WO2013073035A1 - 硫化物固体電解質の製造方法 - Google Patents
硫化物固体電解質の製造方法 Download PDFInfo
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- WO2013073035A1 WO2013073035A1 PCT/JP2011/076530 JP2011076530W WO2013073035A1 WO 2013073035 A1 WO2013073035 A1 WO 2013073035A1 JP 2011076530 W JP2011076530 W JP 2011076530W WO 2013073035 A1 WO2013073035 A1 WO 2013073035A1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0561—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
- H01M10/0562—Solid materials
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0065—Solid electrolytes
- H01M2300/0068—Solid electrolytes inorganic
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/60—Other road transportation technologies with climate change mitigation effect
- Y02T10/70—Energy storage systems for electromobility, e.g. batteries
Definitions
- the present invention relates to a method for producing a sulfide solid electrolyte.
- Lithium ion secondary batteries are characterized by higher energy density than other secondary batteries and capable of operating at high voltages. For this reason, it is used as a secondary battery that can be easily reduced in size and weight in information equipment such as a mobile phone, and in recent years, there is an increasing demand for large motive power such as for electric vehicles and hybrid vehicles.
- a lithium ion secondary battery includes a positive electrode and a negative electrode, and an electrolyte layer disposed between them.
- an electrolyte used for the electrolyte layer for example, a non-aqueous liquid or solid substance is known. ing.
- electrolytic solution a liquid electrolyte (hereinafter referred to as “electrolytic solution”)
- the electrolytic solution easily penetrates into the positive electrode and the negative electrode. Therefore, an interface between the active material contained in the positive electrode or the negative electrode and the electrolytic solution is easily formed, and the performance is easily improved.
- the widely used electrolyte is flammable, it is necessary to mount a system for ensuring safety.
- solid electrolyte that is flame retardant
- solid electrolyte layer a layer containing a solid electrolyte
- Patent Document 1 discloses a ball made of two or more kinds of balls having different diameters when manufacturing a sulfide-based solid electrolyte that manufactures a sulfide-based solid electrolyte using a ball mill. Techniques using groups are disclosed. In the paragraph 0018 of Patent Document 1, it is preferable that the two or more kinds of balls each have a ball diameter within a range of 5 to 40 mm ⁇ and that the ball diameter is smaller than 5 mm ⁇ . Describes that there is a possibility that a solid electrolyte with high conductivity cannot be synthesized because the energy per one is small.
- Patent Document 2 discloses a method for producing sulfide-based solid electrolyte fine particles having an average particle size of 0.1 to 10 ⁇ m by multistage grinding of sulfide-based solid electrolyte coarse particles in a non-aqueous solvent. .
- pulverization when pulverization is performed using a pulverizer that uses balls as pulverization media, comparison is preferably performed after pulverization with relatively large balls (1 mm ⁇ or more, preferably 1 to 50 mm ⁇ ). It describes that multistage pulverization is performed using a small ball (0.1 to 0.6 mm ⁇ ).
- JP 2010-90003 A Japanese Patent Laid-Open No. 2008-4459
- the particle size of the pulverized sulfide solid electrolyte needs to be within a predetermined range.
- the material, diameter, and peripheral speed of the grinding medium can be considered.
- the pulverization energy is controlled by the material of the pulverization medium, the pulverization medium having the same diameter is used, so that the atomization is hardly promoted.
- the solid electrolyte particles are agglomerated rapidly and become secondary particles, resulting in intergranular resistance.
- an object of the present invention is to provide a method for producing a sulfide solid electrolyte capable of improving the productivity of a sulfide solid electrolyte having a small average particle diameter.
- the present inventors have mixed at least one of a sulfide solid electrolyte and its raw material with a solvent, a pulverized media (ball, bead) having a diameter of less than 1 mm, and a diameter of 1 mm or more. It was found that a sulfide solid electrolyte having a small average particle size can be produced with good productivity by mechanically grinding simultaneously using grinding media (balls and beads). The present invention has been completed based on this finding.
