, γ-butyrolactone ester, caprolactone, valerolactone, mevalonolactone, caprolactone, methyl formate, or a combination thereof.

An example of the ether compound includes, but is not limited to, dibutyl ether, tetraglyme, diglyme, <NUM>,<NUM>-dimethoxyethane, <NUM>,<NUM>-diethoxyethane, ethoxymethoxyethane, <NUM>-methyltetrahydrofuran, tetrahydrofuran, or a combination thereof.

An example of the ketone-based compound includes, but is not limited to, cyclohexanone.

An example of the alcohol-based compound includes, but is not limited to, ethanol and isopropanol.

An example of the aprotic solvent includes, but is not limited to, dimethyl sulfoxide, <NUM>,<NUM>-dioxolane, sulfolane, methyl sulfolane, <NUM>,<NUM>-dimethyl-<NUM>-imidazolidinone, N-methyl -<NUM>-pyrrolidone, formamide, dimethylformamide, acetonitrile, nitromethane, trimethyl phosphate, triethyl phosphate, trioctyl phosphate, phosphate ester, or a combination thereof.

In some embodiments, a separator is provided between the positive electrode and the negative electrode to prevent a short circuit. A material and shape of the separator which can be used in the embodiments of this application may include any technology disclosed in the prior art. In some embodiments, the separator includes a polymer or an inorganic substance formed by a material stable to the electrolytic solution of this application.

For example, the separator may include a substrate layer and a surface treatment layer. The substrate layer is a non-woven fabric, a membrane or a composite membrane having a porous structure, and a material of the substrate layer is selected from at least one of polyethylene, polypropylene, polyethylene terephthalate, and polyimide. Specifically, a polypropylene porous membrane, a polyethylene porous membrane, a polypropylene non-woven fabric, a polyethylene non-woven fabric or a polypropylene-polyethylene-polypropylene porous composite membrane can be selected. The porous structure can increase heat resistance, oxidation resistance, and electrolyte infiltration performance of the separator, and enhance adhesion between the separator and electrodes.

The surface treatment layer is provided on at least one surface of the substrate layer, and the surface treatment layer may be a polymer layer or an inorganic layer, or may be a layer formed by a mixed polymer and an inorganic substance.

The inorganic layer includes inorganic particles and a binder. The inorganic particles are selected from one or a combination of aluminum oxide, silicon oxide, magnesium oxide, titanium oxide, hafnium oxide, tin oxide, ceria oxide, nickel oxide, zinc oxide, calcium oxide, zirconium oxide, yttrium oxide, silicon carbide, boehmite, aluminum hydroxide, magnesium hydroxide, calcium hydroxide, and barium sulfate. The binder is selected from one or a combination of polyvinylidene fluoride, a vinylidene fluoride-hexafluoropropylene copolymer, polyamide, polyacrylonitrile, polyacrylate, polyacrylic acid, polyacrylate, polyvinylpyrrolidone, polyvinyl ether, polymethyl methacrylate, polytetrafluoroethylene and polyhexafluoropropylene.

The polymer layer contains a polymer, and a material of the polymer is selected from at least one of polyamide, polyacrylonitrile, an acrylate polymer, polyacrylic acid, polyacrylate, polyvinylpyrrolidone, polyvinyl ether, polyvinylidene fluoride, or poly(vinylidene fluoride-hexafluoropropylene).

The electrochemical device according to this application includes any device in which electrochemical reactions take place. Specific examples of the device include all kinds of primary batteries, secondary batteries, fuel batteries, solar batteries, or capacitors. Especially, the electrochemical device is a lithium secondary battery, including lithium metal secondary batteries, lithium-ion secondary batteries, lithium polymer secondary batteries, or lithium-ion polymer secondary batteries.

This application further provides an electronic device, including the electrochemical device according to this application.

