CN111082128B - High-power all-solid-state battery and preparation thereof - Google Patents

High-power all-solid-state battery and preparation thereof Download PDF

Info

Publication number
CN111082128B
CN111082128B CN201911342394.8A CN201911342394A CN111082128B CN 111082128 B CN111082128 B CN 111082128B CN 201911342394 A CN201911342394 A CN 201911342394A CN 111082128 B CN111082128 B CN 111082128B
Authority
CN
China
Prior art keywords
solid
ion conductor
fast ion
battery
sulfide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201911342394.8A
Other languages
Chinese (zh)
Other versions
CN111082128A (en
Inventor
崔光磊
王延涛
鞠江伟
徐红霞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
Original Assignee
Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Qingdao Institute of Bioenergy and Bioprocess Technology of CAS filed Critical Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
Priority to CN201911342394.8A priority Critical patent/CN111082128B/en
Publication of CN111082128A publication Critical patent/CN111082128A/en
Application granted granted Critical
Publication of CN111082128B publication Critical patent/CN111082128B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • 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
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0565Polymeric materials, e.g. gel-type or solid-type
    • 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
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/44Methods for charging or discharging
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/581Chalcogenides or intercalation compounds thereof
    • H01M4/5815Sulfides
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028Positive electrodes
    • 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
    • H01M2300/0082Organic polymers
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Materials Engineering (AREA)
  • Dispersion Chemistry (AREA)
  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The invention belongs to the technical field of batteries, and relates to a high-power all-solid-state battery and a preparation method thereof. The high-power all-solid-state battery comprises a positive electrode, a solid electrolyte and a negative electrode, wherein the positive electrode is obtained by mixing and grinding a sulfide fast ion conductor and a conductive agent, and the solid electrolyte is an ion transmission medium; wherein the sulfide fast ion conductor is xLi 2 S:(1‑x)P 2 S 5 (x=0.6‑0.8),Li 3 PS 4 ,Li 10 M x P 3‑x S 12 (0≤x≤2,M=Si,Ge,Sn),Li 6 PS 5 X (x=cl, br, I) or a combination of several. The solid-state battery modifies ion and electron transmission channels of the battery active material on an atomic scale, and improves the high-rate performance of the battery. Provides a reference for developing a high-safety, high-capacity and rapid charge and discharge battery.