- the present invention takes the following means. That is, The present invention includes a mixing step of mixing at least one of a sulfide solid electrolyte and its raw material and a solvent to obtain a mixture, a first grinding medium having a diameter of less than 1 mm, and a diameter of 1 mm or more. And a pulverization step of mechanically pulverizing the sulfide solid electrolyte using the second pulverization medium at the same time.
- grinding medium refers to media such as balls used in planetary ball mills and batch type ball mills, and beads used in circulating bead mills.
- the “sulfide solid electrolyte” pulverized in the pulverization step is, for example, the first pulverization medium
- the sulfide solid electrolyte is synthesized with the sulfide solid electrolyte raw material contained in the mixture after the mixture is put into an apparatus such as a planetary ball mill together with the second grinding medium.
- the sulfide solid electrolyte is manufactured through a pulverization process in which the mixture is mechanically pulverized using the first pulverization medium and the second pulverization medium at the same time.
- the pulverizing step the sulfide solid electrolyte having a large initial particle size is pulverized using the second pulverizing medium, and the pulverized sulfide solid electrolyte is further pulverized using the first pulverizing medium.
- the first grinding medium and the second grinding medium it becomes possible to obtain a sulfide solid electrolyte having a small average particle diameter.
- the sulfide solid electrolyte can be obtained. Productivity can be improved.
- the ether compound is preferably further mixed and pulverized in the pulverization step.
- the “ether compound” includes dimethyl ether, diethyl ether, dipropyl ether, dibutyl ether, cyclopentyl methyl ether, anisole and the like.
- the present invention it is possible to provide a method for producing a sulfide solid electrolyte capable of improving the productivity of a sulfide solid electrolyte having a small average particle diameter.
- FIG. 2 is a photograph showing a sulfide solid electrolyte of Example 1.
- FIG. 2 is a photograph showing a sulfide solid electrolyte of Example 2.
- 4 is a photograph showing a sulfide solid electrolyte of Example 3.
- 4 is a photograph showing a sulfide solid electrolyte of Example 4.
- 2 is a photograph showing a sulfide solid electrolyte of Comparative Example 1.
- 4 is a photograph showing a sulfide solid electrolyte of Comparative Example 2.
- 6 is a photograph showing a sulfide solid electrolyte of Comparative Example 3.
- 6 is a photograph showing a sulfide solid electrolyte of Comparative Example 3.
- 6 is a photograph showing a sulfide solid electrolyte of Comparative Example 4.
- 6 is a photograph showing a sulfide solid electrolyte of Comparative Example 5.
- FIG. 1 is a diagram for explaining a method for producing a sulfide solid electrolyte of the present invention (hereinafter sometimes referred to as “the production method of the present invention”).
- FIG. 2 is a diagram for explaining the production method of the present invention using sulfide solid electrolytes 1, 1,... In the mixing step.
- the manufacturing method of this invention has a mixing process (S1) and a grinding
- the mixing step (hereinafter sometimes referred to as “S1”) is a step of obtaining a mixture by mixing at least one of the sulfide solid electrolyte and its raw material with a solvent.
- S1 may be in a form in which a synthesized sulfide solid electrolyte 1, 1,... And solvent 2 are mixed to obtain a mixture.
- the form which mixes the raw material of a sulfide solid electrolyte and a solvent, and obtains a mixture may be sufficient, and the form which mixes the raw material of a sulfide solid electrolyte and a solvent and obtains a mixture may be sufficient.
- the sulfide solid electrolytes 1, 1,... Can be synthesized by, for example, the method described in Japanese Patent Application No. 2010-189965. Further, when the raw material of the sulfide solid electrolyte is used in S1, S1 can be a step of obtaining a mixture by a method described in JP 2010-186682A, for example.
- S2 the first pulverization media 3, 3,... Having a diameter of less than 1 mm and the second pulverization media 4, 4,.
- the sulfide solid electrolyte mechanically pulverized in S2 was included in the mixture.
- the sulfide solid electrolyte mechanically pulverized in S2 is synthesized in S2 when a mixture is obtained by mixing the raw material and the solvent of the sulfide solid electrolyte without using the sulfide solid electrolyte. Sulfide solid electrolyte.
- a sulfide solid electrolyte having a large initial particle size is mechanically treated using the second grinding media 4, 4,.
