WO2021008360A1 - Sulfide solid-state electrolyte sheet and preparation method therefor, battery containing solid-state electrolyte sheet, and device - Google Patents

Sulfide solid-state electrolyte sheet and preparation method therefor, battery containing solid-state electrolyte sheet, and device Download PDF

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WO2021008360A1
WO2021008360A1 PCT/CN2020/099496 CN2020099496W WO2021008360A1 WO 2021008360 A1 WO2021008360 A1 WO 2021008360A1 CN 2020099496 W CN2020099496 W CN 2020099496W WO 2021008360 A1 WO2021008360 A1 WO 2021008360A1
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electrolyte sheet
solid electrolyte
sulfide solid
sulfide
solid
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PCT/CN2020/099496
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French (fr)
Chinese (zh)
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梁成都
刘成勇
胡波兵
郭永胜
李谦
付佳玮
程萌
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宁德时代新能源科技股份有限公司
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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
    • 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
    • H01M10/058Construction or manufacture
    • 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

Definitions

  • This application relates to the field of batteries, in particular to a sulfide solid electrolyte sheet and a preparation method thereof, and also to a battery and a device containing the sulfide solid electrolyte sheet.
  • lithium-ion batteries have become the most widely used secondary battery technology in social life.
  • negative news about the smoke, fire and even explosion of lithium batteries is endless.
  • the safety and energy density of lithium ion batteries need to be improved.
  • the existing solid electrolytes can be divided into three categories according to the material system: sulfide solid electrolytes, oxide solid electrolytes and polymer solid electrolytes.
  • the sulfide solid electrolyte is also one of the most promising solid electrolyte systems because of its ionic conductivity comparable to that of liquid electrolytes and the processing characteristics of easier shaping and densification at room temperature.
  • the existing sulfide solid electrolytes still have problems such as low ion conductivity, and the sulfide solid state batteries also need to improve the energy density and cycle performance.
  • the purpose of this application is to provide a sulfide solid electrolyte sheet and a preparation method thereof to improve the conductivity of the solid electrolyte sheet and the energy density and cycle performance of the battery, and contain the sulfide Batteries and devices with solid electrolyte sheets.
  • the first aspect of the present application provides a sulfide solid electrolyte sheet, which comprises a sulfide electrolyte material and a boron element doped in the sulfide electrolyte material, and the surface of the solid electrolyte sheet is arbitrary
  • the relative deviation (B 0 -B 100 )/B 0 of the boron element mass concentration at the position B 0 and the boron element mass concentration B 100 at a distance of 100 ⁇ m from the surface of the solid electrolyte sheet to the position is not more than 20%, preferably (B 0 -B 100 )/B 0 does not exceed 10%.
  • the second aspect of the application provides a method for preparing the sulfide solid electrolyte sheet according to the first aspect of the application, including:
  • the initial product is subjected to more than one post-treatment, and each post-treatment sequentially includes the steps of grinding, cold pressing and sintering.
  • the third aspect of the application provides an all-solid-state lithium ion battery, which is prepared by the sulfide solid electrolyte sheet according to the first aspect of the application or the sulfide solid electrolyte sheet prepared according to the preparation method according to the second aspect of the application Prepared.
  • the fourth aspect of the present application provides a laminated all-solid-state lithium ion battery, including a positive pole piece, a solid electrolyte sheet and a negative pole piece; wherein the solid electrolyte sheet is the sulfide described in the first aspect of the application A solid electrolyte sheet or a sulfide solid electrolyte sheet prepared according to the preparation method described in the second aspect of the application.
  • a fifth aspect of the present application provides a device, including the all-solid-state lithium ion battery described in the third aspect of the present application or the laminated all-solid-state lithium ion battery described in the fourth aspect of the present application.
  • borate is used as the doping raw material to modify the sulfide solid electrolyte.
  • the doping of B element can reduce the binding effect of anions on lithium ions and improve the transmission capacity of lithium ions;
  • O element is partially doped
  • Substitution of S element can not only produce mixed anion effect to improve lithium ion conductivity, but also inhibit the formation of space charge layer at the interface between oxide cathode and sulfide electrolyte, and reduce the interface impedance; and the borate introduced in the doping process acts as Lewis Acid, with 2P empty orbital, can form a complex with the electron donor of the sulfide electrolyte material, promote the full reaction of the sulfide electrolyte material and the doping material, and improve the doping uniformity and conductivity of the reaction product.
  • the inventor believes that in the doping modification process of the solid electrolyte, if the raw material of the sulfide electrolyte is directly mixed with the cation or anion inorganic compound (such as boron sulfide) that needs to be doped, the heat treatment is caused due to the solid state between the inorganic particles.
  • this mixing method is difficult to achieve a uniform dispersion effect, and it is easy to cause the formation of impurity phases during raw material mixing and heat treatment.
  • the present application utilizes the property of borate to form a uniformly dispersed solution in the solvent to realize the full mixing of the electrolyte raw materials and the borate to be doped.
  • the borate can be completely decomposed at the phase forming temperature of the sulfide electrolyte, thereby reducing the introduction of impurities or residual reactants, so that the ionic conductivity of the prepared sulfide solid electrolyte is significantly improved, which is beneficial to the complete The energy density of solid-state lithium-ion batteries is exerted.
  • the inventor also believes that during the heat treatment process for preparing the sulfide solid electrolyte, the volatilization of the solvent and the decomposition of the organic borate will cause damage to the structure of the electrolyte sheet and poor contact between particles, thereby affecting doping.
  • the diffusion process of elements in the solid electrolyte Therefore, the present application achieves sufficient diffusion and uniform distribution of the modified element in the electrolyte material through repeated grinding, cold pressing and sintering processes, and finally uniform doping of boron element Sulfide electrolyte sheet.
  • the solid electrolyte sheet of the embodiment of the present application due to the introduction of boron element, the binding effect of anions on lithium ions is effectively reduced, and the transmission capacity of lithium ions is improved; on the other hand, due to the boron element in the solid electrolyte sheet It not only improves the doping uniformity and conductivity of the solid electrolyte sheet, but also significantly improves the surface roughness of the solid electrolyte sheet, which is beneficial to the diffusion process of lithium ions at the interface between the electrolyte sheet and the lithium metal anode. Reduce interface impedance and improve battery cycle performance.
  • Fig. 1 is an XRD test pattern of a solid electrolyte according to an embodiment of the present application
  • FIG. 3 is a graph of element distribution test results of a solid electrolyte according to an embodiment of the present application.
  • FIG. 4 is an optical microscope diagram of the surface roughness test of a solid electrolyte sheet according to an embodiment of the present application.
  • Fig. 5 is a schematic diagram of a device according to an embodiment of the present application.
  • the sulfide solid electrolyte sheet provided by the embodiment of the present application includes a sulfide electrolyte material and a boron element doped in the sulfide electrolyte material, and the mass concentration of boron element at any position on the surface of the sulfide electrolyte sheet is B 0 with a surface concentration of sulfide electrolyte plate B 100 relative deviation from the mass of boron element 100 ⁇ m at the location (B 0 -B 100) / B 0 not exceed 20%.
  • the relative deviation (B 0 -B 100 )/B 0 does not exceed 10%, for example, does not exceed 9%, 8%, 7%, 6%, 5%, and any value in between , Preferably not more than 8%.
  • boron is introduced into the sulfide electrolyte, which can effectively reduce the binding effect of anions on lithium ions and improve the transmission capacity of lithium ions; and, boron is present on the surface of the sulfide solid electrolyte sheet. Uniform distribution not only improves the doping uniformity and conductivity of the solid electrolyte sheet, but also significantly improves the surface roughness of the solid electrolyte sheet, which facilitates the diffusion process of lithium ions between the solid electrolyte sheet and the lithium metal anode interface, thereby reducing Interface impedance and improve battery cycle performance.
  • the surface roughness of the solid electrolyte sheet is 3 ⁇ m to 15 ⁇ m, for example, 3 ⁇ m, 4 ⁇ m, 5 ⁇ m, 6 ⁇ m, 7 ⁇ m, 8 ⁇ m, 9 ⁇ m, 10 ⁇ m, 11 ⁇ m, 12 ⁇ m, 13 ⁇ m, 14 ⁇ m, and some of them.
  • the arbitrary value between is preferably 3 ⁇ m to 10 ⁇ m.
  • the surface roughness of the sulfide solid electrolyte sheet is 3 ⁇ m to 6 ⁇ m.
  • the surface roughness of the electrolyte sheet refers to: placing the electrolyte sheet under a high-precision optical microscope for observation, and obtaining the surface height distribution information of the electrolyte sheet in an area of 200*300 ⁇ m 2 in 3D imaging mode.
  • the surface roughness can be obtained by counting the difference in the maximum surface height of the electrolyte sheet.
  • the improvement of the surface roughness of the electrolyte sheet facilitates the diffusion process of lithium ions at the interface between the electrolyte sheet and the lithium metal anode, thereby reducing the interface impedance and improving the cycle performance of the battery.
  • the surface roughness of the electrolyte sheet is too large, its surface morphology is uneven, while the surface of the lithium metal anode is smooth, so the interface contact between the electrolyte and the lithium metal is very insufficient, which makes the interface migration of lithium ions more difficult. Improving the surface roughness of the electrolyte helps increase its contact points with lithium metal, thereby promoting the transport of lithium ions at the interface and reducing the interface polarization.
  • the composition and morphology of the electrolyte material have a limit to the surface roughness.
  • the surface roughness ranges from 3 ⁇ m to 15 ⁇ m, preferably 3 ⁇ m to 10 ⁇ m.
  • the electrical conductivity of the solid electrolyte sheet is 1.6 mS/cm to 2.9 mS/cm, for example 1.6 mS/cm, 1.7 mS/cm, 1.9 mS/cm, 2.1 mS/cm, 2.3 mS/cm, 2.4mS/cm, 2.5mS/cm, 2.6mS/cm, 2.7mS/cm, 2.8mS/cm, 2.9mS/cm and any value between them, preferably 2.1mS/cm ⁇ 2.8mS /cm.
  • Electrolyte conductivity is affected by the content and uniformity of distribution of doped boron in the electrolyte sheet.
  • improving the uniformity of boron doping is beneficial to increase the conductivity.
  • the influence of doping a small amount of elements and improving the uniformity of element distribution on the electrolyte body structure is limited, and the conductivity improvement effect that can be achieved has a certain range.
  • the conductivity range under the improved condition is 1.7mS/ cm ⁇ 2.8mS/cm, the preferred range is 2.1mS/cm ⁇ 2.8mS/cm.
  • the mass percentage of the boron element in the electrolyte sheet is 0.5%-10%, for example, 1%, 2%, 3%, 4%, 5%, 6%, 7% , 8%, 9%, 10% and any value between them, preferably 3% to 7%.
  • the doping of boron has little effect on the electrolyte structure. Although it can also improve the conductivity to a certain extent, the effect of this improvement is not significant, and the boron is too low
  • the content will cause the concentration test error to increase, so the measured concentration deviation will be larger.
  • the content of boron in the electrolyte sheet is too high, the problem of local element enrichment is likely to occur, which is not conducive to achieving uniform modification results, and too high doping of boron element will reduce the relative content of lithium ions in the electrolyte sheet. The content is not conducive to improving the conductivity of the electrolyte sheet and battery performance.
  • the sulfide electrolyte material includes Li 2 S ⁇ P 2 S 5 , Li 2 S ⁇ GeS 2 , Li 2 S ⁇ SiS 2 , Li 6 PS 5 X, and Li 7 P 3 S 11 One or more of them, wherein X is selected from at least one of Cl, Br, and I, preferably Cl.
  • sulfide electrolyte materials can achieve the effect of improving the conductivity and surface uniformity of the doped solid electrolyte through the doping of boron and the improvement of the uniformity of the distribution of boron on the surface of the electrolyte sheet. Therefore, this application is implemented In the sulfide solid electrolyte sheet of the method, the type of sulfide electrolyte material contained is not limited.
  • the embodiments of the present application also provide a method for preparing the above-mentioned sulfide solid electrolyte sheet, including:
  • the initial product is subjected to more than one post-treatment, and each post-treatment sequentially includes the steps of grinding, cold pressing and sintering.
  • borate is used as the doping material to obtain a solid electrolyte co-doped with boron and oxygen, wherein the doping of boron element can reduce the binding effect of anions on lithium ions, and improve lithium ions.
  • Partial doping of oxygen element to replace sulfur element can not only produce mixed anion effect to improve lithium ion conductivity, but also inhibit the formation of space charge layer at the interface between oxide cathode and sulfide electrolyte, and reduce interface impedance; and the doping process
  • the borate ester introduced in the sulfide has a 2P empty orbital, which can form a complex with the sulfide solid electrolyte electron donor to promote the full reaction of the sulfide solid electrolyte with the doping material, thereby improving the doping uniformity of the reaction product And conductivity.
  • the above method utilizes the property that the borate can form a uniformly dispersed solution in a suitable solvent.
  • the electrolyte raw material and the borate to be doped are fully mixed.