Description

High-power all-solid-state battery and preparation thereof
Technical Field
The invention belongs to the technical field of batteries, and relates to a high-power all-solid-state battery and a preparation method thereof.
Background
All-solid-state lithium batteries employing solid electrolytes are receiving wide attention in academia and industry due to their high safety and high energy density, as compared to commercial lithium ion batteries employing liquid electrolytes. However, compared with liquid batteries, the current all-solid-state battery cannot basically work normally at a higher multiplying power, and basically analysis is mainly because the contact between the active substance and the solid electrolyte or the conductive agent in the electrode can only depend on a simple solid-solid contact mode, and the simple mixing of the active substance in the electrode with the solid electrolyte and the conductive agent cannot ensure that the active substance can contact both the electrolyte (ensuring ion transmission) and the conductive agent (ensuring electron transmission), and the mode cannot ensure that an ion or electron transmission channel is continuous and smooth. At present, related improvement and improvement measures are not reported, so that an all-solid-state battery anode is urgently needed to be designed, and the active material is ensured to be contacted with a solid electrolyte and a conductive agent to realize rapid ion and electron transmission.
Disclosure of Invention
The invention aims at a high-power all-solid-state battery and a preparation method thereof.
In order to achieve the above purpose, the invention adopts the following technical scheme:
the high-power all-solid-state battery comprises a positive electrode, a solid electrolyte and a negative electrode, wherein the positive electrode is obtained by mixing and grinding a sulfide fast ion conductor and a conductive agent, and the solid electrolyte is an ion transmission medium; wherein the sulfide fast ion conductor is xLi 2 S:(1-x)P 2 S 5 (x=0.6- 0.8), Li 3 PS 4 , Li 10 M x P 3-x S 12 (0 ≤ x ≤ 2, M= Si, Ge, Sn), Li 6 PS 5 X (x=cl, br, I) or a combination of several.
Discharging the all-solid-state battery under low pressure to a position below an electrochemical stability window of a sulfide fast ion conductor, wherein the all-solid-state battery is presented; or charged at low voltage above the sulfide fast ion conductor electrochemical stability window, an all-solid state battery is presented.
The mass ratio of the sulfide fast ion conductor to the conductive agent is 2:8-8:2, preferably 7:3-4:6.
the solid electrolyte sulfide fast ion conductor, oxide fast ion conductor or polymer solid electrolyte, wherein the sulfide fast ion conductor is xLi 2 S:(1-x)P 2 S 5 (x=0.6 ~ 0.8),Li 3 PS 4 ,Li 10 M x P 3-x S 12 (0 ≤ x ≤ 2, M= Si, Ge, Sn),Li 6 PS 5 X (x=cl, br, I) or a combination of several; the oxide fast ion conductor is Li 1-x Al x Ti 2-x (PO 4 ) 3 (0.1<x<0.6)、Li 3x La (2/3)-x TiO 3 (0.04<x<0.15)、Li 5 La 3 M 2 O 12 (M=Ta,Nb)、Li 5+x A x La 3-X M 2 O 12 (x=0,1,A=Ca,Sr,Ba,M=Nb,Ta,Bi)、ϒ-Al 2 O 3 One or more of the following; the polymer solid electrolyte is composed of a polymer and a lithium salt.
The polymer is one or more of polyoxyethylene, polyoxypropylene, polyacrylonitrile, polyvinyl chloride, polystyrene, polyvinyl carbonate, polyvinylpyrrolidone, polymethyl methacrylate, polyvinylidene fluoride, polyethylene glycol acrylate, polydivinylsulfide and derivatives thereof; the lithium salt is lithium perchlorate (LiClO) 4 ) Lithium bis (oxalato) borate (LiBOB), lithium difluoro (LiDFOB) oxalato borate, lithium trifluoro (CF) 3 SO 3 Li), lithium bis (trifluoromethylsulfonyl) imide (LiTFSI), lithium bis (fluorosulfonyl) imide (LiFSI).
A preparation method of a high-power all-solid-state battery comprises the steps of preparing a positive electrode, a solid electrolyte and a negative electrode; or sequentially stacking the anode, the solid electrolyte and the cathode to form the integrated all-solid-state lithium battery with the sandwich structure.
The negative electrode active material is one of a metal lithium sheet, a metal lithium alloy, graphite, hard carbon, molybdenum disulfide, lithium titanate, graphene and a silicon carbon negative electrode;
the all-solid-state battery discharges the battery below the sulfide fast ion conductor electrochemical stability window or charges the battery above the sulfide fast ion conductor electrochemical stability window, and then charges or discharges the battery for use.