- the pulverized sulfide solid electrolyte is further mechanically pulverized using the first pulverizing media 3, 3.
- a sulfide solid electrolyte having a small average particle diameter can be obtained by mechanically pulverizing using the first pulverizing media 3, 3,... And the second pulverizing media 4, 4,. 3 and the second grinding media 4, 4,... Can be used at the same time to improve the productivity of the sulfide solid electrolyte having a small average particle size. Therefore, according to the production method of the present invention for producing a sulfide solid electrolyte through S1 and S2, the productivity of a sulfide solid electrolyte having a small average particle size can be improved.
- the sulfide solid electrolyte usable in the mixing step includes Li 2 S—SiS 2 , LiI—Li 2 S—SiS 2 , LiI—Li 2 SP—S 2 S 5 , LiI—Li 2 S—.
- P 2 O 5 , LiI—Li 3 PO 4 —P 2 S 5 , Li 2 S—P 2 S 5 , Li 3 PS 4 and the like can be exemplified.
- a sulfide solid electrolyte in which the total ratio of the molecular weights of Li, P, and S in the molecular weight of the sulfide solid electrolyte is 10% or more can be preferably used, and F, Cl, Br, and A sulfide solid electrolyte containing one or more elements selected from the group consisting of I can be preferably used.
- raw material for the sulfide solid electrolyte that can be used in the mixing step
- a known substance that can be used as the raw material for the sulfide solid electrolyte can be appropriately used.
- raw materials for such a sulfide solid electrolyte (i) Li 2 S and SiS 2 , (ii) LiI, Li 2 S, and SiS 2 , (iii) LiI, Li 2 S, and P 2 S 5 , (iv) LiI, Li 2 S, and P 2 O 5 , (v) LiI, Li 3 PO 4 , and P 2 S 5 , (vi) Li 2 S and P 2 S 5 , or these A mixture etc. can be mentioned.
- the solvent that can be used in the mixing step is not particularly limited, but a solvent that does not react with sulfide can be preferably used.
- a solvent that does not react with sulfide include saturated hydrocarbons and aromatic compounds such as benzene, toluene and xylene.
- the materials of the first pulverizing media 3, 3,... And the second pulverizing media 4, 4,... Used in the pulverizing step are not particularly limited, but ceramics that are not contaminated by metal can be preferably used.
- ceramics include zirconia, alumina, agate and the like. Among these, zirconia and alumina which are not easily contaminated by metal can be used more preferably.
- the diameter of the first grinding media 3, 3,... Used in the grinding process is not particularly limited as long as it is less than 1 mm.
- the diameter of the first grinding media 3, 3,... can be, for example, 0.1 mm or more and less than 1 mm.
- the diameter of the second grinding media 4, 4,... Used in the grinding process is not particularly limited as long as it is 1 mm or more.
- the diameter of the second grinding media 4, 4,... can be, for example, 1 mm or more and 5 mm or less.
- the pulverization step may be a step of mechanically pulverizing the sulfide solid electrolyte using the first pulverization media 3, 3,... And the second pulverization media 4, 4,.
- the method is not particularly limited. Examples of the pulverization method that can be used in the present invention include a method using a planetary ball mill, a circulation type bead mill, a batch type ball mill and the like.
- ether compounds that can be used in the present invention include dimethyl ether, diethyl ether, dipropyl ether, dibutyl ether, cyclopentyl methyl ether, and anisole.
- diethyl ether, dipropyl ether, and dibutyl ether having a low boiling point (60 ° C. or more and 200 ° C. or less) and low polarity can be preferably used.
- the mixing ratio of the first pulverizing media 3, 3,... And the second pulverizing media 4, 4,... Used in the pulverizing step is not particularly limited, but it is easy to obtain a sulfide solid electrolyte with small average particles. From the standpoint of form, etc., it is preferable that the number of first grinding media 3, 3,... Used is larger than the number of second grinding media 4, 4,.
- the form having the pulverization step using the first pulverization media 3, 3,... And the second pulverization media 4, 4, is not limited to two types.
- the grinding step includes one or more other grinding media in addition to the first grinding media 3, 3,... Having a diameter of less than 1 mm and the second grinding media 4, 4,.