  • the DSC-TG test showed that the borate has an endothermic decomposition peak and a weight loss curve in the range below the sulfide phase formation temperature, that is to say, the borate can be completely decomposed at the phase formation temperature of the sulfide electrolyte, thereby reducing
  • the introduction of impurities or residual reactants makes the final sulfide electrolyte ionic conductivity significantly improved.
  • the above method also solves the problem that the electrolyte sheet structure is damaged due to the volatilization of the solvent and the decomposition of the organic borate during the heat treatment, and the poor contact between the particles and the particles, thereby affecting the diffusion process of the doping elements in the solid electrolyte.
  • the boron element is uniformly distributed in the electrolyte, so that the doping uniformity and conductivity of the solid electrolyte are improved, and the surface roughness of the solid electrolyte sheet is significantly improved.
  • the solid electrolyte sheet with uniform surface morphology promotes the diffusion process of lithium ions at the interface between the solid electrolyte sheet and the lithium metal anode, reduces the interface impedance and improves the cycle performance of the battery.
  • the sulfide electrolyte raw material is dispersed in an organic solvent to form an initial reaction mixture.
  • the borate is dispersed in an organic solvent to form a modified solution.
  • the borate has a structure represented by formula (I):
  • R is selected from C1-C4 alkyl.
  • the borate is selected from one or more of the structures (I-1) to (I-4):
  • the initial reaction mixture is mixed with the modified solution and then fully dispersed, and the time for the fully dispersed is 5-20 hours.
  • the organic solvent used to disperse the sulfide electrolyte material and the organic solvent used to disperse the borate may be independently selected from tetrahydrofuran, acetonitrile, pyridine, methanol, ethanol, propanol, isopropanol, butane One or more of alcohol, propyl propionate, butyl propionate, and butyl butyrate.
  • the volume ratio of the sulfide electrolyte raw material and the organic solvent can be 1:1 to 1: 10.
  • the volume ratio of borate and organic solvent blending can be 1:1 to 1:10.
  • the blending method used when mixing the initial reaction mixture with the modifying solution, may be a ball milling method.
  • the drying process needs to be performed in a vacuum environment with a vacuum degree of less than -90 kPa, and the drying temperature is 100°C to 120°C.
  • the number of post-treatments is 2 to 3 times.
  • the doped electrolyte material undergoes multiple grinding, tableting and sintering, the distribution of various elements in the bulk material tends to be uniform, and the surface roughness and interface impedance are reduced.
  • too many high-temperature sintering may also cause structural phase changes in the electrolyte, which affects the increase in conductivity.
  • the sintering temperature is 200°C to 700°C, such as 200°C, 300°C, 400°C, 500°C, 550°C, 600°C and any value in between, preferably 200°C. °C ⁇ 600°C.
  • the sintering temperature is 200°C to 400°C.
  • the sintering temperature can affect the performance of the prepared solid electrolyte and battery. Specifically, the sintering temperature should match the phase formation temperature of the sulfide and the decomposition temperature of the borate. If the heat treatment temperature is too low, the specific electrolyte crystal structure cannot be obtained and the borate is not completely decomposed, although the electrolyte conductivity However, the effective amount of B doping is extremely low, resulting in a small increase in conductivity; if the sintering temperature is too high, the electrolyte itself is prone to phase change and impurity generation, and the increase in conductivity and capacity will also decrease. small.
  • the sintering temperature in each post-treatment increases as the number of post-treatments increases.
  • the sintering temperature should not be too high. If the first sintering temperature is too high, the volatilization of the solvent, the decomposition of the borate and the phase formation of the sulfide electrolyte are concentrated in this sintering step, and the two processes of volatilization of the solvent and the decomposition of the borate.
  • the constant volume change in the electrolyte causes the compacted electrolyte block to become a porous and loose structure, and the particle-to-particle contact is not good, which is not conducive to the diffusion process of the boron element in the electrolyte phase, which makes the difference and uniformity of the electrolyte surface composition increase.
  • long-term high-temperature sintering will also lead to the formation of electrolyte impurities and the decrease of conductivity, which will further affect the interface impedance and cycle performance of the battery.
  • the sintering temperature of the first post-treatment is 200°C to 700°C, for example, 200°C, 300°C, 400°C, 500°C, 550°C, 600°C and any value in between, Preferably it is 200 to 400 degreeC.
  • a moderate sintering temperature needs to be selected, preferably higher than the first sintering temperature. If the second sintering temperature is too low, the borate cannot be decomposed, the phase formation process of the electrolyte and the boron element modification process are not complete, or they can only be assembled in the third post-treatment process. As a result, the electrolyte sheet still cannot maintain good interface contact, which is not conducive to the uniform distribution of boron and the improvement of surface properties.
  • the phase formation process of the electrolyte and the boron element modification process will be concentrated in the second post-treatment, which is not conducive to the uniform modification effect, and the too high heat treatment temperature has an effect on the conductivity of the electrolyte. There are also adverse effects.
  • the sintering temperature of the first post-treatment is 200°C to 700°C, for example, 200°C, 300°C, 400°C, 500°C, 550°C, 600°C and any value in between, Preferably it is 300 to 500 degreeC.
  • the sintering temperature of the second post-treatment is higher than the sintering temperature of the first post-treatment by 0-400°C, preferably 100-200°C.
  • the sintering temperature of three temperature zones, low, medium and high temperature is adopted in sequence, which is beneficial to distinguish the different reactions in the electrolyte modification process, so as to prepare an electrolyte sheet with uniform boron element distribution.
  • the cold pressing refers to cold pressing under a cold pressure of 50 MPa to 200 MPa.
  • the time for each sintering is 0.5-5 hours.
  • the heat treatment atmosphere may be an inert atmosphere such as argon and nitrogen.
  • the embodiments of the present application also provide an all-solid-state lithium-ion battery prepared by the solid-state electrolyte sheet of the embodiments of the present application.
  • the all-solid-state lithium-ion battery can be all-solid-state in various forms. Lithium Ion Battery.
  • the embodiments of the present application also provide a laminated all-solid-state lithium-ion battery, including a positive pole piece, a solid electrolyte sheet, and a negative pole piece; wherein, the solid electrolyte sheet is an application implementation Way of solid electrolyte sheet.
  • the positive pole piece is prepared from raw materials comprising a solid electrolyte sheet, a positive electrode active material, and a conductive agent; wherein, the solid electrolyte sheet is the solid electrolyte sheet according to the application embodiment.
  • the preparation method of the laminated all-solid-state lithium ion battery includes the following steps:
  • the step S1 includes:
  • the positive electrode powder is dispersed on the surface of the positive electrode current collector aluminum foil and cold pressed to obtain the positive electrode pole piece.
  • the positive pole piece, solid electrolyte sheet, and negative pole piece are respectively sliced according to the required size, and the sliced positive pole piece, solid electrolyte sheet, and negative pole piece are aligned in the center and sequentially stacked into a sandwich layer unit, and the sandwich layer unit Press and compound together at a certain temperature to obtain the battery cell of the all-solid-state lithium-ion battery; cold-press the battery cell and place it in an outer package to form an all-solid-state lithium-ion battery, which includes a positive pole piece and a negative pole Sheet and solid electrolyte sheet spaced between the positive pole piece and the negative pole piece.
  • the embodiments of the present application also provide a device, including the all-solid-state lithium ion battery described in the third aspect of the present application or the laminated type described in the fourth aspect of the present application. All solid-state lithium-ion battery.
  • the all-solid-state lithium-ion battery or laminated all-solid-state lithium-ion battery can be used as the power source of the device, and can also be used as the energy storage unit of the device.
  • the device of the present application adopts the all-solid-state lithium-ion battery or laminated all-solid-state lithium-ion battery provided in this application, and therefore has at least the same advantages as the all-solid-state lithium-ion battery or the laminated all-solid-state lithium-ion battery.
  • the device can be, but is not limited to, mobile devices (such as mobile phones, laptop computers, etc.), electric vehicles (such as pure electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, electric bicycles, electric scooters, electric golf Vehicles, electric trucks, etc.), electric trains, ships and satellites, energy storage systems, etc.
  • mobile devices such as mobile phones, laptop computers, etc.
  • electric vehicles such as pure electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, electric bicycles, electric scooters, electric golf Vehicles, electric trucks, etc.
  • electric trains ships and satellites, energy storage systems, etc.
  • Figure 5 is a device as an example.
  • the device is a pure electric vehicle, a hybrid electric vehicle, or a plug-in hybrid electric vehicle.
  • a battery pack or battery module can be used.
  • the device may also be a mobile phone, a tablet computer, a notebook computer, etc.
  • the device is generally required to be light and thin, and the battery of the embodiment of the present application can be used as a power source.
  • each post-treatment includes: grinding, cold pressing and sintering steps, among which, cold pressing forms a compact disc sample; sintering is to sinter the disc sample in an argon atmosphere; multiple post-treatments Then a doped modified solid electrolyte sheet is obtained.
  • the specific preparation parameters of the solid electrolyte sheets in Examples 1-14 and Comparative Examples 1-4 are shown in Table 1.
  • the solid electrolyte sheet was prepared according to the method of Example 1-14 or Comparative Example 1-4, ground into a powder, and combined with the positive electrode active material LiNi 1/3 Co 1/3 Mn 1/3 O 2 and the conductive agent Super-P The mass ratio of 70:27:3 is mixed and ground to obtain a uniformly dispersed positive electrode powder; the positive electrode powder is uniformly dispersed on the surface of the positive electrode current collector aluminum foil, and then the positive pole piece is obtained by cold pressing of 50MPa.
  • the solid electrolyte sheet was prepared according to the method of Examples 1-14 or Comparative Examples 1-4.
  • the lithium foil is attached to the surface of the negative electrode current collector copper foil by rolling, and then the negative electrode piece is obtained by slitting.
  • the above-mentioned positive pole piece, solid electrolyte sheet, and lithium metal negative electrode are sequentially stacked, and pressurized at 300 MPa to prepare an all-solid lithium ion battery.
  • Conductivity test Use Chenhua electrochemical workstation to measure the ohmic impedance of the electrolyte sheet.
  • the test temperature is 25°C
  • the frequency range is 1Hz-1MHz
  • the perturbation signal is 5mV. It can be calculated based on the impedance, thickness and area of the electrolyte layer Ionic conductivity.
  • Element content test The electrolyte sheet is dissolved in methanol solvent to form a uniform solution, and then the concentration of each element in the solution is quantitatively characterized by ICP (Inductively Coupled Plasma Emission Spectroscopy) test to obtain the boron element in the electrolyte sheet. content.
  • ICP Inductively Coupled Plasma Emission Spectroscopy
  • Interface impedance test Use Chenhua electrochemical workstation to conduct electrochemical impedance test on all solid-state lithium-ion batteries, the frequency range is 0.01Hz-1MHz, and the perturbation signal is 5mV.
  • Cycle performance test At 25°C, charge the all-solid-state lithium-ion battery at a constant current of 0.1C to a voltage of 4.2V, then discharge at a constant current of 0.1C until the final voltage is 2.8V, and record the discharge of the first cycle capacity. Then carry out charging and discharging cycles according to the above operation. When the cycle reaches 100 cycles, stop charging and discharging. The ratio of the discharge capacity at this time to the first cycle discharge capacity is the cycle capacity retention rate of the battery.
  • Figure 1 is an XRD test spectrum of a solid electrolyte according to an embodiment of the present application. It can be seen from the figure that the main lattice diffraction peaks of the solid electrolyte doped with borate are the same as the control sample, which proves that a small amount of borate The introduction will not affect the structure of the sulfide electrolyte; and the diffraction peak of borate itself does not appear in the doped sample, indicating that the borate has been completely decomposed.
  • Figure 2 is a graph of the Raman test results of the solid electrolyte according to the embodiment of the present application. It can be seen from the figure that the solid electrolyte doped with borate only has the same peak position as the control sample, which represents the solid state of sulfide.
  • the PS 4 -group in the electrolyte also shows that the main structure of the solid electrolyte has not changed before and after doping.
  • Figure 3 is a graph of the element distribution test results of the solid electrolyte according to the embodiment of the present application. It can be clearly seen from the figure that the distribution area of the B and O elements and the distribution area of the S element basically overlap, which proves that the B and O elements are evenly doped The impurities enter the sulfide electrolyte.
  • Fig. 4 is an optical microscope diagram of a surface roughness test of a solid electrolyte sheet according to an embodiment of the present application.
  • the electrolyte sheets of Comparative Example 1, Comparative Example 2 and Example 12 were placed under a high-precision optical microscope for observation.
  • 4-A is an optical microscope image of the solid electrolyte sheet of Comparative Example 1, which did not incorporate boric acid.
  • the surface morphology of the electrolyte sheet is very uneven. The figure shows that the maximum surface height difference is 24.36 ⁇ m;
  • 4-B is the optical microscope image of the solid electrolyte sheet of Comparative Example 2, which is doped with borate, but only through After one post-treatment, the surface roughness of the electrolyte sheet has been reduced.
  • Table 1 shows the influence of various parameters in the embodiments of the present application on the performance of the solid electrolyte and lithium ion battery prepared.
  • Examples 1 to 5 show the influence of the content change of the boron element in the electrolyte sheet on the performance of the electrolyte sheet.
