CN113937345A - Composite solid electrolyte, preparation method thereof and all-solid-state battery - Google Patents

Composite solid electrolyte, preparation method thereof and all-solid-state battery Download PDF

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CN113937345A
CN113937345A CN202010670267.7A CN202010670267A CN113937345A CN 113937345 A CN113937345 A CN 113937345A CN 202010670267 A CN202010670267 A CN 202010670267A CN 113937345 A CN113937345 A CN 113937345A
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electrolyte
glassy
glassy electrolyte
sulfide
oxide
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CN113937345B (en
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胡屹伟
郭姿珠
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BYD Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0561Accumulators 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
    • H01M10/0562Solid materials
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0065Solid electrolytes
    • H01M2300/0068Solid electrolytes inorganic
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0065Solid electrolytes
    • H01M2300/0068Solid electrolytes inorganic
    • H01M2300/0071Oxides
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0088Composites
    • H01M2300/0091Composites in the form of mixtures
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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Abstract

The present disclosure relates to a composite solid electrolyte including an oxide glassy electrolyte matrix and sulfide glassy electrolyte microbeads dispersed in the oxide glassy electrolyte matrix. The composite solid electrolyte glass can simultaneously give consideration to high strength, high stability and high ionic conductivity.

Description

Composite solid electrolyte, preparation method thereof and all-solid-state battery
Technical Field
The application relates to the field of lithium ion batteries, in particular to a composite solid electrolyte, a preparation method thereof and an all-solid-state battery.
Background
With the rapid development of electric vehicles, lithium metal batteries with high energy density are receiving more and more attention. However, in the conventional liquid electrolyte, the unstable deposition process of lithium metal and the dendrite growth cause a series of safety problems, which also seriously hinder the development of the lithium metal negative electrode. Solid-state electrolytes can match lithium metal negative electrodes and high-voltage positive electrodes to make higher energy density all-solid-state lithium battery cells (ASSLBs) than liquid electrolytes.
Most of the existing solid electrolyte glasses are oxide solid electrolytes and sulfide solid electrolytes, but each solid electrolyte glass has the advantages and the inherent defects, for example, the oxide solid electrolyte has higher mechanical strength and is stable in air, but the ionic conductivity is very low; the sulfide solid electrolyte has high ionic conductivity, but is unstable in air, low in strength and easy to crack.
The search for a solid electrolyte that combines high strength, high processability, high ionic conductivity and high stability in air is therefore a key issue in the development of solid-state batteries.
Disclosure of Invention
The purpose of the present disclosure is to provide a solid electrolyte having high stability and high ionic conductivity.
In order to achieve the above object, a first aspect of the present disclosure provides a composite solid electrolyte including an oxide glassy electrolyte matrix and sulfide glassy electrolyte microbeads dispersed in the oxide glassy electrolyte matrix. The composite solid electrolyte main body is an oxide glassy electrolyte, so that the main body electrolyte is stable in air and has higher strength, sulfide glassy electrolyte microbeads are embedded in the oxide glassy electrolyte main body after the composite modification of the sulfide glassy electrolyte, and the sulfide glassy electrolyte has higher ionic conductivity and plays a role of improving the ionic conductivity in the oxide glassy electrolyte main body, so that the composite solid electrolyte glass forms a structure similar to microcrystalline glass, and the microcrystalline but the sulfide glass microbeads improve the ionic conductivity. Finally, the composite solid electrolyte glass has high strength, high stability and high ionic conductivity.
Optionally, the diameter of the sulfide glassy electrolyte microbeads is between 1nm and 5 μm; preferably 50-500 nm.
Optionally, the sulfide glassy electrolyte microbeads are present in an amount of 0.01 to 20 parts by weight relative to 100 parts by weight of the composite solid electrolyte; preferably 1 to 5 parts by weight.
Optionally, the oxide glassy electrolyte matrix is selected from at least one of a phosphate glassy electrolyte, a silicate glassy electrolyte, a borate glassy electrolyte, and an anti-perovskite glassy electrolyte; the sulfide glassy electrolyte microbeads are selected from a thiosilicate glassy electrolyte and/or a thiophosphate glassy electrolyte;
preferably, the oxide glassy electrolyte matrix is selected from phosphate glassy electrolytes; the sulfide glassy electrolyte microbeads are selected from a thiosilicate glassy electrolyte.