- the present invention includes a process of mechanically pulverizing a sulfide solid electrolyte using a first pulverizing medium and a second pulverizing medium simultaneously while mixing at least one of the sulfide solid electrolyte and its raw material and a solvent. After that, it is also possible to adopt a form for producing sulfide solid electrolyte fine particles.
- the sulfide solid electrolyte produced by the production method of the present invention can be used for a solid electrolyte layer, a positive electrode, a negative electrode, and the like of a solid battery.
- Example 1 Mixing powder 1g of the sulfide solid electrolyte material, (10 g of ZrO 2 balls having a diameter of 1 mm, and the ZrO 2 balls having a diameter of 0.3 mm 30 g) grinding media 40 g, 8 g of a solvent (dehydrated heptane, Kanto Chemical And 1 g of additive (dibutyl ether) were put into a 45 ml ZrO 2 pot.
- a solvent dehydrated heptane, Kanto Chemical And 1 g of additive (dibutyl ether)
- Example 1 a sulfide solid electrolyte of Example 1 is obtained by performing a pulverization treatment for 10 hours under a condition of 150 revolutions per minute by a mechanical milling method using a planetary ball mill (manufactured by Fritsch, P7). It was.
- Example 2 A sulfide solid electrolyte of Example 2 was obtained under the same conditions as in Example 1 except that the pulverization time was 20 hours.
- Example 3 A sulfide solid electrolyte of Example 3 was obtained under the same conditions as in Example 1 except that the number of rotations of the pulverization treatment was 200 rpm.
- Example 4 The ZrO 2 balls having a diameter of 1 mm 20g and, except using 20g of ZrO 2 balls having a diameter of 0.3 mm, under the same conditions as those in Example 2, to give a sulfide solid electrolyte of Example 4.
- Comparative Example 2 A sulfide solid electrolyte of Comparative Example 2 was obtained under the same conditions as in Comparative Example 1 except that the number of rotations of the pulverization treatment was 100 revolutions per minute.
- Comparative Example 4 A sulfide solid electrolyte of Comparative Example 4 was obtained under the same conditions as in Comparative Example 3 except that the number of rotations of the pulverization treatment was 300 rpm.
- Comparative Example 5 A sulfide solid electrolyte of Comparative Example 5 was obtained under the same conditions as in Comparative Example 3 except that the number of rotations of the pulverization treatment was 450 rpm.
- Lithium ion conductivity measurement 0.1 g of each of the obtained sulfide solid electrolytes of Examples 1 to 4 and Comparative Examples 1 to 5 was weighed and pressed at a pressure of 421.4 MPa. Two pellets were made. Then, after adjusting the temperature to 25 ° C. using an isothermal layer in an environment not exposed to the atmosphere, the lithium ion conduction of each of the nine pellets was measured by the AC impedance method using a solartron 1260 manufactured by Toyo Corporation. The degree was measured.
- Results Table 1 shows the production conditions of the sulfide solid electrolyte, the lithium ion conductivity measurement results, and the particle size distribution measurement results of Examples 1 to 4 and Comparative Examples 1 to 5.
- D10 is the diameter of a grain having a cumulative particle size distribution of 10% from the fine particle side
- D50 is the diameter of a particle having a cumulative particle size distribution of 50% from the fine particle side
- D90 is a fine particle of the cumulative particle size distribution. It refers to the diameter of a grain that is 90% cumulative from the side.
- FIG. 3 shows the relationship between the average particle size and lithium ion conductivity of the sulfide solid electrolytes of Examples 1 to 4 and Comparative Examples 1 to 5.
- FIG. 3 shows the relationship between the average particle size and lithium ion conductivity of the sulfide solid electrolytes of Examples 1 to 4 and Comparative Examples 1 to 5.
- FIG. 3 shows the relationship between the average particle size and lithium ion conductivity of the sulfide solid electrolytes of Examples 1 to
- the vertical axis represents the lithium ion conductivity ⁇ [S / cm]
- the horizontal axis represents the average particle diameter D50 [ ⁇ m].