The electrochemical device of this application is not particularly limited to any purpose, and may be used for any known electronic device in the prior art. In some embodiments, the electrochemical device of this application may be used for, without limitation to: a notebook computer, a pen-input computer, a mobile computer, an electronic book player, a portable telephone, a portable fax machine, a portable copier, a portable printer, a stereo headset, a video recorder, a liquid crystal television, a portable cleaner, a portable CD player, a mini-disc, a transceiver, an electronic notebook, a calculator, a memory card, a portable recorder, a radio, a standby power source, a motor, an automobile, a motorcycle, a motor bicycle, a bicycle, a lighting appliance, a toy, a game console, a clock, an electric tool, a flash lamp, a camera, a large household battery, a lithium-ion capacitor, or the like.

Lithium-ion batteries are used as an example below in combination with specific examples to describe preparation of a lithium-ion battery. Those skilled in the art should understand that the preparation method described in this application is only an example, and any other suitable preparation methods are within the scope of this application.

Performance evaluation is carried out below based on examples and comparative examples of the lithium-ion battery according to this application.

Coke was crushed so that its median particle size Dv50 fell within a range of <NUM> to <NUM>, and then a binder asphalt with a softening point of <NUM> to <NUM> was added (amounts of the added asphalt in Examples <NUM> to <NUM> and <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, and <NUM>, and Reference Examples <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM> and <NUM>, were <NUM> wt%, and an amount of the added asphalt in Example <NUM> was <NUM> wt%). A mixture of the two was put into granulation equipment for granulation, during which the mixture was continuously stirred and heated to <NUM> to <NUM>, then a graphitization process (in which a graphitization temperature was controlled at <NUM> to <NUM>) was performed, and a graphite negative electrode active material used in the following examples was obtained.

The coke was crushed so that its median particle size Dv50 fell within the range of <NUM> to <NUM>, a mixture was put into granulation equipment for granulation, during which the mixture was continuously stirred and heated to <NUM> to <NUM>, then a graphitization process (in which a graphitization temperature was controlled at <NUM> to <NUM>) was performed, and a graphite negative electrode active material used in Comparative Example <NUM> was obtained.

The prepared graphite negative electrode active material, styrene-butadiene rubber (SBR), and sodium carboxymethyl cellulose (CMC) were dispersed in deionized water at a weight ratio of <NUM>:<NUM>:<NUM>, fully stirred and mixed uniformly to obtain a negative electrode slurry. The negative electrode slurry was coated on a negative electrode current collector, dried, and cold pressed to form a negative electrode active material layer, and then the current collector was cut and welded with tabs to obtain a negative electrode.

Graphite particles of different particle sizes could be obtained by crushing and grading raw materials by using any known technology.

Lithium cobaltate (LiCoO<NUM>), acetylene black, and polyvinylidene fluoride (PVDF) were fully stirred and well mixed in an appropriate amount of N-methylpyrrolidone (NMP) at a weight ratio of <NUM>:<NUM>:<NUM>, a mixture was coated on a positive electrode current collector fluid aluminum foil, dried and cold pressed to form a positive electrode active material layer, and then the current collector was cut and welded with tabs to obtain a positive electrode.

In a dry argon environment, ethylene carbonate (EC), propylene carbonate (PC), and diethyl carbonate (DEC) were mixed at a weight ratio of <NUM>:<NUM>:<NUM>, and LiPF<NUM> was added and mixed well. <NUM>% fluoroethylene carbonate was added and mixed well to obtain the electrolyte solution, in which a concentration of LiPF<NUM> was <NUM> mol/L.

A polyethylene (PE) porous polymer film with a thickness of <NUM> was used as the separator.

The positive electrode, separator, and negative electrode were stacked in order, so that the separator was placed between the positive electrode plate and the negative electrode plate for separation. Then the battery was wound with tabs welded thereto and was placed in an outer packaging aluminum foil film. Then the foregoing prepared electrolyte solution was injected, followed by processes such as vacuum packaging, standing, chemical conversion, shaping and capacity testing, to obtain a lithium-ion battery.