Optionally, the oxide glassy electrolyte matrix contains a halogen, the halogen being at least one of fluorine, chlorine, bromine, and iodine.
A second aspect of the present disclosure provides a method for preparing a composite solid electrolyte, including the steps of:
s1, mixing and grinding the oxide glassy electrolyte and the sulfide glassy electrolyte to obtain a first mixed material;
s2, carrying out melting treatment and quenching treatment on the first mixed material; the melting treatment comprises early-stage high-temperature treatment and later-stage cooling treatment.
Alternatively, the oxide glassy electrolyte matrix may be selected from at least one of a phosphate glassy electrolyte, a silicate glassy electrolyte, a borate glassy electrolyte, and an anti-perovskite glassy electrolyte; the sulfide glassy electrolyte may be selected from a thiosilicate glassy electrolyte and/or a thiophosphate glassy electrolyte; preferably, the oxide glassy electrolyte matrix may be selected from phosphate glassy electrolytes; the sulfide glassy electrolyte may be selected from the group consisting of thiosilicate glassy electrolytes.
Optionally, the mass ratio of the oxide glassy electrolyte to the sulfide glassy electrolyte is 1: 0.01 to 0.25, preferably 1: 0.01-0.05.
Optionally, in step S2, the conditions of the high-temperature pretreatment include: under inert gas, the temperature is 600 ℃ and 1600 ℃, the time is 5-60min, and the heating rate is 0.3-10 ℃/min; the cooling treatment conditions comprise: under inert gas, the temperature is 500-1300 ℃, the time is 5-60min, and the cooling rate is 0.3-5 ℃/min; the inert gas is one of argon, nitrogen and helium; the quenching treatment mode is one of single medium quenching, double medium quenching, staged quenching, surface quenching and isothermal quenching.
A third aspect of the present disclosure provides an all-solid-state battery including a positive electrode, a negative electrode, and a solid electrolyte that is the composite solid electrolyte described above. Compared with the traditional liquid electrolyte battery, the solid-state battery has higher safety due to the existence of the composite solid electrolyte, can be matched with a high-voltage positive electrode and a lithium negative electrode, improves the energy density, and can be compatible with the existing production process due to the fact that the solid electrolyte glass has high flexibility as a diaphragm.
Through the technical scheme, the composite solid electrolyte glass has the advantages that the composite solid electrolyte glass is high in strength, stability and ionic conductivity.
Additional features and advantages of the disclosure will be set forth in the detailed description which follows.
Detailed Description
The following describes in detail specific embodiments of the present disclosure. It should be understood that the detailed description and specific examples, while indicating the present disclosure, are given by way of illustration and explanation only, not limitation.
A first aspect of the present disclosure provides a composite solid electrolyte including an oxide glassy electrolyte matrix and sulfide glassy electrolyte microbeads dispersed in the oxide glassy electrolyte matrix.
According to the composite solid electrolyte disclosed by the invention, the oxide glassy electrolyte and the sulfide glassy electrolyte which cannot be mutually dissolved originally are physically taken as a matrix, and sulfide glassy electrolyte microbeads are embedded in the matrix. The structure enables the sulfide glass state electrolyte to be uniformly dispersed in the oxide glass electrolyte matrix, and the oxide glass state electrolyte has high strength and high stability, and the sulfide glass state electrolyte has higher ionic conductivity, so that the composite solid electrolyte glass has high strength, high stability and high ionic conductivity at the same time.
According to the first aspect of the present disclosure, the diameter of the sulfide glassy electrolyte microbeads may be 1nm to 5 μm; preferably 50-500 nm. The sulfide glassy state electrolyte micro-beads in the present disclosure can play a role in improving the ionic conductivity of oxide glass, while not reducing the structural strength of the oxide glassy state electrolyte matrix.
According to the first aspect of the present disclosure, the sulfide glassy electrolyte microbeads may be contained in an amount of 0.01 to 20 parts by weight, relative to 100 parts by weight of the composite solid electrolyte; preferably 1 to 5 parts by weight. In the present disclosure, a suitable sulfide glassy electrolyte bead content does not affect the physical properties of the oxide glassy electrolyte matrix while significantly increasing the ionic conductivity.