- the sulfide solid electrolytes of Examples 1 to 4 and Comparative Examples 1 to 5 were magnified 5000 times (FIGS. 4 to 10, 12, and 13) or 1000 times magnification (FIG. 11). The photographs observed in Fig. 4 are shown in Figs.
- the sulfide solid electrolytes of Examples 1 to 4 have a lithium ion conductivity of 1.0 ⁇ 10 ⁇ 3 S / cm or more and an average particle diameter D50 of 1.2 ⁇ m or less. Met. As shown in FIGS. 4 to 7, the sulfide solid electrolytes of Examples 1 to 4 had a small average particle size. In contrast, the sulfide solid electrolytes of Comparative Examples 1 to 5 have a lithium ion conductivity of 4.1 ⁇ 10 ⁇ 4 to 1.2 ⁇ 10 ⁇ 3 and an average particle diameter D50 of 1.6 ⁇ m or more. Met. As shown in FIGS.
- the sulfide solid electrolytes of Comparative Examples 1 to 5 have a particle size larger than that of the sulfide solid electrolytes of Examples 1 to 4 shown in FIGS. As shown in FIG. 11, in Comparative Example 3, coarse particles that were not pulverized remained. Further, even if Comparative Examples 1 to 5 and Examples 1 and 3 having the same pulverization time are compared with those of Examples 1 and 3 using the present invention, the sulfide solid electrolyte The average particle size of was small. As described above, according to the present invention, the productivity of a sulfide solid electrolyte having a small average particle diameter can be improved.
Abstract
Description
本発明は、硫化物固体電解質及びその原料のうち少なくとも一方と、溶媒とを混合して混合物を得る、混合工程と、直径が1mm未満である第1粉砕媒体、及び、直径が1mm以上である第2粉砕媒体を同時に用いて、硫化物固体電解質を機械的に粉砕する、粉砕工程と、を有する、硫化物固体電解質の製造方法である。
<硫化物固体電解質材料の混合>
硫化リチウム(日本化学工業株式会社製、純度99.9%)70.0g、及び、五硫化二リン(アルドリッチ社製、純度99%)をメノウ乳鉢でプレミキシング後に、乾式メカニカルミリングで毎分300回転の条件で20時間に亘って混合することにより、硫化物固体電解質材料の混合粉体を得た。
[実施例1]
1gの上記硫化物固体電解質材料の混合粉体、40gの粉砕媒体(直径1mmのZrO2ボールを10g、及び、直径0.3mmのZrO2ボールを30g)、8gの溶媒(脱水ヘプタン、関東化学株式会社製)、及び、1gの添加剤(ジブチルエーテル)を、45mlのZrO2ポットに投入した。そして、遊星型ボールミル機(フリッチュ製、P7)を用いて、メカニカルミリング法にて、毎分150回転の条件で10時間に亘る粉砕処理を行うことにより、実施例1の硫化物固体電解質を得た。
粉砕処理の時間を20時間にしたほかは、上記実施例1と同様の条件で、実施例2の硫化物固体電解質を得た。
粉砕処理の回転数を毎分200回転にしたほかは、上記実施例1と同様の条件で、実施例3の硫化物固体電解質を得た。
直径1mmのZrO2ボールを20g、及び、直径0.3mmのZrO2ボールを20g用いたほかは、上記実施例2と同様の条件で、実施例4の硫化物固体電解質を得た。
1gの上記硫化物固体電解質材料の混合粉体、40gの粉砕媒体(直径1mmのZrO2ボールを40g)、8.9gの溶媒(脱水ヘプタン、関東化学株式会社製)、及び、0.1gの添加剤(ジブチルエーテル)を、45mlのZrO2ポットに投入した。そして、遊星型ボールミル機(フリッチュ製、P7)を用いて、メカニカルミリング法にて、毎分150回転の条件で10時間に亘る粉砕処理を行うことにより、比較例1の硫化物固体電解質を得た。