  • the content of boron in the electrolyte sheet is too low (as in Example 1), the introduction of boron has little effect on the electrolyte structure. Although it can also improve the conductivity of the electrolyte sheet to a certain extent, the improvement effect is not significant , And too low boron content will increase the concentration test error, so the measured concentration deviation is also larger.
  • the mass concentration of the boron element in the electrolyte sheet is 0.5% to 10%, preferably 3% to 7%.
  • Example 3 show the effect of changes in the number of post-treatments on the performance of the electrolyte sheet. It can be seen from Table 1 that Example 6 achieves better performance than Example 3. This is because as the number of post-treatments increases, the doped electrolyte material undergoes multiple grinding, briquetting and sintering. The distribution of multiple elements in the bulk material tends to be uniform, and the surface roughness and interface impedance are reduced. However, too many high-temperature sintering may also cause structural phase changes in the electrolyte, which affects the increase in conductivity. Therefore, in the embodiment of the present application, the number of post-processing should be more than once, preferably 2 to 3 times.
  • Examples 6-12 take three post-treatments as an example to illustrate the technical effect of the gradual increase in the sintering temperature as the number of post-treatments increases.
  • the sintering temperature should not be too high. It can be seen from Table 1 that among Examples 6-9, Example 7 achieved the best performance improvement, followed by Examples 8, 9, and 6. This is because the first sintering temperature of Example 6 is too high. The volatilization of the solvent, the decomposition of boric acid ester and the phase formation of the sulfide electrolyte are concentrated in the first sintering step, and the volume is continuously generated during the first two processes.
  • the change causes the compacted electrolyte block to become a porous and loose structure, and the poor contact between particles will affect the diffusion process of boron in the electrolyte bulk, resulting in increased differences in electrolyte surface composition and reduced uniformity; and High temperature sintering over time will also lead to the formation of electrolyte miscellaneous phases and the decrease of conductivity, which will further affect the interface impedance and cycle performance of the battery. Therefore, in the embodiment of the present application, the performance is best when the sintering temperature in the first post-treatment is 200°C.
  • a moderate sintering temperature needs to be selected, preferably higher than the first sintering temperature.
  • the data of Examples 7 and 10 to 12 illustrate the effect of changing the second sintering temperature on the electrolyte sheet and battery performance.
  • Example 12 has the best performance, followed by Examples 11 and 7, and Example 10 has improved performance Slightly smaller.
  • the electrolyte phase formation process and the boron element modification process are concentrated in the second post-treatment, which is not conducive to the uniform modification effect, and the heat treatment temperature is too high It also has an adverse effect on the conductivity of the electrolyte.
  • the sintering temperature in three temperature zones of low, medium and high temperature is adopted in sequence, which is beneficial to distinguish the different reactions in the electrolyte modification process, so as to prepare an electrolyte sheet with uniform boron element distribution.
  • the surface composition and morphology of the electrolyte sheet are highly uniform, and its surface roughness and ionic conductivity are significantly improved, thereby improving the interface performance and cycle performance of the solid-state battery.
  • Examples 13 and 14 show the effect of changing the electrolyte type on the electrolyte sheet and battery performance.
  • electrolyte sheets with uniformly modified boron elements can be obtained.
  • the surface element distribution, surface morphology and ion conductivity are significantly improved. Therefore,
  • the type of the sulfide electrolyte material contained is not limited.

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Abstract

The present application relates to a sulfide solid-state electrolyte sheet and a preparation method therefor, a battery containing the solid-state electrolyte sheet, and a device. Specifically, the sulfide solid-state electrolyte sheet provided by the present application comprises a sulfide electrolyte material and boron element with which the sulfide electrolyte material is doped; the relative deviation (B 0-B 100)/B 0 between the boron element mass concentration B 0 at any position on the surface of the electrolyte sheet and the boron element mass concentration B 100 at a distance of 100 μm from said position does not exceed 20%. In the present application, the boron element introduced to the sulfide solid-state electrolyte can effectively reduce the binding effect of anions on lithium ions, and improve the transmission capacity of lithium ions; the boron element is uniformly distributed in the sulfide solid-state electrolyte, the doping uniformity and conductivity of the solid-state electrolyte are both improved, and the surface roughness of the solid-state electrolyte sheet is significantly ameliorated, thereby facilitating diffusion of lithium ions in the sulfide solid-state electrolyte sheet and lithium metal anode interface, reducing the interfacial resistance, and improving the battery cycle performance.

Description

硫化物固态电解质片及其制备方法、含有该固态电解质片的电池及装置Sulfide solid electrolyte sheet and preparation method thereof, battery and device containing the solid electrolyte sheet
本申请要求享有2019年7月16日提交的名称为“一种硫化物固态电解质片及其制备方法”的中国专利申请CN 201910641267.1的优先权,其全部内容通过引用并入本文中。This application claims the priority of the Chinese patent application CN 201910641267.1 entitled "A sulfide solid electrolyte sheet and its preparation method" filed on July 16, 2019, the entire content of which is incorporated herein by reference.
技术领域Technical field
本申请涉及电池领域,尤其涉及一种硫化物固态电解质片及其制备方法,还涉及含有所述硫化物固态电解质片的电池及装置。This application relates to the field of batteries, in particular to a sulfide solid electrolyte sheet and a preparation method thereof, and also to a battery and a device containing the sulfide solid electrolyte sheet.
背景技术Background technique
近年来,随着消费类电子设备和电动汽车行业的快速发展,锂离子电池成为了社会生活中应用最为广泛的二次电池技术。但是,伴随着锂电池产品数量的迅猛增长,锂电池冒烟、着火甚至爆炸的负面新闻也是不绝于耳,锂离子电池的安全性和能量密度有待提高。In recent years, with the rapid development of consumer electronic equipment and electric vehicle industries, lithium-ion batteries have become the most widely used secondary battery technology in social life. However, with the rapid growth in the number of lithium battery products, negative news about the smoke, fire and even explosion of lithium batteries is endless. The safety and energy density of lithium ion batteries need to be improved.
传统的液态锂电池由于液态电解质自身易挥发、易燃的特性很难避免电池安全事故的发生,所以固态电解质作为安全性能更高的电解液替代产品受到关注。现有的固态电解质按照材料体系可以分为三类:硫化物固态电解质、氧化物固态电解质和聚合物固态电解质。其中,硫化物固态电解质由于具有在室温下既可媲美液态电解质的离子电导率和较易成型致密化的加工特性,也是最有应用前景的固态电解质体系之一。但是,现有的硫化物固态电解质还存在离子电导率不高等问题,硫化物固态电池也有待提高能量密度和循环性能。Traditional liquid lithium batteries are difficult to avoid battery safety accidents due to the volatile and flammable characteristics of the liquid electrolyte itself. Therefore, solid electrolytes have attracted attention as an electrolyte replacement product with higher safety performance. The existing solid electrolytes can be divided into three categories according to the material system: sulfide solid electrolytes, oxide solid electrolytes and polymer solid electrolytes. Among them, the sulfide solid electrolyte is also one of the most promising solid electrolyte systems because of its ionic conductivity comparable to that of liquid electrolytes and the processing characteristics of easier shaping and densification at room temperature. However, the existing sulfide solid electrolytes still have problems such as low ion conductivity, and the sulfide solid state batteries also need to improve the energy density and cycle performance.
发明内容Summary of the invention
鉴于现有技术中存在的问题,本申请的目的在于提供一种硫化物固态电解质片及其制备方法,以提高固态电解质片的电导率和电池的能量密度及循环性能,及含有所述硫化物固态电解质片的电池及装置。In view of the problems existing in the prior art, the purpose of this application is to provide a sulfide solid electrolyte sheet and a preparation method thereof to improve the conductivity of the solid electrolyte sheet and the energy density and cycle performance of the battery, and contain the sulfide Batteries and devices with solid electrolyte sheets.
为了达到上述目的,本申请的第一方面提供了一种硫化物固态电解质片,其包含硫化物电解质材料及掺杂于所述硫化物电解质材料中的硼元素,且所述固态电解质片表面任意位置的硼元素质量浓度B 0与固态电解质片表面距离该位置100μm处的硼元素质量浓度B 100的相对偏差(B 0-B 100)/B 0不超过20%,优选为(B 0-B 100)/B 0不超过10%。 In order to achieve the above objective, the first aspect of the present application provides a sulfide solid electrolyte sheet, which comprises a sulfide electrolyte material and a boron element doped in the sulfide electrolyte material, and the surface of the solid electrolyte sheet is arbitrary The relative deviation (B 0 -B 100 )/B 0 of the boron element mass concentration at the position B 0 and the boron element mass concentration B 100 at a distance of 100 μm from the surface of the solid electrolyte sheet to the position is not more than 20%, preferably (B 0 -B 100 )/B 0 does not exceed 10%.
本申请的第二方面提供了本申请第一方面所述的硫化物固态电解质片的制备方法,包括:The second aspect of the application provides a method for preparing the sulfide solid electrolyte sheet according to the first aspect of the application, including:
获取包含硫化物电解质原料和有机溶剂的反应初混液;Obtain an initial reaction mixture containing sulfide electrolyte raw materials and organic solvents;
获取包含硼酸酯和有机溶剂的改性溶液;Obtain a modified solution containing borate and organic solvent;
将所述反应初混液与所述改性溶液混合,干燥,得到初始产物;Mixing the initial reaction mixture with the modification solution and drying to obtain an initial product;
对所述初始产物进行1次以上后处理,每次所述后处理依次包括研磨、冷压和烧结步骤。The initial product is subjected to more than one post-treatment, and each post-treatment sequentially includes the steps of grinding, cold pressing and sintering.
本申请的第三方面提供了一种全固态锂离子电池,其通过本申请第一方面所述的硫化物固态电解质片或根据本申请第二方面所述的制备方法制备的硫化物固态电解质片制备得到。The third aspect of the application provides an all-solid-state lithium ion battery, which is prepared by the sulfide solid electrolyte sheet according to the first aspect of the application or the sulfide solid electrolyte sheet prepared according to the preparation method according to the second aspect of the application Prepared.
本申请的第四方面提供了一种叠片式全固态锂离子电池,包括正极极片、固态电解质片和负极极片;其中,所述固态电解质片为本申请第一方面所述的硫化物固态电解质片或根据本申请第二方面所述的制备方法制备的硫化物固态电解质片。The fourth aspect of the present application provides a laminated all-solid-state lithium ion battery, including a positive pole piece, a solid electrolyte sheet and a negative pole piece; wherein the solid electrolyte sheet is the sulfide described in the first aspect of the application A solid electrolyte sheet or a sulfide solid electrolyte sheet prepared according to the preparation method described in the second aspect of the application.
本申请的第五方面提供一种装置,包括本申请第三方面所述的全固态锂离 子电池或本申请第四方面所述的叠片式全固态锂离子电池。A fifth aspect of the present application provides a device, including the all-solid-state lithium ion battery described in the third aspect of the present application or the laminated all-solid-state lithium ion battery described in the fourth aspect of the present application.
相对于现有技术,本申请至少包括如下所述的有益效果:Compared with the prior art, this application includes at least the following beneficial effects:
本申请的实施方式中,以硼酸酯作为掺杂原料对硫化物固态电解质进行改性,B元素掺杂可以降低阴离子对锂离子的束缚作用,提升锂离子的传输能力;O元素部分掺杂取代S元素既可以产生混合阴离子效应从而提升锂离子电导率,又可以抑制氧化物阴极与硫化物电解质界面空间电荷层的形成,降低界面阻抗;而掺杂过程中所引入的硼酸酯作为路易斯酸,具有2P空轨道,可与硫化物电解质材料的电子给体形成络合,促进硫化物电解质材料与掺杂材料充分反应,提高反应产物的掺杂均匀度和电导率。In the embodiment of the application, borate is used as the doping raw material to modify the sulfide solid electrolyte. The doping of B element can reduce the binding effect of anions on lithium ions and improve the transmission capacity of lithium ions; O element is partially doped Substitution of S element can not only produce mixed anion effect to improve lithium ion conductivity, but also inhibit the formation of space charge layer at the interface between oxide cathode and sulfide electrolyte, and reduce the interface impedance; and the borate introduced in the doping process acts as Lewis Acid, with 2P empty orbital, can form a complex with the electron donor of the sulfide electrolyte material, promote the full reaction of the sulfide electrolyte material and the doping material, and improve the doping uniformity and conductivity of the reaction product.
发明人认为,在固态电解质的掺杂改性过程中,如将硫化物电解质原料与需要掺杂的阳离子或阴离子的无机化合物(例如硫化硼)直接混合、热处理,由于无机颗粒之间的固固接触问题,这种混合方式很难达到均匀的分散效果,而且在原料混合和热处理过程中还易导致杂相生成。而本申请则利用了硼酸酯在溶剂中形成均匀分散的溶液的性质,实现了电解质原料与需要掺杂的硼酸酯之间的充分混合。并且,硼酸酯在硫化物电解质的成相温度下可以完全分解,从而减少了杂质的引入或反应物残余,使制得的硫化物固态电解质的离子电导率得到显著的提升,进而有利于全固态锂离子电池能量密度的发挥。The inventor believes that in the doping modification process of the solid electrolyte, if the raw material of the sulfide electrolyte is directly mixed with the cation or anion inorganic compound (such as boron sulfide) that needs to be doped, the heat treatment is caused due to the solid state between the inorganic particles. For contact problems, this mixing method is difficult to achieve a uniform dispersion effect, and it is easy to cause the formation of impurity phases during raw material mixing and heat treatment. However, the present application utilizes the property of borate to form a uniformly dispersed solution in the solvent to realize the full mixing of the electrolyte raw materials and the borate to be doped. In addition, the borate can be completely decomposed at the phase forming temperature of the sulfide electrolyte, thereby reducing the introduction of impurities or residual reactants, so that the ionic conductivity of the prepared sulfide solid electrolyte is significantly improved, which is beneficial to the complete The energy density of solid-state lithium-ion batteries is exerted.