According to a first aspect of the present disclosure, the oxide glassy electrolyte matrix may be selected from at least one of a phosphate glassy electrolyte, a silicate glassy electrolyte, and an anti-perovskite glassy electrolyte; the sulfide glassy electrolyte microbeads may be selected from a thiosilicate glassy electrolyte and/or a thiophosphate glassy electrolyte.
Wherein the phosphate glass may comprise Li having a chemical formulaaXbYcZdPOeWherein a is between 0.5 and 6, X is one or more of Al, Y, Ca, Cr, In, Fe, Se and La, b is between 0 and 0.3, Y is one or more of Ti, Ge, Ta, Zr, Sn, Fe, V and the element Hf, c is between 0 and 0.9, Z is one or more of F, Cl, Br and I, and d is between 0 and 1.5. The silicate glass may comprise Li having the formulaaXbYcZdSiOeWherein a is between 0.3 and 6, X is one or more of Na, K, Ca, Ba and Al, b is between 0 and 0.5, Y is one or more of Ti, Zr, La, Y, Sb, Sc, V, Cr, Mn, Fe, Co, Ni, Cu and Zn, c is between 0 and 0.8, Z is one or more of F, Cl, Br and I, and d is between 0 and 1.5. The borate glass may comprise Li having the formulaaXbYcZdBOeWherein a is between 0.5 and 6, X is one or more of Na, K, Ca, Ba and Al, b is between 0 and 0.5, and Y is Ti, Zr, La, Y, Sb, Sc, V, Cr, Mn, Fe, Co, Al,One or more of Ni, Cu and Zn, c is between 0 and 0.8, Z is one or more of F, Cl, Br and I, and d is between 0 and 1.5. The anti-perovskite glass may comprise Li having the formula3-xM0.5xOZ, wherein x is between 0 and 1.5, M is one or more of Be, Mg, Ca, Sr and Ba, and Z is one or more of F, Cl, Br and I. The thiosilicate has the formula a (Li)2S)-b(SiS2) -c (LiX), wherein X is one or more of F, Cl, Br and I, a is between 20 and 70, b is between 30 and 80, c is between 0.1 and 30. The thiophosphate has the chemical formula alpha (Li)2S)-β(P2S5) - γ (LiX), wherein X is one or more of F, Cl, Br and I, a is between 40 and 75, β is between 25 and 60, c is between 0.1 and 50.
In a preferred embodiment of the present disclosure, the oxide glassy electrolyte matrix is selected from the group consisting of phosphate glassy electrolytes; the sulfide glassy electrolyte microbeads are selected from a thiosilicate glassy electrolyte.
In a preferred embodiment of the present disclosure, the oxide glassy electrolyte matrix contains a halogen, and the halogen is at least one of fluorine, chlorine, bromine, and iodine. The oxide glassy electrolytes containing halogen of the present disclosure can further improve the oxide glass ionic conductivity.
A second aspect of the present disclosure provides a method for preparing a composite solid electrolyte, including the steps of:
s1, mixing and grinding the oxide glassy electrolyte precursor and the sulfide glassy electrolyte to obtain a first mixed material;
s2, carrying out melting treatment and quenching treatment on the first mixed material; the melting treatment comprises early-stage high-temperature treatment and later-stage cooling treatment.
According to the second aspect of the present disclosure, the mass ratio of the oxide glassy electrolyte precursor to the sulfide glassy electrolyte precursor may be 1: 0.01 to 0.25, preferably 1: 0.01-0.05.
According to the second aspect of the present disclosure, the oxide glassy electrolyte may be selected from at least one of a phosphate glassy electrolyte, a silicate glassy electrolyte, a borate glassy electrolyte, and an anti-perovskite glassy electrolyte; the sulfide glassy electrolyte may be selected from a thiosilicate glassy electrolyte and/or a thiophosphate glassy electrolyte; preferably, the oxide glassy electrolyte matrix may be selected from phosphate glassy electrolytes; the sulfide glassy electrolyte may be selected from the group consisting of thiosilicate glassy electrolytes.