粉砕処理の回転数を毎分100回転にしたほかは、上記比較例1と同様の条件で、比較例2の硫化物固体電解質を得た。
1gの上記硫化物固体電解質材料の混合粉体、40gの粉砕媒体(直径0.3mmのZrO2ボールを40g)、8gの溶媒(脱水ヘプタン、関東化学株式会社製)、及び、1gの添加剤(ジブチルエーテル)を、45mlのZrO2ポットに投入した。そして、遊星型ボールミル機(フリッチュ製、P7)を用いて、メカニカルミリング法にて、毎分200回転の条件で10時間に亘る粉砕処理を行うことにより、比較例3の硫化物固体電解質を得た。
粉砕処理の回転数を毎分300回転にしたほかは、上記比較例3と同様の条件で、比較例4の硫化物固体電解質を得た。
粉砕処理の回転数を毎分450回転にしたほかは、上記比較例3と同様の条件で、比較例5の硫化物固体電解質を得た。
得られた実施例1乃至実施例4及び比較例1乃至比較例5の硫化物固体電解質を、それぞれ0.1gずつ秤量し、421.4MPaの圧力でプレスすることにより、9つのペレットを作製した。そして、大気非暴露の環境下で、恒温層を用いて25℃に温度調整をした後、株式会社東陽テクニカ製のソーラートロン1260を用いて、交流インピーダンス法により、9つのペレットそれぞれのリチウムイオン伝導度を測定した。
得られた実施例1乃至実施例4及び比較例1乃至比較例5の硫化物固体電解質を、それぞれ少量ずつサンプリングし、レーザー回折・散乱式粒度分布計(日機装株式会社製、マイクロトラックMT3300EXII)を用いて粒度分布を測定した。
実施例1乃至実施例4並びに比較例1乃至比較例5の、硫化物固体電解質の製造条件、リチウムイオン伝導度測定結果、及び、粒度分布測定結果を表1に示す。ここで、D10は累積粒度分布の微粒側からの累積が10%である粒の直径、D50は累積粒度分布の微粒側からの累積が50%である粒の直径、D90は累積粒度分布の微粒側からの累積が90%である粒の直径をいう。また、実施例1乃至実施例4並びに比較例1乃至比較例5の硫化物固体電解質の、平均粒径とリチウムイオン伝導度との関係を、図3に示す。図3の縦軸はリチウムイオン伝導度σ[S/cm]、横軸は平均粒径D50[μm]である。また、実施例1乃至実施例4並びに比較例1乃至比較例5の硫化物固体電解質を、倍率5000倍(図4乃至図10、図12、及び、図13)又は倍率1000倍(図11)で観察した写真を、図4乃至図13にそれぞれ示す。
以上より、本発明によれば、平均粒径の小さい硫化物固体電解質の生産性を向上させることができた。
2…溶媒
3…第1粉砕媒体
4…第2粉砕媒体
Claims (2)
- 硫化物固体電解質及びその原料のうち少なくとも一方と、溶媒とを混合して混合物を得る、混合工程と、
直径が1mm未満である第1粉砕媒体、及び、直径が1mm以上である第2粉砕媒体を同時に用いて、硫化物固体電解質を機械的に粉砕する、粉砕工程と、
を有する、硫化物固体電解質の製造方法。 - 前記粉砕工程で、さらに、エーテル化合物が混合されて粉砕される、請求項1に記載の硫化物固体電解質の製造方法。
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CN201180074622.3A CN103918039A (zh) | 2011-11-17 | 2011-11-17 | 硫化物固体电解质的制造方法 |
US14/355,985 US20140295260A1 (en) | 2011-11-17 | 2011-11-17 | Method for producing sulfide solid electrolyte |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2014192309A1 (ja) * | 2013-05-31 | 2017-02-23 | 出光興産株式会社 | 固体電解質の製造方法 |
US10020535B2 (en) * | 2015-12-01 | 2018-07-10 | Idemitsu Kosan Co., Ltd. | Method for producing sulfide solid electrolyte |
KR20180115130A (ko) * | 2017-04-12 | 2018-10-22 | 한국전기연구원 | 황화물계 고체전해질 분말 제조방법, 고체전해질 분말을 포함하는 고체전해질층, 전극복합체층 제조방법 및 이를 포함하는 전고체전지 |
JP2020126760A (ja) * | 2019-02-04 | 2020-08-20 | 三井金属鉱業株式会社 | 固体電解質 |
JP6780140B1 (ja) * | 2020-01-17 | 2020-11-04 | 住友化学株式会社 | 全固体リチウムイオン電池用混合粉末、全固体リチウムイオン電池用混合ペースト、電極および全固体リチウムイオン電池 |
DE112014004188B4 (de) * | 2013-09-13 | 2020-12-24 | Toyota Jidosha Kabushiki Kaisha | Verfahren zum Herstellen von Sulfidfestelektrolyt |