The all-solid-state battery is firstly discharged below an electrochemical stability window of a sulfide fast ion conductor under a low voltage of 0-1.5V or charged (3-5V) above the electrochemical stability window of the sulfide fast ion conductor, so that the sulfide fast ion conductor at the contact part with the conductive agent is decomposed to generate battery active substances with capacity, the active substances are generated in situ through electrochemical reaction, and the active substances are contacted with the sulfide fast ion conductor and the conductive agent in an atomic level, so that the active substances have excellent ion and electron transmission in the subsequent oxidation-reduction process, the solid-solid interface impedance is reduced, and the high multiplying power and the high cycle stability of the all-solid-state battery are improved.
A method for improving the efficiency of solid-state battery features that the electrolyte is discharged under the low voltage of 0-1.5V or charged (3-5V) to the position above the electrochemical stability window of sulfide fast ion conductor, so realizing high multiplying power and high cyclic stability.
The working principle of the battery is that the battery is firstly discharged below the electrochemical stability window of the sulfide fast ion conductor or charged above the electrochemical stability window of the sulfide fast ion conductor, and only the sulfide fast ion conductor contacted with the conductive agent in the positive electrode can be decomposed and generate Li in the process 2 S,P 2 S 5 , Li 2 S n Etc. by-products, wherein Li 2 S,Li 2 S n Is an electrochemically active material, and the generated byproducts can prevent the electrolyte from decomposing during the subsequent charge and discharge process due to the inertia of electrons and ions (the electrolyte in the positive electrode does not undergo oxidation-reduction reaction if not contacted with electrons). Li generated after discharge 2 S generates Li during charging 2 S n Or Li generated after charging 2 S n Li is generated during discharge 2 S, S. After this, the electrochemical reaction during the battery charge and discharge is as follows: .
The invention has the advantages that:
the solid-state battery modifies ion and electron transmission channels of the battery active material on an atomic scale, and improves the high-rate performance of the battery. Provides a reference for developing a high-safety, high-capacity and rapid charge and discharge battery.
The method is suitable for all-solid-state batteries which take sulfide fast ion conductors and conductive agents as electrode components, utilizes the generated sulfide byproducts as active materials of the batteries so as to improve the rate performance, and the generated byproducts are tightly contacted with sulfide electrolyte on the atomic scale to realize fast ion and electron transmission.
The high-power all-solid-state battery of the present invention utilizing the above method spontaneously decomposes into Li at low voltage using sulfide electrolyte 2 By utilizing the characteristics of by-products such as S and the like and utilizing the generated Li 2 S serves as the positive electrode active material of the battery. Due to the generated Li 2 S is generated spontaneously in situ, so that the active material is in close contact with sulfide electrolyte and conductive agent on the atomic scale, thereby greatly reducing solid-solid interface impedance and facilitating rapid transmission of ions and electrons. The all-solid-state battery assembled in this way can be manufactured at 25mA cm -2 Realizes stable circulation under the current density of (1.54 mAh cm) and can reach the battery capacity -2 . And the ratio of sulfide electrolyte to conductive agent in the positive electrode material is further regulated to obtain the full-solid lithium battery with different capacities and high multiplying power and high cycle stability.
Drawings
Fig. 1a is a schematic diagram of a discharging process of a high-power all-solid-state battery according to an embodiment of the present invention in the first cycle; fig. 1b is a schematic diagram of a change of a discharge ending substance of a first cycle of a high-power all-solid-state battery according to an embodiment of the present invention.
Fig. 2 is a graph showing the relationship between capacity and voltage at different cycles of the high-power all-solid-state battery according to example 1 of the present invention.