According to the second aspect of the present disclosure, in step S2, the conditions of the front-end high-temperature treatment may include: under inert gas, the temperature is 600 ℃ and 1600 ℃, the time is 5-60min, and the heating rate is 0.3-10 ℃/min; the cooling treatment conditions may include: under inert gas, the temperature is 500-1300 ℃, the time is 5-60min, and the cooling rate is 0.3-5 ℃/min; the inert gas is one of argon, nitrogen and helium; the conditions of the third quenching treatment may include: single medium quenching, double medium quenching, graded quenching, surface quenching and isothermal quenching; .
A third aspect of the present disclosure provides an all-solid-state battery including a positive electrode, a negative electrode, and a solid electrolyte that is the composite solid electrolyte described above.
The all-solid-state battery has higher safety compared with the traditional liquid electrolyte battery due to the existence of the composite solid electrolyte, and can be matched with a high-voltage anode and a lithium cathode to improve the energy density.
The present disclosure is further illustrated by the following examples, but is not to be construed as being limited thereby.
The materials, reagents, instruments and equipment used in the examples of the present disclosure are commercially available, unless otherwise specified. The example operations of the present disclosure were performed under an argon atmosphere.
Example 1
16mmol of LiCl and 24mmol of P2O5And 16mmol Li2CO3Adding into mortar, grinding and mixing. And placing the mixed powder into a boron nitride crucible, placing the boron nitride crucible into a muffle furnace heated to 800 ℃, taking out the boron nitride crucible after 10 minutes, pouring the boron nitride crucible into a stainless steel mold, and quenching to obtain the oxide glassy electrolyte.
40mmol of SiS2And 60mmol of Li2And S, adding the materials into a mortar for grinding, mixing fully, placing the materials into a boron nitride crucible, heating the materials to 950 ℃ along with a furnace, keeping the temperature at the rate of 5 ℃/min for 30 minutes, taking the materials out after full melting, pouring the materials into a stainless steel mold, and quenching to obtain the sulfide glassy electrolyte.
Grinding 95 mass percent of oxide glassy electrolyte and 5 mass percent of sulfide glassy electrolyte, grinding, uniformly mixing, placing into a boron nitride crucible, heating to 1300 ℃ along with the furnace, heating at a rate of 5 ℃/min, keeping for 10 minutes, cooling to 1100 ℃, taking out, pouring into a stainless steel mold, and quenching to obtain the composite solid electrolyte of the embodiment.
Example 2
24mmol of P2O5And 16mmol Li2CO3Adding into mortar, grinding and mixing. And placing the mixed powder into a boron nitride crucible, placing the boron nitride crucible into a muffle furnace heated to 800 ℃, taking out the boron nitride crucible after 10 minutes, pouring the boron nitride crucible into a stainless steel mold, and quenching to obtain the oxide glassy electrolyte.
40mmol of SiS2And 60mmol of Li2And S, adding the materials into a mortar for grinding, mixing fully, placing the materials into a boron nitride crucible, heating the materials to 950 ℃ along with a furnace, keeping the temperature at the rate of 5 ℃/min for 30 minutes, taking the materials out after full melting, pouring the materials into a stainless steel mold, and quenching to obtain the sulfide glassy electrolyte.
Grinding 95 mass percent of oxide glassy electrolyte and 5 mass percent of sulfide glassy electrolyte, grinding, uniformly mixing, placing into a boron nitride crucible, heating to 1300 ℃ along with the furnace, heating at a rate of 5 ℃/min, keeping for 10 minutes, cooling to 1100 ℃, taking out, pouring into a stainless steel mold, and quenching to obtain the composite solid electrolyte of the embodiment.
Example 3
The oxide glassy electrolyte and the sulfide glassy electrolyte of this example were prepared in the same manner as in example 1.
Grinding 80 mass percent of oxide glassy electrolyte and 20 mass percent of sulfide glassy electrolyte, grinding, uniformly mixing, placing into a boron nitride crucible, heating to 1300 ℃ along with the furnace, heating at a rate of 5 ℃/min, keeping for 10 minutes, cooling to 1100 ℃, taking out, pouring into a stainless steel mold, and quenching to obtain the composite solid electrolyte of the embodiment.
Example 4
The oxide glassy electrolyte and the sulfide glassy electrolyte of this example were prepared in the same manner as in example 1.