JP2022077680A (ja) * | 2020-11-12 | 2022-05-24 | 株式会社テオス | シリコン破砕用低汚染衝撃工具 |
KR102560211B1 (ko) | 2022-04-26 | 2023-07-28 | 주식회사 포스코제이케이솔리드솔루션 | 전고체 이차전지용 황화물계 고체전해질 및 이의 제조방법 |
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Publication number | Priority date | Publication date | Assignee | Title |
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JP2016035913A (ja) | 2014-07-31 | 2016-03-17 | 富士フイルム株式会社 | 全固体二次電池、ならびに、無機固体電解質粒子、固体電解質組成物、電池用電極シートおよび全固体二次電池の製造方法 |
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63194748A (ja) * | 1987-02-05 | 1988-08-11 | 日本鋼管株式会社 | 高濃度石炭・水スラリ−の製造装置及びその製造方法 |
JPH09253517A (ja) * | 1996-03-25 | 1997-09-30 | Natl Res Inst For Metals | 粉末粒子の粉砕方法と粒子修飾方法 |
JP2009211950A (ja) * | 2008-03-04 | 2009-09-17 | Idemitsu Kosan Co Ltd | 固体電解質及びその製造方法 |
JP2010090003A (ja) * | 2008-10-09 | 2010-04-22 | Idemitsu Kosan Co Ltd | 硫化物系固体電解質の製造方法 |
Family Cites Families (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04267056A (ja) * | 1991-02-22 | 1992-09-22 | Matsushita Electric Ind Co Ltd | 固形電極組成物 |
US5513803A (en) * | 1994-05-25 | 1996-05-07 | Eastman Kodak Company | Continuous media recirculation milling process |
JP3233345B2 (ja) * | 1997-10-31 | 2001-11-26 | 大阪府 | 全固体型電池用イオン伝導性硫化物ガラス微粉末の製造方法、全固体型電池用イオン伝導性硫化物ガラス微粉末、固体型電解質及び全固体型二次電池 |
AU8847101A (en) * | 2000-08-31 | 2002-03-13 | Rtp Pharma Inc | Milled particles |
KR100436712B1 (ko) * | 2001-12-19 | 2004-06-22 | 삼성에스디아이 주식회사 | 캐소드 전극, 그 제조방법 및 이를 채용한 리튬 전지 |
CN1297026C (zh) * | 2002-10-11 | 2007-01-24 | 株式会社日本触媒 | 固体氧化物型燃料电池用电解质薄片及其制法 |
US7955735B2 (en) * | 2004-11-15 | 2011-06-07 | Panasonic Corporation | Non-aqueous electrolyte secondary battery |
JP3954085B2 (ja) * | 2005-10-07 | 2007-08-08 | シャープ株式会社 | 光電変換素子およびこれを用いた太陽電池 |
JP2009082910A (ja) * | 2007-09-14 | 2009-04-23 | Toyota Motor Corp | 微粒子コンポジット、その製造方法、固体高分子型燃料電池用触媒、及び固体高分子型燃料電池 |
JP2009104990A (ja) * | 2007-10-25 | 2009-05-14 | Nippon Shokubai Co Ltd | 固体酸化物形燃料電池用電解質シートの製造方法および電解質シート |
EP2231815A1 (en) * | 2007-12-14 | 2010-09-29 | Basf Se | Inorganic phosphor, obtainable by wet milling |
JP5680288B2 (ja) * | 2008-07-07 | 2015-03-04 | トヨタ自動車株式会社 | 硫化物系固体電解質の製造方法 |
JP4835736B2 (ja) * | 2009-08-31 | 2011-12-14 | トヨタ自動車株式会社 | 固体電解質シートの製造方法 |
JP5272995B2 (ja) * | 2009-09-29 | 2013-08-28 | トヨタ自動車株式会社 | 固体電解質層、電極活物質層、全固体リチウム電池、固体電解質層の製造方法、および電極活物質層の製造方法 |
CN102205946A (zh) * | 2011-05-03 | 2011-10-05 | 浙江大学 | 一种非碱金属类金属硼氢化物的液相合成方法 |
-
2011
- 2011-11-17 US US14/355,985 patent/US20140295260A1/en not_active Abandoned
- 2011-11-17 JP JP2013544060A patent/JP5800027B2/ja not_active Expired - Fee Related
- 2011-11-17 CN CN201180074622.3A patent/CN103918039A/zh active Pending
- 2011-11-17 WO PCT/JP2011/076530 patent/WO2013073035A1/ja active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63194748A (ja) * | 1987-02-05 | 1988-08-11 | 日本鋼管株式会社 | 高濃度石炭・水スラリ−の製造装置及びその製造方法 |
JPH09253517A (ja) * | 1996-03-25 | 1997-09-30 | Natl Res Inst For Metals | 粉末粒子の粉砕方法と粒子修飾方法 |
JP2009211950A (ja) * | 2008-03-04 | 2009-09-17 | Idemitsu Kosan Co Ltd | 固体電解質及びその製造方法 |
JP2010090003A (ja) * | 2008-10-09 | 2010-04-22 | Idemitsu Kosan Co Ltd | 硫化物系固体電解質の製造方法 |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10116002B2 (en) | 2013-05-31 | 2018-10-30 | Idemitsu Kosan Co., Ltd. | Production method of solid electrolyte |
JPWO2014192309A1 (ja) * | 2013-05-31 | 2017-02-23 | 出光興産株式会社 | 固体電解質の製造方法 |
DE112014004188B4 (de) * | 2013-09-13 | 2020-12-24 | Toyota Jidosha Kabushiki Kaisha | Verfahren zum Herstellen von Sulfidfestelektrolyt |
US10020535B2 (en) * | 2015-12-01 | 2018-07-10 | Idemitsu Kosan Co., Ltd. | Method for producing sulfide solid electrolyte |
KR20180115130A (ko) * | 2017-04-12 | 2018-10-22 | 한국전기연구원 | 황화물계 고체전해질 분말 제조방법, 고체전해질 분말을 포함하는 고체전해질층, 전극복합체층 제조방법 및 이를 포함하는 전고체전지 |
KR102398467B1 (ko) * | 2017-04-12 | 2022-05-13 | 한국전기연구원 | 황화물계 고체전해질 분말을 포함하는 복합체 제조방법, 이를 이용한 고체전해질층, 전극복합체층 제조방법 및 이를 포함하는 전고체전지 |
JP2020126760A (ja) * | 2019-02-04 | 2020-08-20 | 三井金属鉱業株式会社 | 固体電解質 |
JP7239337B2 (ja) | 2019-02-04 | 2023-03-14 | 三井金属鉱業株式会社 | 固体電解質 |
JP6780140B1 (ja) * | 2020-01-17 | 2020-11-04 | 住友化学株式会社 | 全固体リチウムイオン電池用混合粉末、全固体リチウムイオン電池用混合ペースト、電極および全固体リチウムイオン電池 |
JP2021114407A (ja) * | 2020-01-17 | 2021-08-05 | 住友化学株式会社 | 全固体リチウムイオン電池用混合粉末、全固体リチウムイオン電池用混合ペースト、電極および全固体リチウムイオン電池 |
JP2022077680A (ja) * | 2020-11-12 | 2022-05-24 | 株式会社テオス | シリコン破砕用低汚染衝撃工具 |
JP7316670B2 (ja) | 2020-11-12 | 2023-07-28 | 株式会社テオス | シリコン破砕用低汚染衝撃工具 |
KR102560211B1 (ko) | 2022-04-26 | 2023-07-28 | 주식회사 포스코제이케이솔리드솔루션 | 전고체 이차전지용 황화물계 고체전해질 및 이의 제조방법 |
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