Fig. 3 is a graph showing the relationship between capacity and voltage in the steady state of the high-power all-solid-state battery according to embodiment 2 of the present invention.
Detailed Description
The present invention will be described in further detail with reference to the following examples. The specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
The invention relates to a high-power all-solid-state battery, which comprises an anode, an electrolyte and a cathode, wherein the anode is a mixture of a sulfide fast ion conductor and a conductive agent according to a certain proportion, and the electrolyte is a solid fast ion conductor or a polymer electrolyte. The cell is first discharged below the sulfide fast ion conductor electrochemical stability window or charged above the sulfide fast ion conductor electrochemical stability window, positiveOnly sulfide fast ion conductors in contact with the conductive agent in the electrode are decomposed in the process and Li is generated 2 S,P 2 S 5 ,Li 2 S n Etc. by-products, wherein Li 2 S,Li 2 S n Is an electrochemically active material, and the generated byproducts can prevent the electrolyte from decomposing during the subsequent charge and discharge process due to the inertia of electrons and ions (the electrolyte in the positive electrode does not undergo oxidation-reduction reaction if not contacted with electrons). Li generated after discharge 2 S generates Li during charging 2 S n Or Li generated after charging 2 S n Li is generated during discharge 2 S, S. After this, the electrochemical reaction during the battery charge and discharge is as follows: . The generated sulfide byproducts are used as the active materials of the battery to further improve the rate performance, and the generated byproducts are tightly contacted with sulfide electrolyte on the atomic scale to realize rapid ion and electron transmission.
Example 1
Li is mixed with 3 PS 4 Mixing the material with conductive carbon black according to the mass ratio of 7:3, and fully grinding and mixing the mixture to obtain the composite anode. For all-solid-state batteries using sulfide fast ion conductors as electrolytes, cold pressing methods can be used to prepare all-solid-state batteries, specifically: first, 0.1 g of Li is taken 3 PS 4 The resulting mixture was placed in a swagelok-type battery under a pressure of 100 Mpa for 1 min, and then 10 mg of the above-mentioned composite positive electrode powder was uniformly spread on one side of the electrolyte sheet and kept under a pressure of 300 Mpa for 5 min. And finally, placing the lithium sheet or the lithium indium alloy sheet on the other side of the electrolyte and maintaining the pressure for 5 min under the pressure of 50 Mpa. Finally, the battery is placed on a constant current charge-discharge instrument, firstly, cross-flow discharge is carried out to 1V (vs. Li/Li) + ) After the discharge, the battery was charged to a voltage of 4V (vs. Li/Li + ). Charge and discharge tests were then performed at voltage intervals 1-4V (see fig. 1a, 1b and 2).
The battery obtained by using the above example was subjected to a cross-flow charge-discharge test, and the active material of high capacity had been generated at the time of the first discharge to 1V, and the redox reaction occurring at the charge-discharge of the subsequent battery was all based on the generated active material.
As can be seen from the figure, the battery is first discharged to Li 3 PS 4 Below the electrochemical stability window, the reactions that occur are different following normal charge and discharge. At the first-round discharge, li 3 PS 4 Will decompose at low voltage to produce Li 2 S and other byproducts, li when the battery is charged 2 S will generate Li 2 S n And contributes to capacity. Due to Li 3 PS 4 Is irreversible and other by-products formed can also inhibit Li 3 PS 4 Further decomposition, this ensures an ion transport channel in the positive electrode. In the subsequent electrochemical reaction of the cell, only Li occurs 2 S and Li 2 S n And oxidation-reduction reaction between the two.
Example 2