A Malvern particle size tester was used to measure a particle size of the negative electrode active material: A sample of the negative electrode active material was dispersed in dispersant ethanol, and ultrasonicated for <NUM> minutes. The sample was put into the Malvern particle size tester to test Dv50, Dv10, and Dv90 of the negative electrode active material.

A specific surface area analyzer (Tristar II <NUM>) was used to measure a specific surface area of the negative electrode active material by using a nitrogen adsorption/desorption method: A sample of the negative electrode active material was added into a vacuum drying oven for drying, and then was put into a sample tube to measure the sample in the analyzer.

The lithium-ion battery was discharged at <NUM> C to <NUM> mV, at <NUM>µA to <NUM> mV, at <NUM>µA to <NUM> mV, and charged at <NUM> C to <NUM> V. A capacity of the lithium-ion battery was recorded at this time as a gram capacity. <NUM> C is a current value under <NUM> times the designed gram capacity, and <NUM> C is a current value under <NUM> times the designed gram capacity.

At <NUM>, a micrometer was used to test a thickness of the lithium-ion battery in an initial half-charged state, which was denoted as H<NUM>. The lithium-ion battery was charged and discharged for <NUM> cycles at a rate of <NUM> C, during which, after each <NUM> cycles, the thickness of the lithium-ion battery in the fully charged state was measured and denoted as Hn. The post-cycling thickness swelling rate of the lithium-ion battery was calculated based on the following formula: <MAT>.

The lithium-ion battery was charged at <NUM> C to <NUM> V, and an initial charge capacity C was recorded. Then the lithium-ion battery was discharged at <NUM> C to <NUM> V, and its discharge capacity D was recorded. The initial coulomb efficiency CE of the lithium-ion battery was calculated based on the following formula: <MAT>.

Table <NUM> shows influence of characteristics of the negative electrode active material on the gram capacity and post-cycling thickness swelling rate of the lithium-ion battery during the preparation of the negative electrode active material.

As shown in Comparative Example <NUM>, no high-viscosity binder was added during the preparation of the negative electrode active material, the negative electrode active material was primary particles, and the primary particles were not recombined to form secondary particles. Although the resulting lithium-ion battery had a relatively high gram capacity, the negative electrode active material had relatively high anisotropy, leading to a high post-cycling thickness swelling rate of the lithium-ion battery and poor performance.

As shown in Examples <NUM> to <NUM>, and <NUM> to <NUM> and Reference Examples <NUM>, <NUM>, and <NUM>, when the negative electrode active material was prepared, an appropriate amount of high-viscosity binder was added so that D<NUM>v50/D<NUM>v50 of the negative electrode active material was not less than <NUM>. In this way, the lithium-ion battery not only had a high gram capacity, but also had a low post-cycling thickness swelling rate, implementing balance between a high gram capacity and a low post-cycling thickness swelling rate.

When a content percentage of the high-viscosity binder was constant, and when the median particle size D<NUM>v50 of the negative electrode active material was gradually increased in the range of <NUM> to <NUM>, a ratio D<NUM>v50/D<NUM>v50 of the median particle size D<NUM>v50 of the negative electrode active material under a pressure of <NUM> t to D<NUM>v50 was decreased, (BET<NUM>-BET<NUM>)/BET<NUM> of the negative electrode active material was increased, and the weight ratio of the carbon element to the oxygen element was increased, so that the gram capacity of the lithium-ion battery was increased and the post-cycling thickness swelling rate was decreased. When the specific surface area of the negative electrode active material satisfied that BET<NUM> fell within the range of <NUM><NUM>/g to <NUM><NUM>/g and (BET<NUM>-BET<NUM>)/BET<NUM>≤<NUM> and/or a content ratio of the carbon element to the oxygen element in the negative electrode active material layer fell within a range of <NUM>:<NUM> to <NUM>:<NUM>, further balance between a high gram capacity and a low post-cycling thickness swelling rate could be achieved.

Table <NUM> shows influence of D<NUM>v90/D<NUM>v10 and C004/C110 of the negative electrode active material on the initial coulomb efficiency and post-cycling thickness swelling rate of the lithium-ion battery. Except for parameters listed in Table <NUM>, conditions of Examples <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, and <NUM>, and Reference Examples <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, and <NUM> were the same as those of Reference Example <NUM>.

The results show that when D<NUM>v90/D<NUM>v10 of the negative electrode active material was less than <NUM>, the initial coulomb efficiency of the lithium-ion battery was significantly increased. When D<NUM>v90/D<NUM>v10 of the negative electrode active material was gradually decreased in the range of less than <NUM>, the initial coulomb efficiency of the lithium-ion battery did not change much, and the post-cycling thickness swelling rate was gradually decreased. When C004/C110 of the negative electrode active material layer was gradually decreased in the range of <NUM> to <NUM>, the grain size La of the graphite particles was decreased, Lc was increased, the porosity was increased, the post-cycling thickness swelling rate of the lithium-ion battery was gradually decreased, and the initial coulomb efficiency was slightly decreased. In conclusion, when the negative electrode active material satisfied that D<NUM>v90/D<NUM>v10 was less than <NUM>, C004/C110 fell within the range of <NUM> to <NUM>, La was <NUM> to <NUM>, Lc was <NUM> to <NUM>, and/or the porosity was <NUM>% to <NUM>%, the lithium-ion battery achieved a balance between the initial coulomb efficiency and the post-cycling thickness swelling rate.

Table <NUM> shows influence of characteristics of the negative electrode active material on the initial coulomb efficiency and post-cycling thickness swelling rate of the lithium-ion battery when the lithium-ion battery is in a fully discharged state.

The results show that when the lithium-ion battery was in the fully discharged state, Dbv50/Dav50 of the negative electrode active material and (BETb-BETa)/BETa of the negative electrode active material would affect the increase of the initial coulomb efficiency of the lithium-ion battery, and would also affect the post-cycling thickness swelling rate of the lithium-ion battery.

Figure shows post-cycling thickness swelling rates of lithium-ion batteries against a quantity of cycles in Reference Example <NUM> and Comparative Example <NUM>. The results show that compared to Comparative Example <NUM>, the lithium-ion battery in Reference Example <NUM> had a significantly lower post-cycling thickness swelling rate. As a quantity of cycles increased, a difference between the post-cycling thickness swelling rates of the two was significant.

Claim 1:
An electrochemical device comprising a negative electrode, the negative electrode comprises a negative electrode current collector and a negative electrode active material layer, and the negative electrode active material layer comprising a negative electrode active material, characterized in that, the negative electrode active material is graphite particles and has a median particle size D<NUM>v50; after being compressed under a pressure of <NUM> t, the negative electrode active material has a median particle size D<NUM>v50 as measured in accordance with China National Standard GB/T24533-<NUM>, and D<NUM>v50/D<NUM>v50 is greater than or equal to <NUM>;
wherein D<NUM>v50 is <NUM> to <NUM>;
D<NUM>v90 and D<NUM>v10 of the graphite particles satisfy that D<NUM>v90/D<NUM>v10 is less than <NUM>;
wherein according to an X-ray diffraction measurement, a grain size La of the graphite particles in a horizontal direction is <NUM> to <NUM>, and a grain size Lc of the graphite particles in a vertical direction is <NUM> to <NUM>; and
as measured through an X-ray diffraction spectrum, a ratio C004/C110 of the negative electrode active material layer is <NUM> to <NUM>, C004 is a peak area of a (<NUM>) plane of the negative electrode active material layer, C110 is a peak area of a (<NUM>) plane of the negative electrode active material layer.