进一步地,发明人还认为,在制备硫化物固态电解质的热处理过程中,由于溶剂的挥发和有机硼酸酯的分解会导致电解质片结构破坏、以及颗粒与颗粒间的接触不良,从而影响掺杂元素在固态电解质内部的扩散过程。因此,本申请通过多次研磨、冷压和烧结处理的方式,在反复的压片和烧结过程中实现了改性元素在电解质材料中的充分扩散和均匀分布,最终得到了硼元素均匀掺杂的硫化物电解质片。Further, the inventor also believes that during the heat treatment process for preparing the sulfide solid electrolyte, the volatilization of the solvent and the decomposition of the organic borate will cause damage to the structure of the electrolyte sheet and poor contact between particles, thereby affecting doping. The diffusion process of elements in the solid electrolyte. Therefore, the present application achieves sufficient diffusion and uniform distribution of the modified element in the electrolyte material through repeated grinding, cold pressing and sintering processes, and finally uniform doping of boron element Sulfide electrolyte sheet.
因此,本申请实施方式的固态电解质片中,一方面由于硼元素的引入,有效降低了阴离子对锂离子的束缚作用,提升了锂离子的传输能力;另一方面, 由于硼元素在固态电解质片中呈均匀分布,不但提高了固态电解质片的掺杂均匀性和电导率,还能显著改善固态电解质片的表面粗糙度,利于锂离子在电解质片和锂金属阳极界面之间的扩散过程,从而降低界面阻抗,并改善电池的循环性能。Therefore, in the solid electrolyte sheet of the embodiment of the present application, on the one hand, due to the introduction of boron element, the binding effect of anions on lithium ions is effectively reduced, and the transmission capacity of lithium ions is improved; on the other hand, due to the boron element in the solid electrolyte sheet It not only improves the doping uniformity and conductivity of the solid electrolyte sheet, but also significantly improves the surface roughness of the solid electrolyte sheet, which is beneficial to the diffusion process of lithium ions at the interface between the electrolyte sheet and the lithium metal anode. Reduce interface impedance and improve battery cycle performance.
附图说明Description of the drawings
图1是根据本申请实施方式的固态电解质的XRD测试图谱;Fig. 1 is an XRD test pattern of a solid electrolyte according to an embodiment of the present application;
图2是根据本申请实施方式的固态电解质的Raman测试结果图;2 is a graph of Raman test results of a solid electrolyte according to an embodiment of the present application;
图3是根据本申请实施方式的固态电解质的元素分布测试结果图;FIG. 3 is a graph of element distribution test results of a solid electrolyte according to an embodiment of the present application;
图4是根据本申请实施方式的固态电解质片的表面粗糙度测试的光学显微镜图;4 is an optical microscope diagram of the surface roughness test of a solid electrolyte sheet according to an embodiment of the present application;
图5是根据本申请实施方式的装置的示意图。Fig. 5 is a schematic diagram of a device according to an embodiment of the present application.
具体实施方式Detailed ways
本申请的实施方式所提供的硫化物固态电解质片,包含硫化物电解质材料及掺杂于所述硫化物电解质材料中的硼元素,且所述硫化物电解质片表面任意位置的硼元素质量浓度B 0与硫化物电解质片表面距离该位置100μm处的硼元素质量浓度B 100的相对偏差(B 0-B 100)/B 0不超过20%。 The sulfide solid electrolyte sheet provided by the embodiment of the present application includes a sulfide electrolyte material and a boron element doped in the sulfide electrolyte material, and the mass concentration of boron element at any position on the surface of the sulfide electrolyte sheet is B 0 with a surface concentration of sulfide electrolyte plate B 100 relative deviation from the mass of boron element 100μm at the location (B 0 -B 100) / B 0 not exceed 20%.
根据本申请的一些实施方式,相对偏差(B 0-B 100)/B 0不超过10%,例如为不超过9%、8%、7%、6%、5%以及它们之间的任意值,优选不超过8%。 According to some embodiments of the present application, the relative deviation (B 0 -B 100 )/B 0 does not exceed 10%, for example, does not exceed 9%, 8%, 7%, 6%, 5%, and any value in between , Preferably not more than 8%.
在本申请的实施方式中,向硫化物电解质中引入了硼元素,硼元素可有效降低阴离子对锂离子的束缚作用,提升锂离子的传输能力;并且,硼元素在硫化物固态电解质片表面呈均匀分布,不但提高了固态电解质片的掺杂均匀性和电导率,还能显著改善固态电解质片的表面粗糙度,利于锂离子在固态电解质 片和锂金属阳极界面之间的扩散过程,从而降低界面阻抗并改善电池的循环性能。In the embodiment of the present application, boron is introduced into the sulfide electrolyte, which can effectively reduce the binding effect of anions on lithium ions and improve the transmission capacity of lithium ions; and, boron is present on the surface of the sulfide solid electrolyte sheet. Uniform distribution not only improves the doping uniformity and conductivity of the solid electrolyte sheet, but also significantly improves the surface roughness of the solid electrolyte sheet, which facilitates the diffusion process of lithium ions between the solid electrolyte sheet and the lithium metal anode interface, thereby reducing Interface impedance and improve battery cycle performance.
根据本申请的一些实施方式,所述固态电解质片的表面粗糙度为3μm~15μm,例如为3μm、4μm、5μm、6μm、7μm、8μm、9μm、10μm、11μm、12μm、13μm、14μm以及它们之间的任意值,优选为3μm~10μm。According to some embodiments of the application, the surface roughness of the solid electrolyte sheet is 3 μm to 15 μm, for example, 3 μm, 4 μm, 5 μm, 6 μm, 7 μm, 8 μm, 9 μm, 10 μm, 11 μm, 12 μm, 13 μm, 14 μm, and some of them. The arbitrary value between is preferably 3 μm to 10 μm.
根据本申请的优选实施方式,所述硫化物固态电解质片的表面粗糙度为3μm~6μm。According to a preferred embodiment of the present application, the surface roughness of the sulfide solid electrolyte sheet is 3 μm to 6 μm.
本申请的实施方式中,电解质片的表面粗糙度是指:将电解质片放置在高精度光学显微镜下进行观测,在3D成像模式下得到电解质片在200*300μm 2面积内的表面高度分布信息,通过统计电解质片最大表面高度差值即得到表面粗糙度。 In the embodiment of the application, the surface roughness of the electrolyte sheet refers to: placing the electrolyte sheet under a high-precision optical microscope for observation, and obtaining the surface height distribution information of the electrolyte sheet in an area of 200*300μm 2 in 3D imaging mode. The surface roughness can be obtained by counting the difference in the maximum surface height of the electrolyte sheet.
电解质片的表面粗糙度的改善利于锂离子在电解质片和锂金属阳极界面之间的扩散过程,从而降低界面阻抗和改善电池的循环性能。电解质片表面粗糙度过大时,其表面形貌凹凸不平,而锂金属阳极表面平滑,因此电解质与锂金属的界面接触非常不充分,导致锂离子的界面迁移比较困难。改善电解质表面粗糙度有助于增加其与锂金属的接触位点,从而促进锂离子在界面的传输并降低界面极化。但在特定的工艺条件下,电解质材料组成和形貌对于表面粗糙度的影响是有极限的,要进一步降低表面粗糙度需要在加压工艺和模具方面进行改进,因此在目前的工艺条件下,表面粗糙度范围为3μm~15μm,优选3μm~10μm。The improvement of the surface roughness of the electrolyte sheet facilitates the diffusion process of lithium ions at the interface between the electrolyte sheet and the lithium metal anode, thereby reducing the interface impedance and improving the cycle performance of the battery. When the surface roughness of the electrolyte sheet is too large, its surface morphology is uneven, while the surface of the lithium metal anode is smooth, so the interface contact between the electrolyte and the lithium metal is very insufficient, which makes the interface migration of lithium ions more difficult. Improving the surface roughness of the electrolyte helps increase its contact points with lithium metal, thereby promoting the transport of lithium ions at the interface and reducing the interface polarization. However, under certain process conditions, the composition and morphology of the electrolyte material have a limit to the surface roughness. To further reduce the surface roughness, it is necessary to improve the press process and the mold. Therefore, under the current process conditions, The surface roughness ranges from 3 μm to 15 μm, preferably 3 μm to 10 μm.
根据本申请的一些实施方式,所述固态电解质片的电导率为1.6mS/cm~2.9mS/cm,例如为1.6mS/cm、1.7mS/cm、1.9mS/cm、2.1mS/cm、2.3mS/cm、2.4mS/cm、2.5mS/cm、2.6mS/cm、2.7mS/cm、2.8mS/cm、2.9mS/cm以及它们之间的任意值,优选为2.1mS/cm~2.8mS/cm。According to some embodiments of the present application, the electrical conductivity of the solid electrolyte sheet is 1.6 mS/cm to 2.9 mS/cm, for example 1.6 mS/cm, 1.7 mS/cm, 1.9 mS/cm, 2.1 mS/cm, 2.3 mS/cm, 2.4mS/cm, 2.5mS/cm, 2.6mS/cm, 2.7mS/cm, 2.8mS/cm, 2.9mS/cm and any value between them, preferably 2.1mS/cm~2.8mS /cm.
电解质电导率受掺杂硼元素在电解质片中的含量和分布均匀性影响,当含 量一定时,改善硼元素掺杂均匀性有利于提高电导率,如果硼元素分布不均,则必然存在部分区域硼元素掺杂量过低以及部分区域掺杂量过高,一方面达不到理想的结构改性效果,另一方面也会影响锂离子局部分布和迁移能力,电导率的提升效果不佳。此外,通过掺杂少量元素和改善元素分布均匀性的方式对于电解质本体结构的影响是有限的,其能达到的电导率提升效果也有一定范围,所述改善条件下电导率的范围是1.7mS/cm~2.8mS/cm,优选范围是2.1mS/cm~2.8mS/cm。Electrolyte conductivity is affected by the content and uniformity of distribution of doped boron in the electrolyte sheet. When the content is constant, improving the uniformity of boron doping is beneficial to increase the conductivity. If the distribution of boron is uneven, there must be some areas Too low doping amount of boron element and too high doping amount in some areas, on the one hand, can not achieve the ideal structure modification effect, on the other hand, it will also affect the local distribution and migration of lithium ions, and the improvement effect of conductivity is not good. In addition, the influence of doping a small amount of elements and improving the uniformity of element distribution on the electrolyte body structure is limited, and the conductivity improvement effect that can be achieved has a certain range. The conductivity range under the improved condition is 1.7mS/ cm~2.8mS/cm, the preferred range is 2.1mS/cm~2.8mS/cm.
根据本申请的一些实施方式,所述电解质片中的硼元素的质量百分含量为0.5%~10%,例如为1%、2%、3%、4%、5%、6%、7%、8%、9%、10%以及它们之间的任意值,优选为3%~7%。According to some embodiments of the present application, the mass percentage of the boron element in the electrolyte sheet is 0.5%-10%, for example, 1%, 2%, 3%, 4%, 5%, 6%, 7% , 8%, 9%, 10% and any value between them, preferably 3% to 7%.
当电解质片中的硼元素含量过低时,硼元素的掺杂对电解质结构的影响较小,虽然也可对电导率有一定的提升,但该种提升效果不显著,且过低的硼元素含量会导致浓度测试误差增大,因而测得的浓度偏差也会较大。当电解质片中的硼元素含量过高时,易出现局部元素富集的问题,不利于实现均匀的改性结果,且过高的硼元素掺入量会降低含锂离子在电解质片中的相对含量,不利于提升电解质片的电导率和电池性能。When the content of boron in the electrolyte sheet is too low, the doping of boron has little effect on the electrolyte structure. Although it can also improve the conductivity to a certain extent, the effect of this improvement is not significant, and the boron is too low The content will cause the concentration test error to increase, so the measured concentration deviation will be larger. When the content of boron in the electrolyte sheet is too high, the problem of local element enrichment is likely to occur, which is not conducive to achieving uniform modification results, and too high doping of boron element will reduce the relative content of lithium ions in the electrolyte sheet. The content is not conducive to improving the conductivity of the electrolyte sheet and battery performance.
根据本申请的一些实施方式,所述硫化物电解质材料包括Li 2S·P 2S 5、Li 2S·GeS 2、Li 2S·SiS 2、Li 6PS 5X和Li 7P 3S 11中的一种或几种,其中,X选自Cl、Br、I中的至少一种,优选为Cl。 According to some embodiments of the present application, the sulfide electrolyte material includes Li 2 S·P 2 S 5 , Li 2 S·GeS 2 , Li 2 S·SiS 2 , Li 6 PS 5 X, and Li 7 P 3 S 11 One or more of them, wherein X is selected from at least one of Cl, Br, and I, preferably Cl.