Li is mixed with 7 P 3 S 11 Mixing with graphene according to a mass ratio of 5:5, and fully grinding and mixing to obtain the composite anode. For all-solid-state batteries using sulfide fast ion conductors as electrolytes, cold pressing methods can be used to prepare all-solid-state batteries, specifically: first, 0.1 g of Li is taken 7 P 3 S 11 The resulting mixture was placed in a swagelok-type battery under a pressure of 100 Mpa for 1 min, and then 10 mg of the above-mentioned composite positive electrode powder was uniformly spread on one side of the electrolyte sheet and kept under a pressure of 300 Mpa for 5 min. And finally, placing the lithium sheet or the lithium indium alloy sheet on the other side of the electrolyte and maintaining the pressure for 5 min under the pressure of 50 Mpa. Finally, the battery is placed on a constant current charge-discharge instrument, and is charged to 4.5V (vs. Li/Li) in a cross-flow manner + ) After the charge is completed, the battery is subjected to cross-current discharge to a voltage of 1V (vs. Li/Li + ). Charge and discharge tests were then performed at voltage intervals 1-4V (see fig. 1a, 1b and 3).
The battery obtained by using the above example was subjected to a cross-flow charge-discharge test, and the active material of high capacity had been generated when the battery was charged to 4.5V for the first time, and the redox reaction occurring in the charge-discharge of the subsequent battery was all based on the generated active material.
It can be seen from the figure that the use of in situ formation of high capacity active species greatly reduces the resistance of the cell reaction kinetics, which results in reduced electrochemical polarization of the cell reaction and a cell efficiency approaching 100%.
Example 3
Li is mixed with 10 GeP 2 S 12 Mixing with super P according to a mass ratio of 4:6, and fully grinding and mixing to obtain the composite anode. For all-solid-state batteries using sulfide fast ion conductors as electrolytes, cold-pressing methods can be used to prepare all-solid-state batteries. First, 0.1 g of Li is taken 10 GeP 2 S 12 The resulting mixture was placed in a swagelok-type battery under a pressure of 100 Mpa for 1 min, and then 10 mg of the above-mentioned composite positive electrode powder was uniformly spread on one side of the electrolyte sheet and kept under a pressure of 300 Mpa for 5 min. And finally, placing the lithium sheet or the lithium indium alloy sheet on the other side of the electrolyte and maintaining the pressure for 5 min under the pressure of 50 Mpa. Finally, the battery is placed on a constant current charge-discharge instrument, firstly, cross-flow discharge is carried out to 0.5V (vs. Li/Li) + ) After the discharge, the battery was charged to a voltage of 4V (vs. Li/Li + ). Charge and discharge tests were then performed at voltage intervals 1-4V (see fig. 1a and 1 b).
Example 4
Li is mixed with 10 SnP 2 S 12 Mixing with super P according to a mass ratio of 4:6, and fully grinding and mixing to obtain the composite anode. For all-solid-state batteries using sulfide fast ion conductors as electrolytes, cold-pressing methods can be used to prepare all-solid-state batteries. First, 0.1 g of Li is taken 10 SnP 2 S 12 The resulting mixture was placed in a swagelok-type battery under a pressure of 100 Mpa for 1 min, and then 10 mg of the above-mentioned composite positive electrode powder was uniformly spread on one side of the electrolyte sheet and kept under a pressure of 300 Mpa for 5 min. And finally, placing the lithium sheet or the lithium indium alloy sheet on the other side of the electrolyte and maintaining the pressure for 5 min under the pressure of 50 Mpa. Finally, the battery is placed on a constant current charge-discharge instrument, and is charged to 4.5V (vs. Li/Li) in a cross-flow manner + ) After the charge is completed, the battery is subjected to cross-current discharge to a voltage of 1V (vs. Li/Li + ). Charge and discharge tests were then performed at voltage intervals 1-4V (see fig. 1a and 1 b).
Example 5
Will be 0.7. 0.7 Li 2 S: 0.3P 2 S 5 Mixing with conductive carbon black according to a mass ratio of 5: 5. mixing, fully grinding and mixing to obtain the composite positive electrode. For all-solid-state batteries using sulfide fast ion conductors as electrolytes, cold-pressing methods can be used to prepare all-solid-state batteries. First, 0.1 g of Li is taken 10 GeP 2 S 12 The resulting mixture was placed in a swagelok-type battery under a pressure of 100 Mpa for 1 min, and then 10 mg of the above-mentioned composite positive electrode powder was uniformly spread on one side of the electrolyte sheet and kept under a pressure of 300 Mpa for 5 min. And finally, placing the lithium sheet or the lithium indium alloy sheet on the other side of the electrolyte and maintaining the pressure for 5 min under the pressure of 50 Mpa. Finally, the battery is placed on a constant current charge-discharge instrument, firstly, cross-flow discharge is carried out to 0.8V (vs. Li/Li) + ) After the discharge, the battery was charged to a voltage of 4V (vs. Li/Li + ). Charge and discharge tests were then performed at voltage intervals 1-4V (see fig. 1a and 1 b).