Grinding and then uniformly mixing the oxide glassy electrolyte with the mass ratio of 99% and the sulfide glassy electrolyte with the mass ratio of 1%, putting the mixture into a boron nitride crucible, heating the mixture to 1300 ℃ along with a furnace, heating the mixture at a rate of 5 ℃/min, keeping the temperature for 10 minutes, then cooling the mixture to 1100 ℃, taking the mixture out, pouring the mixture into a stainless steel mold, and quenching the mixture to obtain the composite solid electrolyte of the embodiment.
Comparative example 1
The preparation method of the composite solid electrolyte in this embodiment is the same as that in embodiment 1, except that in this embodiment, 95% by mass of the oxide glassy state electrolyte precursor and 5% by mass of the sulfide glassy state electrolyte precursor are ground, then ground, uniformly mixed, placed in a boron nitride crucible, heated to 1100 ℃ along with a furnace, heated at a rate of 5 ℃/min, kept for 10 minutes, taken out, poured into a stainless steel mold, and quenched, so as to obtain the composite solid electrolyte in this embodiment.
Comparative example 2
16mmol of LiCl and 24mmol of P2O5And 16mmol Li2CO3Adding into mortar, grinding and mixing. And placing the mixed powder into a boron nitride crucible, placing the boron nitride crucible into a muffle furnace heated to 800 ℃, taking out the boron nitride crucible after 10 minutes, pouring the boron nitride crucible into a stainless steel mold, and quenching to obtain the solid electrolyte of the comparative example.
Comparative example 3
40mmol of SiS2And 60mmol of Li2S additionGrinding in a pot, mixing fully, placing in a boron nitride crucible, heating to 950 ℃ along with the furnace, keeping the temperature at the rate of 5 ℃/min for 30 minutes, taking out after full melting, pouring into a stainless steel mold, and quenching to obtain the solid electrolyte of the comparative example.
Test example 1
The diameters of the sulfide glassy electrolyte microbeads in the solid electrolytes prepared in examples 1 to 4 and comparative examples 1 to 3 were measured by the following specific measurement methods: the measurement can be directly carried out under a scanning electron microscope, and the measurement result is shown in table 1.
TABLE 1
Group of Diameter of sulfide glassy state electrolyte microbeads Content of sulfide glass state electrolyte micro beads
Example 1 50~100nm 5%
Example 2 30~80nm 5%
Example 3 300-500nm 20%
Example 4 5-20nm 1%
Comparative example 1 - -
Comparative example 2 - -
Comparative example 3 - -
Test example 2
The solid electrolytes obtained in examples 1 to 4 and comparative examples 1 to 2 were subjected to an ion conductivity test by the following method: coating conductive silver adhesive on two sides of a glass sheet in a glove box, and drying in an oven at 150 ℃ for 1h to remove the solvent. Connecting electrodes at two ends of the glass sheet coated with the conductive silver paste, and carrying out electrochemical impedance test at a frequency of 7MHz-10 mHz.
0.5g of the samples obtained in examples 1 to 4 and comparative examples 1 to 2 was placed in a closed chamber having a capacity of 10L, and tested for H using a sensor2(ii) the concentration of S, to obtain the difference in its stability in air; the thermoformed samples (thickness 200 μm) were tested for bending resistance and the angle at which they broke was recorded to obtain strength data. The specific results are shown in Table 2.
Group of Ionic conductivity H2S content Bending angleDegree of rotation
Example 1 10-5S/cm-10-4S/cm 0.5ppm 85°
Example 2 10-6S/cm-10-5S/cm 0.5ppm 95°
Example 3 10-4S/cm 7ppm 70°
Example 4 10-6S/cm 0.1ppm 110°
Comparative example 1 10-6S/cm-10-5S/cm 533ppm 30°
Comparative example 2 10-8S/cm-10-7S/cm 0ppm 160°
Comparative example 3 10-4S/cm-10-3S/cm 1383ppm 60°
As can be seen from the data in table 2: examples 1 to 4 were excellent in ionic conductivity and generally increased in stability and strength, and comparative example 1 was not subjected to high-temperature heat treatment, did not form a uniformly dispersed glass bead composite structure, and could not have high stability and high strength. As can be seen from comparative examples 2 and 3, the pure oxide solid state electrolyte glass does not have high ionic conductivity, and the pure sulfide solid state electrolyte glass does not have high stability and high strength. It follows that the composite solid electrolyte of the present disclosure can simultaneously achieve high strength, high stability, and high ionic conductivity.
The preferred embodiments of the present disclosure have been described in detail above, however, the present disclosure is not limited to the specific details of the above embodiments, and various simple modifications may be made to the technical solution of the present disclosure within the technical idea of the present disclosure, and these simple modifications all fall within the protection scope of the present disclosure.
It should be noted that, in the foregoing embodiments, various features described in the above embodiments may be combined in any suitable manner, and in order to avoid unnecessary repetition, various combinations that are possible in the present disclosure are not described again.
In addition, any combination of various embodiments of the present disclosure may be made, and the same should be considered as the disclosure of the present disclosure, as long as it does not depart from the spirit of the present disclosure.

Claims (10)

1. A composite solid electrolyte comprising an oxide glassy electrolyte matrix and sulfide glassy electrolyte microbeads dispersed in the oxide glassy electrolyte matrix.
2. A composite solid-state electrolyte according to claim 1, wherein the diameter of the sulfide glassy electrolyte microbeads is between 1nm and 5 μ ι η; preferably 50-500 nm.
3. A composite solid electrolyte according to claim 1, wherein the sulfide glassy electrolyte microbeads are contained in an amount of 0.01 to 20 parts by weight relative to 100 parts by weight of the composite solid electrolyte; preferably 1 to 5 parts by weight.
4. A composite solid electrolyte according to claim 1, wherein the oxide glassy electrolyte matrix is selected from at least one of a phosphate glassy electrolyte, a silicate glassy electrolyte, a borate glassy electrolyte, and an anti-perovskite glassy electrolyte; the sulfide glassy electrolyte microbeads are selected from a thiosilicate glassy electrolyte and/or a thiophosphate glassy electrolyte;
preferably, the oxide glassy electrolyte matrix is selected from phosphate glassy electrolytes; the sulfide glassy electrolyte microbeads are selected from a thiosilicate glassy electrolyte.
5. The method of claim 4, wherein the oxide glassy electrolyte matrix comprises a halogen, the halogen being at least one of fluorine, chlorine, bromine, and iodine.
6. A method for producing a composite solid electrolyte according to any one of claims 1 to 5, characterized by comprising the steps of:
s1, mixing and grinding the oxide glassy electrolyte and the sulfide glassy electrolyte to obtain a first mixed material;
s2, carrying out melting treatment and quenching treatment on the first mixed material; the melting treatment comprises early-stage high-temperature treatment and later-stage cooling treatment.
7. The method of claim 6, wherein the mass ratio of the oxide glassy electrolyte to the sulfide glassy electrolyte is 1: 0.01 to 0.25, preferably 1: 0.01-0.05.
8. The method of claim 6, wherein the oxide glassy electrolyte is selected from at least one of a phosphate glassy electrolyte, a silicate glassy electrolyte, a borate glassy electrolyte, and an anti-perovskite glassy electrolyte; the sulfide glassy electrolyte is selected from a thiosilicate glassy electrolyte and/or a thiophosphate glassy electrolyte;
preferably, the oxide glassy electrolyte matrix is selected from phosphate glassy electrolytes; the sulfide glassy electrolyte is selected from the group consisting of thiosilicate glassy electrolytes.
9. The method of claim 6, wherein in step S2, the conditions of the pre-high temperature treatment include: under inert gas, the temperature is 600 ℃ and 1600 ℃, the time is 5-60min, and the heating rate is 0.3-10 ℃/min; the cooling treatment conditions comprise: under inert gas, the temperature is 500-1300 ℃, the time is 5-60min, and the cooling rate is 0.3-5 ℃/min; the inert gas is one of argon, nitrogen and helium;
the quenching treatment mode is one of single medium quenching, double medium quenching, staged quenching, surface quenching and isothermal quenching.
10. An all-solid-state battery comprising a positive electrode, a negative electrode and a solid-state electrolyte, characterized in that the solid-state electrolyte is a composite solid-state electrolyte according to any one of claims 1 to 5.
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