采用不同的硫化物电解质材料,均能通过硼元素的掺杂以及电解质片表面硼元素的分布均匀性改善达到提高掺杂后的固态电解质的电导率和表面均一性的效果,因而,本申请实施方式的硫化物固态电解质片中,所包含的硫化物电解质材料种类不受限制。The use of different sulfide electrolyte materials can achieve the effect of improving the conductivity and surface uniformity of the doped solid electrolyte through the doping of boron and the improvement of the uniformity of the distribution of boron on the surface of the electrolyte sheet. Therefore, this application is implemented In the sulfide solid electrolyte sheet of the method, the type of sulfide electrolyte material contained is not limited.
在本申请第二方面,本申请的实施方式还提供上述硫化物固态电解质片的制备方法,包括:In the second aspect of the present application, the embodiments of the present application also provide a method for preparing the above-mentioned sulfide solid electrolyte sheet, including:
获取包含硫化物硫化物电解质原料和有机溶剂的反应初混液;Obtain an initial reaction mixture containing sulfide sulfide electrolyte raw material and organic solvent;
获取包含硼酸酯和有机溶剂的改性溶液;Obtain a modified solution containing borate and organic solvent;
将所述反应初混液与所述改性溶液混合,干燥,得到初始产物;Mixing the initial reaction mixture with the modification solution and drying to obtain an initial product;
对所述初始产物进行1次以上后处理,每次所述后处理依次包括研磨、冷压和烧结步骤。The initial product is subjected to more than one post-treatment, and each post-treatment sequentially includes the steps of grinding, cold pressing and sintering.
本申请实施方式所提供的制备方法中,以硼酸酯作为掺杂原料,得到硼、氧共掺杂的固态电解质,其中,硼元素掺杂可以降低阴离子对锂离子的束缚作用,提升锂离子的传输能力;氧元素部分掺杂取代硫元素既可以产生混合阴离子效应从而提升锂离子电导率,又可以抑制氧化物阴极与硫化物电解质界面空间电荷层的形成,降低界面阻抗;而掺杂过程中所引入的硼酸酯作为路易斯酸,具有2P空轨道,可与硫化物固态电解质电子给体形成络合,促进硫化物固态电解质与掺杂材料充分反应,从而提高反应产物的掺杂均匀性和电导率。In the preparation method provided by the embodiment of the present application, borate is used as the doping material to obtain a solid electrolyte co-doped with boron and oxygen, wherein the doping of boron element can reduce the binding effect of anions on lithium ions, and improve lithium ions. Partial doping of oxygen element to replace sulfur element can not only produce mixed anion effect to improve lithium ion conductivity, but also inhibit the formation of space charge layer at the interface between oxide cathode and sulfide electrolyte, and reduce interface impedance; and the doping process As a Lewis acid, the borate ester introduced in the sulfide has a 2P empty orbital, which can form a complex with the sulfide solid electrolyte electron donor to promote the full reaction of the sulfide solid electrolyte with the doping material, thereby improving the doping uniformity of the reaction product And conductivity.
上述方法利用了硼酸酯在合适的溶剂中可形成均匀分散的溶液的性质,在固态电解质的掺杂改性过程中,实现了电解质原料与需要掺杂的硼酸酯之间的充分混合。并且,DSC-TG测试显示,硼酸酯在硫化物成相温度以下区间存在吸热分解峰和失重曲线,也就是说,硼酸酯在硫化物电解质的成相温度下可以完全分解,从而减少了杂质的引入或反应物残余,使得最终制得的硫化物电解质离子电导率有明显提升。The above method utilizes the property that the borate can form a uniformly dispersed solution in a suitable solvent. During the doping modification process of the solid electrolyte, the electrolyte raw material and the borate to be doped are fully mixed. In addition, the DSC-TG test showed that the borate has an endothermic decomposition peak and a weight loss curve in the range below the sulfide phase formation temperature, that is to say, the borate can be completely decomposed at the phase formation temperature of the sulfide electrolyte, thereby reducing The introduction of impurities or residual reactants makes the final sulfide electrolyte ionic conductivity significantly improved.
此外,上述方法还解决了热处理过程中由于溶剂的挥发和有机硼酸酯的分解导致电解质片结构破坏、颗粒与颗粒间的接触不良,从而影响掺杂元素在固态电解质内部扩散过程的问题。通过多次研磨、冷压和烧结,实现了硼元素在电解质中的均匀分布,使得固态电解质的掺杂均匀性和电导率得到提高,且固态电解质片表面的粗糙度得到显著改善,可制备得到表面形貌均一的固态电解质片,从而促进锂离子在固态电解质片和锂金属阳极界面的扩散过程,降低界面阻抗并改善电池的循环性能。In addition, the above method also solves the problem that the electrolyte sheet structure is damaged due to the volatilization of the solvent and the decomposition of the organic borate during the heat treatment, and the poor contact between the particles and the particles, thereby affecting the diffusion process of the doping elements in the solid electrolyte. Through multiple grinding, cold pressing and sintering, the boron element is uniformly distributed in the electrolyte, so that the doping uniformity and conductivity of the solid electrolyte are improved, and the surface roughness of the solid electrolyte sheet is significantly improved. The solid electrolyte sheet with uniform surface morphology promotes the diffusion process of lithium ions at the interface between the solid electrolyte sheet and the lithium metal anode, reduces the interface impedance and improves the cycle performance of the battery.
根据本申请的优选实施方式,将硫化物电解质原料分散于有机溶剂中,形成反应初混液。According to a preferred embodiment of the present application, the sulfide electrolyte raw material is dispersed in an organic solvent to form an initial reaction mixture.
根据本申请的优选实施方式,将硼酸酯分散于有机溶剂中,形成改性溶液。According to a preferred embodiment of the present application, the borate is dispersed in an organic solvent to form a modified solution.
根据本申请的一些实施方式,所述硼酸酯具有式(I)所示的结构:According to some embodiments of the present application, the borate has a structure represented by formula (I):
Figure PCTCN2020099496-appb-000001
其中,R选自C1~C4烷基。
Figure PCTCN2020099496-appb-000001
Wherein, R is selected from C1-C4 alkyl.
值得说明的是,如硼酸酯结构中取代的烷基碳原子数目增加,仅会对硼酸酯在有机溶剂中的溶解度略有影响,但相比于固固接触的制备方法,所获得的固态电解质的电导率性能仍然保持较大的优势。It is worth noting that if the number of substituted alkyl carbon atoms in the borate structure increases, it will only slightly affect the solubility of the borate in organic solvents, but compared to the solid-solid contact preparation method, the obtained The conductivity performance of the solid electrolyte still maintains a greater advantage.
根据本申请的一些优选方式,所述硼酸酯选自(I-1)至(I-4)结构中的一种或几种:According to some preferred modes of this application, the borate is selected from one or more of the structures (I-1) to (I-4):
Figure PCTCN2020099496-appb-000002
Figure PCTCN2020099496-appb-000002
根据本申请的一些实施方式,所述反应初混液与所述改性溶液混合后进行充分分散,所述充分分散的时间为5~20小时。According to some embodiments of the present application, the initial reaction mixture is mixed with the modified solution and then fully dispersed, and the time for the fully dispersed is 5-20 hours.
根据本申请的一些实施方式,用于分散硫化物电解质材料的有机溶剂和用于分散硼酸酯的有机溶剂可独立选自四氢呋喃、乙腈、吡啶、甲醇、乙醇、丙醇、异丙醇、丁醇、丙酸丙酯、丙酸丁酯、丁酸丁酯中的一种或几种。According to some embodiments of the present application, the organic solvent used to disperse the sulfide electrolyte material and the organic solvent used to disperse the borate may be independently selected from tetrahydrofuran, acetonitrile, pyridine, methanol, ethanol, propanol, isopropanol, butane One or more of alcohol, propyl propionate, butyl propionate, and butyl butyrate.
根据本申请的一些实施方式,将硫化物电解质原料分散于有机溶剂中、将硼酸酯分散于有机溶剂中时,硫化物电解质原料与有机溶剂共混的体积比例可以为1:1~1:10,硼酸酯与有机溶剂共混的体积比例可以为1:1~1:10。According to some embodiments of the present application, when the sulfide electrolyte raw material is dispersed in an organic solvent and the borate is dispersed in an organic solvent, the volume ratio of the sulfide electrolyte raw material and the organic solvent can be 1:1 to 1: 10. The volume ratio of borate and organic solvent blending can be 1:1 to 1:10.
根据本申请的一些实施方式,将反应初混液与改性溶液进行混合时,所采用的共混的方式可以是球磨方式。According to some embodiments of the present application, when mixing the initial reaction mixture with the modifying solution, the blending method used may be a ball milling method.
根据本申请的一些实施方式,所述干燥的过程需在真空度小于-90kPa的真空环境下进行,干燥的温度为100℃~120℃。According to some embodiments of the present application, the drying process needs to be performed in a vacuum environment with a vacuum degree of less than -90 kPa, and the drying temperature is 100°C to 120°C.
根据本申请的优选实施方式,所述后处理的次数为2~3次。According to a preferred embodiment of the present application, the number of post-treatments is 2 to 3 times.
随着后处理次数的增加,掺杂后的电解质材料经过多次的研磨、压片和烧结,多种元素在体相材料中的分布趋于均匀,表面粗糙度和界面阻抗得到降低。但是,过于多次的高温烧结也可能导致电解质发生结构相变,影响电导率的提升幅度。With the increase of the number of post-treatments, the doped electrolyte material undergoes multiple grinding, tableting and sintering, the distribution of various elements in the bulk material tends to be uniform, and the surface roughness and interface impedance are reduced. However, too many high-temperature sintering may also cause structural phase changes in the electrolyte, which affects the increase in conductivity.
根据本申请的一些实施方式,所述烧结的温度为200℃~700℃,例如为200℃、300℃、400℃、500℃、550℃、600℃以及它们之间的任意值,优选为200℃~600℃。According to some embodiments of the present application, the sintering temperature is 200°C to 700°C, such as 200°C, 300°C, 400°C, 500°C, 550°C, 600°C and any value in between, preferably 200°C. ℃~600℃.
根据本申请的优选实施方式,所述烧结的温度为200℃~400℃。According to a preferred embodiment of the present application, the sintering temperature is 200°C to 400°C.
烧结温度可对制得的固态电解质和电池的性能产生影响。具体来说,烧结温度应与硫化物的成相温度和硼酸酯的分解温度相匹配,热处理温度过低,则无法得到特定的电解质晶相结构且硼酸酯未完全分解,电解质电导率虽有所增加,但由于有效掺B量极低,导致电导率增加幅度较小;如果烧结温度过高,则电解质自身易发生相变导致杂相生成,电导率和容量发挥增加的幅度也会减小。The sintering temperature can affect the performance of the prepared solid electrolyte and battery. Specifically, the sintering temperature should match the phase formation temperature of the sulfide and the decomposition temperature of the borate. If the heat treatment temperature is too low, the specific electrolyte crystal structure cannot be obtained and the borate is not completely decomposed, although the electrolyte conductivity However, the effective amount of B doping is extremely low, resulting in a small increase in conductivity; if the sintering temperature is too high, the electrolyte itself is prone to phase change and impurity generation, and the increase in conductivity and capacity will also decrease. small.
根据本申请的优选实施方式,每次后处理中的烧结温度随着后处理次数的增加而升高。According to a preferred embodiment of the present application, the sintering temperature in each post-treatment increases as the number of post-treatments increases.
下面以三次后处理为例,说明烧结温度成梯度上升的技术效果。The following takes three post-treatments as an example to illustrate the technical effect of the sintering temperature gradient increase.
在首次后处理的烧结步骤中,烧结温度不宜过高。如第一次烧结温度过高,则溶剂的挥发、硼酸酯的分解和硫化物电解质的成相过程集中在此次烧结步骤中进行,其中溶剂的挥发和硼酸酯的分解这两个过程中不断发生体积变化导致压实的电解质块体变成多孔疏松结构、颗粒与颗粒间的接触不良,不利于硼元素在电解质体相中的扩散过程,使得电解质表面成分的差异增大、均匀性降低, 而且长时间的高温烧结也会导致电解质杂相生成以及电导率降低,进一步影响电池的界面阻抗和循环性能。In the sintering step of the first post-treatment, the sintering temperature should not be too high. If the first sintering temperature is too high, the volatilization of the solvent, the decomposition of the borate and the phase formation of the sulfide electrolyte are concentrated in this sintering step, and the two processes of volatilization of the solvent and the decomposition of the borate The constant volume change in the electrolyte causes the compacted electrolyte block to become a porous and loose structure, and the particle-to-particle contact is not good, which is not conducive to the diffusion process of the boron element in the electrolyte phase, which makes the difference and uniformity of the electrolyte surface composition increase. In addition, long-term high-temperature sintering will also lead to the formation of electrolyte impurities and the decrease of conductivity, which will further affect the interface impedance and cycle performance of the battery.
根据本申请的优选实施方式,第一次后处理的烧结温度为200℃~700℃,例如为200℃、300℃、400℃、500℃、550℃、600℃以及它们之间的任意值,优选为200℃~400℃。According to a preferred embodiment of the present application, the sintering temperature of the first post-treatment is 200°C to 700°C, for example, 200°C, 300°C, 400°C, 500°C, 550°C, 600°C and any value in between, Preferably it is 200 to 400 degreeC.
在第二次后处理的烧结步骤中,则需要选择适中的烧结温度,最好高于第一的烧结温度。如第二次烧结温度过低,硼酸酯无法分解,电解质的成相过程和硼元素改性过程未完全、或者都只能聚集到第三次后处理过程中完成,由于硼酸酯分解的影响,电解质片仍无法保持良好的界面接触,因此不利于硼元素的均匀分布和表面性能改善。如第二次烧结温度过高,电解质的成相过程和硼元素改性过程则集中至第二次后处理中进行,也不利于均匀改性效果,且过高的热处理温度对于电解质的电导率也有不良影响。In the sintering step of the second post-treatment, a moderate sintering temperature needs to be selected, preferably higher than the first sintering temperature. If the second sintering temperature is too low, the borate cannot be decomposed, the phase formation process of the electrolyte and the boron element modification process are not complete, or they can only be assembled in the third post-treatment process. As a result, the electrolyte sheet still cannot maintain good interface contact, which is not conducive to the uniform distribution of boron and the improvement of surface properties. If the second sintering temperature is too high, the phase formation process of the electrolyte and the boron element modification process will be concentrated in the second post-treatment, which is not conducive to the uniform modification effect, and the too high heat treatment temperature has an effect on the conductivity of the electrolyte. There are also adverse effects.
根据本申请的优选实施方式,第一次后处理的烧结温度为200℃~700℃,例如为200℃、300℃、400℃、500℃、550℃、600℃以及它们之间的任意值,优选为300℃~500℃。According to a preferred embodiment of the present application, the sintering temperature of the first post-treatment is 200°C to 700°C, for example, 200°C, 300°C, 400°C, 500°C, 550°C, 600°C and any value in between, Preferably it is 300 to 500 degreeC.
根据本申请的优选实施方式,所述第二次后处理的烧结温度高于所述第一次后处理的烧结温度0~400℃,优选100~200℃。According to a preferred embodiment of the present application, the sintering temperature of the second post-treatment is higher than the sintering temperature of the first post-treatment by 0-400°C, preferably 100-200°C.
综上,在三次后处理过程中,依次采取低、中、高温三种温区的烧结温度,有利于将电解质改性过程中的不同反应区分开来,从而制备得到硼元素均匀分布的电解质片,由于电解质片表面成分和形貌的高度均一性,其表面粗糙度和离子电导率均有明显改善,从而提升固态电池的界面性能和循环性能。To sum up, in the three post-treatment processes, the sintering temperature of three temperature zones, low, medium and high temperature is adopted in sequence, which is beneficial to distinguish the different reactions in the electrolyte modification process, so as to prepare an electrolyte sheet with uniform boron element distribution. , Due to the high uniformity of the surface composition and morphology of the electrolyte sheet, its surface roughness and ionic conductivity are significantly improved, thereby improving the interface performance and cycle performance of the solid-state battery.
根据本申请的一些实施方式,所述冷压是指在50MPa~200MPa冷压压力下冷压成型。According to some embodiments of the present application, the cold pressing refers to cold pressing under a cold pressure of 50 MPa to 200 MPa.
根据本申请的一些实施方式,所述每一次烧结的时间为0.5~5小时。According to some embodiments of the present application, the time for each sintering is 0.5-5 hours.
根据本申请的一些实施方式,所述热处理的气氛可以为氩气、氮气等惰性 气氛。According to some embodiments of the present application, the heat treatment atmosphere may be an inert atmosphere such as argon and nitrogen.
在本申请的第三方面,本申请的实施方式还提供了一种通过本申请实施方式的固态电解质片制备的全固态锂离子电池,所述全固态锂离子电池可以为各种形式的全固态锂离子电池。In the third aspect of the present application, the embodiments of the present application also provide an all-solid-state lithium-ion battery prepared by the solid-state electrolyte sheet of the embodiments of the present application. The all-solid-state lithium-ion battery can be all-solid-state in various forms. Lithium Ion Battery.
在本申请的第四方面,本申请的实施方式还提供了一种叠片式全固态锂离子电池,包括正极极片、固态电解质片和负极极片;其中,所述固态电解质片为申请实施方式的固态电解质片。In the fourth aspect of the present application, the embodiments of the present application also provide a laminated all-solid-state lithium-ion battery, including a positive pole piece, a solid electrolyte sheet, and a negative pole piece; wherein, the solid electrolyte sheet is an application implementation Way of solid electrolyte sheet.
根据本申请的一些实施方式,所述正极极片通过包含固态电解质片、正极活性材料和导电剂的原料制备得到;其中,所述固态电解质片为申请实施方式的固态电解质片。According to some embodiments of the present application, the positive pole piece is prepared from raw materials comprising a solid electrolyte sheet, a positive electrode active material, and a conductive agent; wherein, the solid electrolyte sheet is the solid electrolyte sheet according to the application embodiment.
根据本申请的一些实施方式,所述叠片式全固态锂离子电池的制备方法包括如下步骤:According to some embodiments of the present application, the preparation method of the laminated all-solid-state lithium ion battery includes the following steps:
S1.制备正极极片;S1. Preparation of positive pole pieces;
S2.按照本申请第二方面所述的制备方法制备硫化物固态电解质片;S2. Prepare a sulfide solid electrolyte sheet according to the preparation method described in the second aspect of this application;
S3.制备负极极片;S3. Preparation of negative pole piece;
S4.将正极极片、固态电解质片和负极极片依次层叠,压制得到所述全固态锂离子电池。S4. Laminating the positive pole piece, the solid electrolyte sheet and the negative pole piece in sequence, and pressing to obtain the all-solid lithium ion battery.
根据本申请的优选实施方式,所述步骤S1包括:According to a preferred embodiment of the present application, the step S1 includes:
按照本申请第二方面所述的制备方法制备硫化物固态电解质片;Preparing a sulfide solid electrolyte sheet according to the preparation method described in the second aspect of the present application;
将所述硫化物固态电解质片与正极活性材料和导电剂混合研磨,得到正极粉料;Mixing and grinding the sulfide solid electrolyte sheet with a positive electrode active material and a conductive agent to obtain a positive electrode powder;
将所述正极粉料分散在正极集流体铝箔表面,冷压得到所述正极极片。The positive electrode powder is dispersed on the surface of the positive electrode current collector aluminum foil and cold pressed to obtain the positive electrode pole piece.
将正极极片、固态电解质片、负极极片分别按所需尺寸进行切片,将切片后的正极极片、固态电解质片、负极极片按中心对齐、依次堆叠成夹心层单元,将夹心层单元在一定温度下加压复合在一起,得到全固态锂离子电池的电芯; 将电芯冷压后置于外包装中封装成型,即得到全固态锂离子电池,其包括正极极片、负极极片、以及间隔设于正极极片和负极极片之间的固态电解质片。The positive pole piece, solid electrolyte sheet, and negative pole piece are respectively sliced according to the required size, and the sliced positive pole piece, solid electrolyte sheet, and negative pole piece are aligned in the center and sequentially stacked into a sandwich layer unit, and the sandwich layer unit Press and compound together at a certain temperature to obtain the battery cell of the all-solid-state lithium-ion battery; cold-press the battery cell and place it in an outer package to form an all-solid-state lithium-ion battery, which includes a positive pole piece and a negative pole Sheet and solid electrolyte sheet spaced between the positive pole piece and the negative pole piece.
在本申请的第五方面,本申请的实施方式还提供了一种装置,包括本申请第三方面实施方式所述的全固态锂离子电池或本申请第四方面实施方式所述的叠片式全固态锂离子电池。In the fifth aspect of the present application, the embodiments of the present application also provide a device, including the all-solid-state lithium ion battery described in the third aspect of the present application or the laminated type described in the fourth aspect of the present application. All solid-state lithium-ion battery.
根据本申请的优选实施方式,所述全固态锂离子电池或叠片式全固态锂离子电池可以用作装置的电源,也可以用作所述装置的能量存储单元。本申请的装置采用了本申请所提供的全固态锂离子电池或叠片式全固态锂离子电池,因此至少具有与所述全固态锂离子电池或叠片式全固态锂离子电池相同的优势。According to a preferred embodiment of the present application, the all-solid-state lithium-ion battery or laminated all-solid-state lithium-ion battery can be used as the power source of the device, and can also be used as the energy storage unit of the device. The device of the present application adopts the all-solid-state lithium-ion battery or laminated all-solid-state lithium-ion battery provided in this application, and therefore has at least the same advantages as the all-solid-state lithium-ion battery or the laminated all-solid-state lithium-ion battery.
所述装置可以但不限于是移动设备(例如手机、笔记本电脑等)、电动车辆(例如纯电动车、混合动力电动车、插电式混合动力电动车、电动自行车、电动踏板车、电动高尔夫球车、电动卡车等)、电气列车、船舶及卫星、储能系统等。The device can be, but is not limited to, mobile devices (such as mobile phones, laptop computers, etc.), electric vehicles (such as pure electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, electric bicycles, electric scooters, electric golf Vehicles, electric trucks, etc.), electric trains, ships and satellites, energy storage systems, etc.
图5是作为一个示例的装置。该装置为纯电动车、混合动力电动车、或插电式混合动力电动车等。为了满足该装置对电池的高功率和高能量密度的需求,可以采用电池包或电池模块。Figure 5 is a device as an example. The device is a pure electric vehicle, a hybrid electric vehicle, or a plug-in hybrid electric vehicle. In order to meet the requirements of the device for high power and high energy density of the battery, a battery pack or battery module can be used.
根据本申请的具体实施例,所述装置还可以是手机、平板电脑、笔记本电脑等。该装置通常要求轻薄化,可以采用本申请实施方式的电池作为电源。According to specific embodiments of the present application, the device may also be a mobile phone, a tablet computer, a notebook computer, etc. The device is generally required to be light and thin, and the battery of the embodiment of the present application can be used as a power source.
下面结合具体实施例,进一步阐述本申请。应理解,这些实施例仅用于说明本申请而不用于限制本申请的范围。The application will be further explained below in conjunction with specific embodiments. It should be understood that these embodiments are only used to illustrate the application and not to limit the scope of the application.
固态电解质片的制备Preparation of solid electrolyte sheet
将硫化物电解质原料分散在吡啶内,形成反应初混液;将式(I-1)所示的硼酸酯分散在吡啶内,形成改性溶液;将反应初混液与改性溶液混合后,通过充分分散,形成均匀混合料;将该均匀混合料进行加热干燥处理去除溶剂,干 燥过程需保持在真空度小于-90kPa的真空环境下,干燥温度保持在100℃,得到初始产物;对初始产物进行若干次后处理,每一次后处理包括:研磨,冷压和烧结步骤,其中,冷压成型得到结构致密的圆片样品;烧结是在氩气气氛中将圆片样品进行烧结;多次后处理后即得到掺杂改性的固态电解质片。实施例1-14及对比例1-4中固态电解质片的具体制备参数如表1所示。Disperse the sulfide electrolyte raw materials in pyridine to form an initial reaction mixture; disperse the boric acid ester represented by formula (I-1) in pyridine to form a modified solution; after mixing the initial reaction mixture and the modified solution, pass Disperse sufficiently to form a uniform mixture; heat and dry the uniform mixture to remove the solvent. The drying process must be maintained in a vacuum environment with a vacuum degree of less than -90kPa, and the drying temperature should be maintained at 100°C to obtain the initial product; Several post-treatments, each post-treatment includes: grinding, cold pressing and sintering steps, among which, cold pressing forms a compact disc sample; sintering is to sinter the disc sample in an argon atmosphere; multiple post-treatments Then a doped modified solid electrolyte sheet is obtained. The specific preparation parameters of the solid electrolyte sheets in Examples 1-14 and Comparative Examples 1-4 are shown in Table 1.
全固态锂离子电池的制备Preparation of all solid-state lithium ion batteries
(1)正极极片的制备(1) Preparation of positive pole piece
按照实施例1-14或对比例1-4的方法制备得到固态电解质片,研磨成粉状,与正极活性材料LiNi 1/3Co 1/3Mn 1/3O 2、导电剂Super-P按质量比70:27:3进行混合研磨,获得均匀分散的正极粉料;将正极粉料均匀分散在正极集流体铝箔表面上,然后经过50MPa冷压得到正极极片。 The solid electrolyte sheet was prepared according to the method of Example 1-14 or Comparative Example 1-4, ground into a powder, and combined with the positive electrode active material LiNi 1/3 Co 1/3 Mn 1/3 O 2 and the conductive agent Super-P The mass ratio of 70:27:3 is mixed and ground to obtain a uniformly dispersed positive electrode powder; the positive electrode powder is uniformly dispersed on the surface of the positive electrode current collector aluminum foil, and then the positive pole piece is obtained by cold pressing of 50MPa.
(2)固态电解质片的制备(2) Preparation of solid electrolyte sheet
按照实施例1-14或对比例1-4的方法制备得到固态电解质片。The solid electrolyte sheet was prepared according to the method of Examples 1-14 or Comparative Examples 1-4.
(3)锂金属负极极片的制备(3) Preparation of lithium metal negative pole piece
将锂箔经过辊压附着在负极集流体铜箔表面上,然后经过分切得到负极极片。The lithium foil is attached to the surface of the negative electrode current collector copper foil by rolling, and then the negative electrode piece is obtained by slitting.
(4)全固态锂离子电池的制备(4) Preparation of all solid-state lithium-ion batteries
将上述正极极片、固态电解质片、锂金属负极依次层叠,并在300MPa下加压制备全固态锂离子电池。The above-mentioned positive pole piece, solid electrolyte sheet, and lithium metal negative electrode are sequentially stacked, and pressurized at 300 MPa to prepare an all-solid lithium ion battery.
对上述制备的固态电解质片和全固态锂离子电池分别进行如下性能检测:Perform the following performance tests on the solid electrolyte sheet and all-solid-state lithium ion battery prepared above:
(1)电导率测试:使用辰华电化学工作站测量电解质片的欧姆阻抗,测试温度为25℃,频率范围为1Hz-1MHz,微扰信号为5mV,基于电解质层的阻抗、厚度和面积即可计算离子电导率。(1) Conductivity test: Use Chenhua electrochemical workstation to measure the ohmic impedance of the electrolyte sheet. The test temperature is 25℃, the frequency range is 1Hz-1MHz, and the perturbation signal is 5mV. It can be calculated based on the impedance, thickness and area of the electrolyte layer Ionic conductivity.
(2)表面粗糙度测试:将电解质片放置在高精度光学显微镜下进行观测,在3D成像模式下可以得到电解质片在200*300μm 2内的表面高度分布信息,通过统计电解质片最大表面高度差值即可得到表面粗糙度。 (2) Surface roughness test: Place the electrolyte sheet under a high-precision optical microscope for observation. In 3D imaging mode, the surface height distribution information of the electrolyte sheet within 200*300μm 2 can be obtained, and the maximum surface height difference of the electrolyte sheet can be counted Value to get the surface roughness.
(3)表面元素浓度分布测试:将电解质片放置在扫描电镜下进行观测,并通过EDS(能谱分析)测试采集电解质片表面的元素含量信息,采样面积为1μm*1μm的正方形区域,调整不同采样区域的间距为100μm,即可得到硼元素在电解质片表面不同区域的含量分布结果。(3) Surface element concentration distribution test: place the electrolyte sheet under a scanning electron microscope for observation, and collect the element content information on the surface of the electrolyte sheet through EDS (energy spectrum analysis) test. The sampling area is a square area of 1μm*1μm, and the adjustment is different. The sampling area is 100μm apart, and the content distribution results of boron in different areas on the surface of the electrolyte sheet can be obtained.
(4)元素含量测试:将电解质片溶解于甲醇溶剂中形成均匀溶液,然后通过ICP(电感耦合等离子体发射光谱)测试定量表征溶液中各元素的浓度,即可得到硼元素在电解质片中的含量。(4) Element content test: The electrolyte sheet is dissolved in methanol solvent to form a uniform solution, and then the concentration of each element in the solution is quantitatively characterized by ICP (Inductively Coupled Plasma Emission Spectroscopy) test to obtain the boron element in the electrolyte sheet. content.
(5)界面阻抗测试:使用辰华电化学工作站对全固态锂离子电池进行电化学阻抗测试,频率范围为0.01Hz-1MHz,微扰信号为5mV。(5) Interface impedance test: Use Chenhua electrochemical workstation to conduct electrochemical impedance test on all solid-state lithium-ion batteries, the frequency range is 0.01Hz-1MHz, and the perturbation signal is 5mV.
(6)循环性能测试:在25℃下,将全固态锂离子电池以0.1C恒流充电至电压为4.2V,接着以0.1C恒流放电,直到最终电压为2.8V,记录首次循环的放电容量。然后按照上述操作进行充电和放电循环,循环至100圈时,停止充放电,此时的放电容量与首圈放电容量的比值即为电池的循环容量保持率。(6) Cycle performance test: At 25℃, charge the all-solid-state lithium-ion battery at a constant current of 0.1C to a voltage of 4.2V, then discharge at a constant current of 0.1C until the final voltage is 2.8V, and record the discharge of the first cycle capacity. Then carry out charging and discharging cycles according to the above operation. When the cycle reaches 100 cycles, stop charging and discharging. The ratio of the discharge capacity at this time to the first cycle discharge capacity is the cycle capacity retention rate of the battery.
图1~4及表1具体显示了上述测试的结果:Figures 1 to 4 and Table 1 specifically show the results of the above test:
图1是根据本申请实施方式的固态电解质的XRD测试图谱,从图中可以看到,进行硼酸酯掺杂后的固态电解质的主要晶格衍射峰与对照样品相同,证明少量硼酸酯的引入不会影响硫化物电解质的结构;且硼酸酯自身的衍射峰并没有出现在掺杂样品中,表明硼酸酯已经完全分解。Figure 1 is an XRD test spectrum of a solid electrolyte according to an embodiment of the present application. It can be seen from the figure that the main lattice diffraction peaks of the solid electrolyte doped with borate are the same as the control sample, which proves that a small amount of borate The introduction will not affect the structure of the sulfide electrolyte; and the diffraction peak of borate itself does not appear in the doped sample, indicating that the borate has been completely decomposed.
图2是根据本申请实施方式的固态电解质的Raman测试结果图,从图中可以看到,进行硼酸酯掺杂后的固态电解质只出现了和对照样品相同的峰位,其 代表硫化物固态电解质中的PS 4-基团,也表明掺杂前后固态电解质的主体结构没有改变。 Figure 2 is a graph of the Raman test results of the solid electrolyte according to the embodiment of the present application. It can be seen from the figure that the solid electrolyte doped with borate only has the same peak position as the control sample, which represents the solid state of sulfide. The PS 4 -group in the electrolyte also shows that the main structure of the solid electrolyte has not changed before and after doping.
图3是根据本申请实施方式的固态电解质的元素分布测试结果图,从图中可以明显看到,B、O元素的分布区域和S元素的分布区域基本重叠,证明B、O元素均匀地掺杂进入了硫化物电解质内。Figure 3 is a graph of the element distribution test results of the solid electrolyte according to the embodiment of the present application. It can be clearly seen from the figure that the distribution area of the B and O elements and the distribution area of the S element basically overlap, which proves that the B and O elements are evenly doped The impurities enter the sulfide electrolyte.
图4是根据本申请实施方式的固态电解质片的表面粗糙度测试光学显微镜图。将对比例1、对比例2和实施例12的电解质片分别放置在高精度光学显微镜下进行观测,其中,4-A为对比例1的固态电解质片的光学显微镜图,其未掺入硼酸酯,该电解质片表面形貌非常不均匀,图中显示最大表面高度差为24.36μm;4-B为对比例2的固态电解质片的光学显微镜图,其掺杂有硼酸酯,但仅经过一次后处理,该电解质片表面粗糙度有所降低,图中显示最大表面高度差为18.11μm,但形貌差异仍然明显;4-C为实施例12的固态电解质片的光学显微镜图,而其掺入硼酸酯并经过多次后处理,该电解质片表面均一且粗糙度显著降低,图中显示最大表面高度差仅为3.23μm。Fig. 4 is an optical microscope diagram of a surface roughness test of a solid electrolyte sheet according to an embodiment of the present application. The electrolyte sheets of Comparative Example 1, Comparative Example 2 and Example 12 were placed under a high-precision optical microscope for observation. Among them, 4-A is an optical microscope image of the solid electrolyte sheet of Comparative Example 1, which did not incorporate boric acid. The surface morphology of the electrolyte sheet is very uneven. The figure shows that the maximum surface height difference is 24.36μm; 4-B is the optical microscope image of the solid electrolyte sheet of Comparative Example 2, which is doped with borate, but only through After one post-treatment, the surface roughness of the electrolyte sheet has been reduced. The figure shows that the maximum surface height difference is 18.11μm, but the morphology difference is still obvious; 4-C is an optical microscope image of the solid electrolyte sheet of Example 12, and its Incorporating boric acid ester and after many post-treatments, the surface of the electrolyte sheet is uniform and the roughness is significantly reduced. The figure shows that the maximum surface height difference is only 3.23 μm.
下表1为实施例1-14和对比例1-4的具体参数和测试结果:Table 1 below shows the specific parameters and test results of Examples 1-14 and Comparative Examples 1-4:
表1实施例及对比例的具体参数和测试结果Table 1 Specific parameters and test results of Examples and Comparative Examples
Figure PCTCN2020099496-appb-000003
Figure PCTCN2020099496-appb-000003
表1所示的数据表明了本申请实施方式中的各参数对于所制得的固态电解质和锂离子电池性能的影响。The data shown in Table 1 shows the influence of various parameters in the embodiments of the present application on the performance of the solid electrolyte and lithium ion battery prepared.
实施例1~5的数据表明了硼元素在电解质片中的含量变化对电解质片性能的影响。当电解质片中的硼元素含量过低时(如实施例1),硼元素的引入对电解质结构的影响较小,虽然也可对电解质片电导率有一定的提升,但该种提升效果不显著,且过低的硼元素含量会导致浓度测试误差增大,因而测得的浓度偏差也较大。当电解质片中的硼元素含量过高时,易出现局部元素富集的问题,不利于实现均匀的改性结果,且过高的硼元素掺入量会降低含锂离子在电解质片中的相对含量,因此也不利于提升电解质片的电导率和电池性能。因而,本申请的实施方式中,电解质片中的硼元素的质量浓度为0.5%~10%,优选为3%~7%。The data of Examples 1 to 5 show the influence of the content change of the boron element in the electrolyte sheet on the performance of the electrolyte sheet. When the content of boron in the electrolyte sheet is too low (as in Example 1), the introduction of boron has little effect on the electrolyte structure. Although it can also improve the conductivity of the electrolyte sheet to a certain extent, the improvement effect is not significant , And too low boron content will increase the concentration test error, so the measured concentration deviation is also larger. When the content of boron in the electrolyte sheet is too high, the problem of local element enrichment is likely to occur, which is not conducive to achieving uniform modification results, and too high doping of boron element will reduce the relative content of lithium ions in the electrolyte sheet. The content is therefore not conducive to improving the conductivity of the electrolyte sheet and battery performance. Therefore, in the embodiment of the present application, the mass concentration of the boron element in the electrolyte sheet is 0.5% to 10%, preferably 3% to 7%.
实施例3、6的数据表明了后处理次数变化对电解质片性能的影响。从表1可以看到,实施例6获得了比实施例3更好的性能,这是由于,随着后处理次 数的增加,掺杂后的电解质材料经过多次的研磨、压块和烧结,多种元素在体相材料中的分布趋于均匀,表面粗糙度和界面阻抗得到降低。不过,过于多次的高温烧结也可能导致电解质发生结构相变,影响电导率的提升幅度。因而,本申请的实施方式中,后处理的次数应在1次以上,以2~3次为宜。The data of Examples 3 and 6 show the effect of changes in the number of post-treatments on the performance of the electrolyte sheet. It can be seen from Table 1 that Example 6 achieves better performance than Example 3. This is because as the number of post-treatments increases, the doped electrolyte material undergoes multiple grinding, briquetting and sintering. The distribution of multiple elements in the bulk material tends to be uniform, and the surface roughness and interface impedance are reduced. However, too many high-temperature sintering may also cause structural phase changes in the electrolyte, which affects the increase in conductivity. Therefore, in the embodiment of the present application, the number of post-processing should be more than once, preferably 2 to 3 times.
实施例6~12以进行三次后处理为例,说明了随着后处理次数的增加,烧结温度成梯度上升所产生的技术效果。Examples 6-12 take three post-treatments as an example to illustrate the technical effect of the gradual increase in the sintering temperature as the number of post-treatments increases.
首先,对于首次后处理中的烧结步骤,烧结温度不宜过高。从表1中可以看到,实施例6~9中,实施例7获得了最佳的性能提升,其后依次为实施例8、9、6。这是由于,实施例6的首次烧结温度过高,溶剂的挥发、硼酸酯的分解和硫化物电解质的成相过程集中在第一次烧结步骤中进行,而前两个过程中不断发生体积变化导致压实的电解质块体变成多孔疏松结构,颗粒与颗粒间的接触不良会影响硼元素在电解质体相中的扩散过程,因而导致电解质表面成分的差异增大、均匀性降低;而且长时间的高温烧结也会导致电解质杂相生成以及电导率降低,进一步影响电池的界面阻抗和循环性能。因此,在本申请的实施方式中,首次后处理中的烧结温度为200℃时性能最好。First of all, for the sintering step in the first post-treatment, the sintering temperature should not be too high. It can be seen from Table 1 that among Examples 6-9, Example 7 achieved the best performance improvement, followed by Examples 8, 9, and 6. This is because the first sintering temperature of Example 6 is too high. The volatilization of the solvent, the decomposition of boric acid ester and the phase formation of the sulfide electrolyte are concentrated in the first sintering step, and the volume is continuously generated during the first two processes. The change causes the compacted electrolyte block to become a porous and loose structure, and the poor contact between particles will affect the diffusion process of boron in the electrolyte bulk, resulting in increased differences in electrolyte surface composition and reduced uniformity; and High temperature sintering over time will also lead to the formation of electrolyte miscellaneous phases and the decrease of conductivity, which will further affect the interface impedance and cycle performance of the battery. Therefore, in the embodiment of the present application, the performance is best when the sintering temperature in the first post-treatment is 200°C.
其次,对于第二次后处理中的烧结步骤,则需要选择适中的烧结温度,最好高于第一的烧结温度。实施例7、10~12的数据说明了改变第二次烧结温度对电解质片和电池性能的影响,实施例12的性能最优,其次为实施例11和7,而实施例10的性能改善幅度略小。这是由于,如第二次烧结温度过低(如实施例10),硼酸酯无法分解,电解质的成相过程和硼元素改性过程未完全、或者都只能聚集到第三次后处理过程中完成,由于硼酸酯分解的影响,电解质片仍无法保持良好的界面接触,因此不利于硼元素的均匀分布和表面性能改善。如第二次烧结温度过高(实施例7),则电解质的成相过程和硼元素改性过程集中至第二次后处理中进行,也不利于均匀改性效果,且过高的热处理温度对于电解质的电导率也有不良影响。Secondly, for the sintering step in the second post-treatment, a moderate sintering temperature needs to be selected, preferably higher than the first sintering temperature. The data of Examples 7 and 10 to 12 illustrate the effect of changing the second sintering temperature on the electrolyte sheet and battery performance. Example 12 has the best performance, followed by Examples 11 and 7, and Example 10 has improved performance Slightly smaller. This is because, if the second sintering temperature is too low (as in Example 10), the borate cannot be decomposed, the electrolyte phase formation process and the boron element modification process are not complete, or they can only be aggregated to the third post-treatment During the completion of the process, due to the influence of the decomposition of borate, the electrolyte sheet still cannot maintain good interface contact, which is not conducive to the uniform distribution of boron element and the improvement of surface properties. If the second sintering temperature is too high (Example 7), the electrolyte phase formation process and the boron element modification process are concentrated in the second post-treatment, which is not conducive to the uniform modification effect, and the heat treatment temperature is too high It also has an adverse effect on the conductivity of the electrolyte.
综上,以三次后处理为例,依次采取低、中、高温三种温区的烧结温度,有利于将电解质改性过程中的不同反应区分开来,从而制备得到硼元素均匀分布的电解质片,电解质片表面成分和形貌的高度均一性,其表面粗糙度和离子电导率均有明显改善,从而提升固态电池的界面性能和循环性能。To sum up, taking the three post-treatments as an example, the sintering temperature in three temperature zones of low, medium and high temperature is adopted in sequence, which is beneficial to distinguish the different reactions in the electrolyte modification process, so as to prepare an electrolyte sheet with uniform boron element distribution. , The surface composition and morphology of the electrolyte sheet are highly uniform, and its surface roughness and ionic conductivity are significantly improved, thereby improving the interface performance and cycle performance of the solid-state battery.
实施例13、14显示了改变电解质的种类对电解质片和电池性能的影响。采用不同组成的硫化物电解质材料,均能得到硼元素均匀改性的电解质片,相比于对比例而言,在表面元素分布、表面形貌和离子电导率方面均有明显的提升,因而,本申请实施方式的硫化物固态电解质片中,所包含的硫化物电解质材料的种类不受限制。Examples 13 and 14 show the effect of changing the electrolyte type on the electrolyte sheet and battery performance. Using sulfide electrolyte materials of different compositions, electrolyte sheets with uniformly modified boron elements can be obtained. Compared with the comparative example, the surface element distribution, surface morphology and ion conductivity are significantly improved. Therefore, In the sulfide solid electrolyte sheet of the embodiment of the present application, the type of the sulfide electrolyte material contained is not limited.
根据上述说明书的揭示和教导,本领域技术人员还可以对上述实施方式进行变更和修改。因此,本申请并不局限于上面揭示和描述的具体实施方式,对本申请的一些修改和变更也应当落入本申请的权利要求的保护范围内。此外,尽管本说明书中使用了一些特定的术语,但这些术语只是为了方便说明,并不对本申请构成任何限制。Based on the disclosure and teaching of the foregoing specification, those skilled in the art can also make changes and modifications to the foregoing embodiments. Therefore, this application is not limited to the specific implementations disclosed and described above, and some modifications and changes to this application should also fall within the protection scope of the claims of this application. In addition, although some specific terms are used in this specification, these terms are only for convenience of description and do not constitute any limitation to the application.

Claims (21)

  1. 一种硫化物固态电解质片,包含硫化物电解质材料及掺杂于所述硫化物电解质材料中的硼元素,且所述电解质片表面任意位置的硼元素质量浓度B 0与电解质片表面距离该位置100μm处的硼元素质量浓度B 100的相对偏差(B 0-B 100)/B 0不超过20%。 A sulfide solid electrolyte sheet, the electrolyte material comprising a sulfide and boron is doped in the sulfide electrolyte material, and the boron concentration of the electrolyte sheet B 0 from the surface of the electrolyte sheet surface position of an arbitrary position The relative deviation (B 0 -B 100 )/B 0 of the boron element mass concentration B 100 at 100 μm does not exceed 20%.
  2. 根据权利要求1所述的硫化物固态电解质片,其中,所述相对偏差(B 0-B 100)/B 0不超过10%。 The sulfide solid electrolyte sheet according to claim 1, wherein the relative deviation (B 0 -B 100 )/B 0 does not exceed 10%.
  3. 根据权利要求1或2所述的硫化物固态电解质片,其中,所述相对偏差(B 0-B 100)/B 0不超过8%。 The sulfide solid electrolyte sheet according to claim 1 or 2, wherein the relative deviation (B 0 -B 100 )/B 0 does not exceed 8%.
  4. 根据权利要求1-3中任一项所述的硫化物固态电解质片,其中,所述硫化物固态电解质片的表面粗糙度为3μm~15μm。The sulfide solid electrolyte sheet according to any one of claims 1 to 3, wherein the surface roughness of the sulfide solid electrolyte sheet is 3 μm to 15 μm.
  5. 根据权利要求1-4中任一项所述的硫化物固态电解质片,其中,所述硫化物固态电解质片的表面粗糙度为3μm~10μm。The sulfide solid electrolyte sheet according to any one of claims 1 to 4, wherein the surface roughness of the sulfide solid electrolyte sheet is 3 μm to 10 μm.
  6. 根据权利要求1-5中任一项所述的硫化物固态电解质片,其中,所述硫化物固态电解质片的表面粗糙度为3μm~6μm。The sulfide solid electrolyte sheet according to any one of claims 1 to 5, wherein the surface roughness of the sulfide solid electrolyte sheet is 3 μm to 6 μm.
  7. 根据权利要求1-6中任一项所述的硫化物固态电解质片,其中,所述硫化物固态电解质片的电导率为1.6mS/cm~2.9mS/cm。The sulfide solid electrolyte sheet according to any one of claims 1 to 6, wherein the electrical conductivity of the sulfide solid electrolyte sheet is 1.6 mS/cm to 2.9 mS/cm.
  8. 根据权利要求1-7中任一项所述的硫化物固态电解质片,其中,所述硫化物固态电解质片的电导率为2.1mS/cm~2.8mS/cm。The sulfide solid electrolyte sheet according to any one of claims 1-7, wherein the conductivity of the sulfide solid electrolyte sheet is 2.1 mS/cm to 2.8 mS/cm.
  9. 根据权利要求1-8中任一项所述的硫化物固态电解质片,其中,所述硫化物固态电解质片中硼元素的质量浓度为0.5%~10%。The sulfide solid electrolyte sheet according to any one of claims 1-8, wherein the mass concentration of boron element in the sulfide solid electrolyte sheet is 0.5%-10%.
  10. 根据权利要求1-9中任一项所述的硫化物固态电解质片,其中,所述硫化物固态电解质片中硼元素的质量浓度为3%~7%。The sulfide solid electrolyte sheet according to any one of claims 1-9, wherein the mass concentration of boron element in the sulfide solid electrolyte sheet is 3% to 7%.
  11. 根据权利要求1-10中任一项所述的硫化物固态电解质片,其中,所述 硫化物电解质材料包括Li 2S·P 2S 5、Li 2S·GeS 2、Li 2S·SiS 2、Li 6PS 5X和Li 7P 3S 11中的一种或几种,其中,X选自Cl、Br、I中的至少一种。 The sulfide solid electrolyte sheet according to any one of claims 1-10, wherein the sulfide electrolyte material comprises Li 2 S·P 2 S 5 , Li 2 S·GeS 2 , Li 2 S·SiS 2 One or more of Li 6 PS 5 X and Li 7 P 3 S 11 , wherein X is selected from at least one of Cl, Br, and I.
  12. 一种权利要求1-11中任一项所述的硫化物固态电解质片的制备方法,包括:A method for preparing the sulfide solid electrolyte sheet according to any one of claims 1-11, comprising:
    获取包含硫化物电解质原料和有机溶剂的反应初混液;Obtain an initial reaction mixture containing sulfide electrolyte raw materials and organic solvents;
    获取包含硼酸酯和有机溶剂的改性溶液;Obtain a modified solution containing borate and organic solvent;
    将所述反应初混液与所述改性溶液混合,干燥,得到初始产物;Mixing the initial reaction mixture with the modification solution and drying to obtain an initial product;
    对所述初始产物进行1次以上后处理,每次所述后处理依次包括研磨、冷压和烧结步骤。The initial product is subjected to more than one post-treatment, and each post-treatment sequentially includes the steps of grinding, cold pressing and sintering.
  13. 根据权利要求12所述的硫化物固态电解质片的制备方法,其中,所述后处理的次数为2~3次。The method for preparing a sulfide solid electrolyte sheet according to claim 12, wherein the number of post-treatments is 2 to 3 times.
  14. 根据权利要求12或13所述的硫化物固态电解质片的制备方法,其中,所述烧结的温度为200℃~700℃。The method for preparing a sulfide solid electrolyte sheet according to claim 12 or 13, wherein the sintering temperature is 200°C to 700°C.
  15. 根据权利要求12-14中任一项所述的硫化物固态电解质片的制备方法,其中,所述烧结的温度为200℃~600℃。The method for preparing a sulfide solid electrolyte sheet according to any one of claims 12-14, wherein the sintering temperature is 200°C to 600°C.
  16. 根据权利要求12-15中任一项所述的硫化物固态电解质片的制备方法,其中,每次后处理中的烧结温度随着后处理次数的增加而升高。The method for preparing a sulfide solid electrolyte sheet according to any one of claims 12-15, wherein the sintering temperature in each post-treatment increases as the number of post-treatments increases.
  17. 根据权利要求12-16中任一项所述的硫化物固态电解质片的制备方法,其中,所述硼酸酯具有式(I)所示的结构:The method for preparing a sulfide solid electrolyte sheet according to any one of claims 12-16, wherein the borate has a structure represented by formula (I):
    Figure PCTCN2020099496-appb-100001
    Figure PCTCN2020099496-appb-100001
    其中,R选自C1~C4烷基。Wherein, R is selected from C1-C4 alkyl.
  18. 一种全固态锂离子电池,其通过权利要求1-11中任一项所述的硫化物固态电解质片或根据权利要求12-17中任一项所述的制备方法制备的硫化物固 态电解质片制备得到。An all-solid-state lithium ion battery, which is prepared by the sulfide solid electrolyte sheet according to any one of claims 1-11 or the preparation method according to any one of claims 12-17 Prepared.
  19. 一种叠片式全固态锂离子电池,包括正极极片、固态电解质片和负极极片;其中,所述固态电解质片为权利要求1-11中任一项所述的硫化物固态电解质片或根据权利要求12-17中任一项所述的制备方法制备的硫化物固态电解质片。A laminated all-solid-state lithium ion battery, comprising a positive pole piece, a solid electrolyte sheet and a negative pole piece; wherein the solid electrolyte sheet is the sulfide solid electrolyte sheet according to any one of claims 1-11 or A sulfide solid electrolyte sheet prepared according to the preparation method of any one of claims 12-17.
  20. 根据权利要求19所述的叠片式全固态锂离子电池,所述正极极片通过包含固态电解质片、正极活性材料和导电剂的原料制备得到;其中,所述固态电解质片为权利要求1-11中任一项所述的硫化物固态电解质片或根据权利要求12-17中任一项所述的制备方法制备的硫化物固态电解质片。The laminated all-solid-state lithium-ion battery according to claim 19, wherein the positive pole piece is prepared from a raw material comprising a solid electrolyte sheet, a positive electrode active material and a conductive agent; wherein, the solid electrolyte sheet is according to claim 1- The sulfide solid electrolyte sheet according to any one of 11 or the sulfide solid electrolyte sheet prepared according to the preparation method according to any one of claims 12-17.
  21. 一种装置,包括根据权利要求18所述的全固态锂离子电池或根据权利要求19或20所述的叠片式全固态锂离子电池。A device comprising the all solid state lithium ion battery according to claim 18 or the laminated all solid state lithium ion battery according to claim 19 or 20.
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