Example 6
Li is mixed with 10 SiP 2 S 12 Mixing with graphite according to a mass ratio of 7:3, and fully grinding and mixing to obtain the composite anode. For all-solid-state batteries using sulfide fast ion conductors as electrolytes, cold-pressing methods can be used to prepare all-solid-state batteries. First, 0.1 g of Li is taken 10 SiP 2 S 12 The resulting mixture was placed in a swagelok-type battery under a pressure of 100 Mpa for 1 min, and then 10 mg of the above-mentioned composite positive electrode powder was uniformly spread on one side of the electrolyte sheet and kept under a pressure of 300 Mpa for 5 min. And finally, placing the lithium sheet or the lithium indium alloy sheet on the other side of the electrolyte and maintaining the pressure for 5 min under the pressure of 50 Mpa. Finally, the battery is placed on a constant current charge-discharge instrument, and is charged to 4.5V (vs. Li/Li) in a cross-flow manner + ) After the charge is completed, the battery is subjected to cross-current discharge to a voltage of 0.5V (vs. Li/Li + ). Charge and discharge tests were then performed at voltage intervals 1-4V (see fig. 1a and 1 b).
Example 7
Li is mixed with 6 PS 5 Cl and ketjen black are mixed according to the mass ratio of 6:4, and the mixture is fully ground and mixed to be used as a composite anode. For fast separation with sulfidesAll-solid-state batteries in which the subconductors are electrolytes can be prepared by cold pressing. First, 0.1 g of Li is taken 10 GeP 2 S 12 The resulting mixture was placed in a swagelok-type battery under a pressure of 100 Mpa for 1 min, and then 10 mg of the above-mentioned composite positive electrode powder was uniformly spread on one side of the electrolyte sheet and kept under a pressure of 300 Mpa for 5 min. And finally, placing the lithium sheet or the lithium indium alloy sheet on the other side of the electrolyte and maintaining the pressure for 5 min under the pressure of 50 Mpa. Finally, the battery is placed on a constant current charge-discharge instrument, and is charged to 5.5V (vs. Li/Li) in a cross-flow manner + ) After the charge is completed, the battery is subjected to cross-current discharge to a voltage of 1V (vs. Li/Li + ). Charge and discharge tests were then performed at voltage intervals 1-4V (see fig. 1a and 1 b).
Example 8
Li is mixed with 6 PS 5 And mixing Br and KS graphite according to a mass ratio of 5:5, and fully grinding and mixing to obtain the composite anode. For all-solid-state batteries using sulfide fast ion conductors as electrolytes, cold-pressing methods can be used to prepare all-solid-state batteries. First, 0.1 g of Li is taken 6 PS 5 Cl was placed in a swagelok type cell under a pressure of 100 Mpa for 1 min, followed by uniformly spreading 10 mg of the above composite cathode powder on one side of the electrolyte sheet and under a pressure of 300 Mpa for 5 min. And finally, placing the lithium sheet or the lithium indium alloy sheet on the other side of the electrolyte and maintaining the pressure for 5 min under the pressure of 50 Mpa. Finally, the battery is placed on a constant current charge-discharge instrument, firstly, cross-flow discharge is carried out to 1V (vs. Li/Li) + ) After the discharge, the battery was charged to a voltage of 4V (vs. Li/Li + ). Charge and discharge tests were then performed at voltage intervals 1-4V (see fig. 1a and 1 b).
As can be seen from the above examples, fig. 1a and fig. 1b, which show the generation of active materials in the positive electrode after the battery is discharged at low voltage after the battery is assembled, show that decomposition of sulfide fast ion conductor occurs during the first cycle of discharge at low voltage; after the first cycle discharge of the battery is finished, high-capacity electrochemical active substance Li is generated 2 S, S. The active material in the positive electrode is generated after the battery is charged under high voltage after being assembled, and sulfide fast ion conductor can also be generated in the first cycle charging processDecomposition at high voltage; after the first cycle discharge of the battery is finished, high-capacity electrochemical active substance Li is generated 2 S n /S。

Claims (7)

1. The high-power all-solid-state battery comprises a positive electrode, a solid electrolyte and a negative electrode, and is characterized in that the positive electrode is obtained by mixing and grinding a sulfide fast ion conductor and a conductive agent, and the solid electrolyte is an ion transmission medium; wherein the sulfide fast ion conductor is xLi 2 S:(1-x)P 2 S 5 (x=0.6 -0.8), Li 3 PS 4 , Li 10 M x P 3-x S 12 (0 ≤ x ≤ 2, M= Si, Ge, Sn), Li 6 PS 5 X (x=cl, br, I) or a combination of several;
discharging the all-solid-state battery below an electrochemical stability window of a sulfide fast ion conductor; or charging to above the sulfide fast ion conductor electrochemical stability window; the sulfide fast ion conductor in the contact part with the conductive agent is decomposed to generate a battery active substance with capacity, and the active substance is generated in situ by electrochemical reaction, so that the active substance is in atomic-level contact with the sulfide fast ion conductor and the conductive agent, the ion and electron transmission is fast in the subsequent oxidation-reduction process, the solid-solid interface impedance is reduced, and the high multiplying power and the high cycling stability of the all-solid battery are further realized; the redox reactions occurring in the charge and discharge of the subsequent cell are all based on the active species generated in situ by the electrochemical reactions described above;
the mass ratio of the sulfide fast ion conductor to the conductive agent is 2:8-8:2.
2. a high power all-solid-state battery according to claim 1, wherein: the solid electrolyte sulfide fast ion conductor, oxide fast ion conductor or polymer solid electrolyte, wherein the sulfide fast ion conductor is xLi 2 S:(1-x)P 2 S 5 (x=0.6-0.8),Li 3 PS 4 ,Li 10 M x P 3-x S 12 (0 ≤ x ≤ 2, M= Si, Ge, Sn),Li 6 PS 5 X (x=cl, br, I) or a combination of several;the oxide fast ion conductor is Li 1-x Al x Ti 2-x (PO 4 ) 3 (0.1<x<0.6)、Li 3x La (2/3)-x TiO 3 (0.04<x<0.15)、Li 5 La 3 M 2 O 12 (M=Ta,Nb)、Li 5+x A x La 3-X M 2 O 12 (x=0,1,A=Ca,Sr,Ba,M=Nb,Ta,Bi)、ϒ-Al 2 O 3 One or more of the following; the polymer solid electrolyte is composed of a polymer and a lithium salt.
3. A high power all-solid-state battery according to claim 2, wherein: the polymer is one or more of polyoxyethylene, polyoxypropylene, polyacrylonitrile, polyvinyl chloride, polystyrene, polyvinyl carbonate, polyvinylpyrrolidone, polymethyl methacrylate, polyvinylidene fluoride, polyethylene glycol acrylate, polydivinylsulfide and derivatives thereof; the lithium salt is lithium perchlorate (LiClO) 4 ) Lithium bis (oxalato) borate (LiBOB), lithium difluoro (LiDFOB) oxalato borate, lithium trifluoro (CF) 3 SO 3 Li), lithium bis (trifluoromethylsulfonyl) imide (LiTFSI), lithium bis (fluorosulfonyl) imide (LiFSI).
4. A method of making a high power all-solid-state battery according to claim 1, characterized by: a positive electrode, a solid electrolyte and a negative electrode; or sequentially stacking the anode, the solid electrolyte and the cathode to form the integrated all-solid-state lithium battery with the sandwich structure.
5. The method for manufacturing a high-power all-solid-state battery according to claim 4, wherein: the negative electrode is one of a metal lithium sheet, a metal lithium alloy, graphite, hard carbon, molybdenum disulfide, lithium titanate, graphene and silicon carbon negative electrode.
6. The method of producing a high power all-solid-state battery according to claim 4, wherein said all-solid-state battery is discharged below an electrochemical stability window of a sulfide fast ion conductor with a cutoff voltage of 0 to 1.5V; or charging to above the electrochemical stability window of the sulfide fast ion conductor, and the cut-off voltage is 3-5v; the sulfide fast ion conductor in contact with the conductive agent is decomposed to generate a battery active substance with capacity, and the active substance is generated in situ by electrochemical reaction, so that the active substance is in atomic-level contact with the sulfide fast ion conductor and the conductive agent, the ion and electron transmission is fast in the subsequent oxidation-reduction process, the solid-solid interface impedance is reduced, and the high multiplying power and the high cycling stability of the all-solid battery are further realized.
7. A method of improving the efficiency of a solid state battery, characterized by: discharging the all-solid-state battery of claim 1 below the sulfide fast ion conductor electrochemical stability window with a cutoff voltage of 0-1.5V; or charging to above the electrochemical stability window of the sulfide fast ion conductor, and the cut-off voltage is 3-5v; and further can realize high multiplying power and high cycle stability of the all-solid-state battery.
CN201911342394.8A 2019-12-23 2019-12-23 High-power all-solid-state battery and preparation thereof Active CN111082128B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911342394.8A CN111082128B (en) 2019-12-23 2019-12-23 High-power all-solid-state battery and preparation thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911342394.8A CN111082128B (en) 2019-12-23 2019-12-23 High-power all-solid-state battery and preparation thereof

Publications (2)

Publication Number Publication Date
CN111082128A CN111082128A (en) 2020-04-28
CN111082128B true CN111082128B (en) 2023-10-20

Family

ID=70317020

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911342394.8A Active CN111082128B (en) 2019-12-23 2019-12-23 High-power all-solid-state battery and preparation thereof

Country Status (1)

Country Link
CN (1) CN111082128B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111628139B (en) * 2020-06-30 2021-09-21 中国第一汽车股份有限公司 All-solid-state battery electrode and preparation method and application thereof
JP7442022B2 (en) 2022-02-26 2024-03-01 三井金属鉱業株式会社 Composite material and its manufacturing method
CN114613996B (en) * 2022-03-07 2024-06-21 中国科学院宁波材料技术与工程研究所 High-capacity molybdenum polysulfide composite positive electrode material for all-solid-state battery, and preparation method and application thereof
CN117701928B (en) * 2023-11-28 2024-08-30 西安工业大学 Micro-nano LiSr alloy composite material, preparation method and application thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180011207A (en) * 2015-06-01 2018-01-31 뉴매티코트 테크놀로지스 엘엘씨 Method for manufacturing a battery containing a nano-engineered coating and a nano-engineered coating for an anode active material, a cathode active material, and a solid-state electrolyte
CN108899486A (en) * 2018-06-14 2018-11-27 中国人民解放军国防科技大学 Sulfur electrolyte-coated positive electrode active material and preparation method thereof, and all-solid-state lithium sulfur battery and preparation method thereof
CN109256555A (en) * 2018-10-16 2019-01-22 清华大学 A kind of sulphur system composite positive pole and its solid lithium battery and their preparation method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9466834B2 (en) * 2013-08-23 2016-10-11 Ut-Battelle, Llc Lithium-conducting sulfur compound cathode for lithium-sulfur batteries

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180011207A (en) * 2015-06-01 2018-01-31 뉴매티코트 테크놀로지스 엘엘씨 Method for manufacturing a battery containing a nano-engineered coating and a nano-engineered coating for an anode active material, a cathode active material, and a solid-state electrolyte
CN108899486A (en) * 2018-06-14 2018-11-27 中国人民解放军国防科技大学 Sulfur electrolyte-coated positive electrode active material and preparation method thereof, and all-solid-state lithium sulfur battery and preparation method thereof
CN109256555A (en) * 2018-10-16 2019-01-22 清华大学 A kind of sulphur system composite positive pole and its solid lithium battery and their preparation method

Also Published As

Publication number Publication date
CN111082128A (en) 2020-04-28

Similar Documents

Publication Publication Date Title
CN111082128B (en) High-power all-solid-state battery and preparation thereof
JP5217076B2 (en) Lithium ion battery
KR101670327B1 (en) Composite cathode materials with controlled irreversible capacity loss for lithium ion batteries
CN111295789A (en) Solid electrolyte material and battery
Shi et al. Electrochemical impedance spectroscopic study of the electronic and ionic transport properties of NiF2/C composites
CN110707287B (en) Metal lithium negative electrode, preparation method thereof and lithium battery
CN103000884A (en) Vanadium sodium phosphate composite material as well as preparation method and application thereof
CN109980285A (en) For lithium-chalcogen battery electrolyte system
CN115020678B (en) Positive electrode active material, electrochemical device, and electronic device
CN103855389A (en) Ferric (III) fluoride / carbon composite material and its preparation method and application
CN101116200A (en) Positive electrode and nonaqueous electrolyte secondary battery using the same
CN110875490B (en) Lithium ion battery and preparation method thereof
CN102160215A (en) Nonaqueous electrolyte secondary battery
JP5151329B2 (en) Positive electrode body and lithium secondary battery using the same
US10446826B2 (en) Method for making lithium ionic energy storage element
CN105470473A (en) Positive electrode active material and secondary battery
CN116845235B (en) Positive electrode material, positive electrode sheet and battery
CN105720265A (en) Carbon nanotube polymer lithium ion battery and preparation method thereof
KR20150016018A (en) Composite electrode comprising different electrode active material and electrode assembly
CN103682293A (en) Lithium-rich solid solution positive electrode material as well as preparation method of lithium-rich solid solution positive electrode material, lithium ion battery positive electrode material and lithium ion battery
WO2017179541A1 (en) Electricity storage device, and charging method and manufacturing method therefor
CN102637876B (en) Lithium battery anode material and method for improving cycle performance of battery
KR20130140945A (en) Lithium-ion capacitor and manufacturing method of therof
KR20110078307A (en) Metal based zn negative active material and lithium secondary battery comprising thereof
CN115051030A (en) Battery electrolyte and lithium ion battery

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant