WO2021179740A1 - Diaphragm-negative electrode material of integrated structure and preparation method therefor, and secondary battery - Google Patents

Diaphragm-negative electrode material of integrated structure and preparation method therefor, and secondary battery Download PDF

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WO2021179740A1
WO2021179740A1 PCT/CN2020/139234 CN2020139234W WO2021179740A1 WO 2021179740 A1 WO2021179740 A1 WO 2021179740A1 CN 2020139234 W CN2020139234 W CN 2020139234W WO 2021179740 A1 WO2021179740 A1 WO 2021179740A1
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negative electrode
integrated structure
separator
electrode material
prepared
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PCT/CN2020/139234
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French (fr)
Chinese (zh)
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唐永炳
李晋
李翔
龚德才
欧学武
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深圳先进技术研究院
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1395Processes of manufacture of electrodes based on metals, Si or alloys
    • 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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/134Electrodes based on metals, Si or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/403Manufacturing processes of separators, membranes or diaphragms
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/46Separators, membranes or diaphragms characterised by their combination with electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027Negative electrodes
    • 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

Definitions

  • the present invention relates to the field of lithium ion batteries, and in particular to a diaphragm negative electrode material with an integrated structure, a preparation method thereof, and a secondary battery.
  • lithium-ion batteries As a new type of energy storage device, lithium-ion batteries have the advantages of high energy density, long cycle life, no memory effect, and small self-discharge, and are widely used in various portable mobile devices and electric vehicles.
  • Lithium-ion batteries are mainly composed of positive and negative electrodes, separators, electrolyte and other parts, and are assembled by stacking negative electrodes, separators, and positive electrodes in sequence.
  • When charging lithium ions are removed from the positive electrode material and migrate to the negative electrode active material; when discharging, lithium ions are removed from the negative electrode active material and return to the positive electrode.
  • Traditional lithium-ion battery negative electrodes usually use graphite as the active material and metal copper foil as the current collector. Recent studies have shown that the use of metal foil as the negative electrode and the integrated design of the negative electrode active material and the negative current collector.
  • This new type of battery system can effectively reduce the weight and volume of the battery, and significantly improve the quality and volume energy density of the battery. .
  • metal foil as a negative electrode has the above advantages, but it also has the following problems: (1) The alloying/dealloying process of the metal negative electrode is likely to cause volume expansion and pulverization; (2) The metal negative electrode is The burrs produced in the process of swelling and pulverization may pierce the separator and cause safety problems; (3) The SEI film formed on the surface of the metal negative electrode is continuously generated-broken-regenerated, consuming a large amount of ions and electrolyte, and causing the coulomb of the battery. low efficiency.
  • the polymer coating can inhibit the volume expansion and pulverization during the charging and discharging process of the aluminum anode, and effectively isolate the electrolyte from the aluminum anode, and improve the capacity attenuation caused by the continuous regeneration of the SEI film.
  • the polymer coating under this technology The combination performance with the metal negative electrode is general, the effect is limited, and the operation process is more complicated.
  • Another example is a three-dimensional porous metal negative electrode, the porous structure of the negative electrode is designed to have high porosity and excellent spatial structure. It is helpful to alleviate the problem of metal negative electrode expansion and powdering caused by stress concentration.
  • the structure has a high specific surface area, which can enhance the storage and transport capacity of the electrolyte during the charge and discharge process, facilitate the progress of the electrochemical reaction, and improve the utilization efficiency of the metal negative electrode.
  • the metal anode with a three-dimensional porous structure can play a role in alleviating the volume expansion of the anode during the charge and discharge process, the synthesis and preparation process of this porous structure is more complicated, and the problem of capacity attenuation caused by the continuous regeneration of the SEI film still exists.
  • a method for improving the cycle life of a metal negative electrode using a high-concentration electrolyte In the process of charging and discharging, the high-concentration electrolyte can form a structurally stable SEI film on the surface of the metal negative electrode, thereby improving the service life of the metal negative electrode material and the specific capacity and cycle stability of the new battery.
  • the use of high-concentration electrolyte can effectively increase the electrochemical window of the electrolyte.
  • the use of high-concentration electrolyte can also improve the cycle stability of the metal negative electrode, the high-concentration electrolyte has insufficient wettability for conventional separator materials, which is not ideal in actual use. Therefore, the current preparation method still cannot completely solve the problems existing in the metal negative electrode.
  • the purpose of the present invention is to provide a separator negative electrode material with an integrated structure, a preparation method thereof, and a secondary battery. Poor battery safety performance and low Coulomb efficiency.
  • a method for preparing a separator anode material with an integrated structure includes the following steps:
  • the metal negative electrode in an electrospinning device, set the electrospinning power supply voltage to be 5-30kV, the distance between the syringe and the metal negative electrode is 5-50cm, and control the polymer solution
  • the flow rate is 300-1000 ⁇ L/h, and the polymer diaphragm layer is prepared by electrostatic spinning on the surface of the metal negative electrode to obtain the diaphragm negative electrode material of the integrated structure.
  • an integrated structured separator negative electrode material includes a metal negative electrode, and a polymer separator layer bonded on any side of the metal negative electrode.
  • a secondary battery comprising a positive electrode, an integrated structure of the separator negative electrode material and an electrolyte; wherein the integrated structure of the separator negative electrode material is made of the integrated structure of the separator negative electrode material
  • the preparation method is prepared or obtained by the separator negative electrode material of the integrated structure.
  • the preparation method of the diaphragm negative electrode material of the integrated structure of the present invention firstly prepares a high molecular polymer solution, adopts the preparation method of electrostatic spinning, and controls the power supply voltage of the electrostatic spinning and the distance between the syringe and the metal negative electrode. And the flow rate of the high molecular polymer solution to prepare the integrated structure of the negative electrode material for the diaphragm.
  • Porosity and controllable porosity can better suppress the volume expansion and pulverization of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form burrs and pierce the separator, ensuring the safety performance of the secondary battery; secondly, through The electrospinning process is combined with the metal negative electrode to form an integrated structure, so that the diaphragm and the metal negative electrode are combined, which further increases the effective contact between the polymer diaphragm layer and the metal negative electrode, and makes the obtained integrated structure
  • the thickness and shape of the structured separator anode material can be designed at will, and the flexibility is good, which to a certain extent inhibits the problem of expansion and pulverization of the metal foil anode during the cycle of the secondary battery, and improves the safety performance and coulomb efficiency of the secondary battery. .
  • the preparation method materials are easily available, the production method is environmentally friendly, and the production process is simple and the conditions are controllable.
  • the negative electrode material of the integrated structure of the separator includes a metal negative electrode, a polymer separator layer bonded to any side of the metal negative electrode, and the separator layer is a polymer separator layer,
  • the polymer separator layer has good flexibility, and has a certain degree of toughness and controllable porosity, which can better inhibit the volume expansion and powdering of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form burrs and thorns.
  • the polymer diaphragm layer is directly combined with the metal negative electrode, which further increases the effective contact between the diaphragm and the metal negative electrode, and makes the thickness of the prepared integrated structure of the diaphragm negative electrode material And the shape can be designed at will, the flexibility is good, to a certain extent, the secondary battery cycle, the metal foil negative electrode is easy to cause the problem of swelling and powdering, and the safety performance and coulomb efficiency of the secondary battery are improved.
  • the secondary battery includes a positive electrode, an integrated structured separator negative electrode material and an electrolyte; wherein the integrated structured separator negative electrode material is composed of the integrated structured separator negative electrode material
  • the preparation method is obtained by the preparation method or is the separator negative electrode material with the integrated structure.
  • the use of the above-mentioned integrated structure of the diaphragm negative electrode material or the battery negative electrode prepared by the preparation method of the above-mentioned integrated structure of the diaphragm negative electrode material is used as the negative electrode material of the secondary battery, which simplifies the internal structure and assembly process of the battery, and greatly improves the metal
  • the interface contact characteristics of the negative electrode and the separator, the prepared secondary battery ensures that the metal negative electrode material is not easy to pulverize and can maintain integrity; at the same time, the effective contact distance between the metal negative electrode and the separator is increased, and the cycle stability of the secondary battery is enhanced. Coulomb efficiency.
  • FIG. 1 is a schematic diagram of the structure of a separator negative electrode material with an integrated structure provided by an embodiment of the present invention.
  • Fig. 2 is an equipment diagram of an electrospinning device provided by an embodiment of the present invention.
  • FIG. 3 is a schematic structural diagram of a separator negative electrode material with an integrated structure including two polymer separator layers provided by Embodiment 4 of the present invention.
  • FIG. 4 is a schematic structural diagram of a separator negative electrode material with an integrated structure including three polymer separator layers provided by Embodiment 5 of the present invention.
  • Fig. 5 is a schematic structural diagram of a secondary battery provided by an embodiment of the present invention.
  • Fig. 6 is an electron micrograph of a separator negative electrode material with an integrated structure provided by an embodiment of the present invention.
  • FIG. 7 is a cross-sectional view of a separator negative electrode material with an integrated structure provided by an embodiment of the present invention.
  • FIG. 8 is a performance analysis diagram of charging and discharging of the secondary battery provided in Example 1 of the present invention.
  • Fig. 9 is a performance analysis diagram of the charging and discharging of the secondary battery provided by the comparative example of the present invention.
  • FIG. 10 is an analysis diagram of the wettability of the separator negative electrode material of the integrated structure provided in the embodiment 1 and the embodiment 2 of the present invention.
  • first and second are only used for description purposes, and cannot be understood as indicating or implying relative importance or implicitly indicating the number of indicated technical features. Thus, the features defined with “first” and “second” may explicitly or implicitly include one or more of these features.
  • “plurality” means two or more than two, unless otherwise specifically defined.
  • An example of the present invention provides a separator negative electrode material with an integrated structure. As shown in FIG. Wherein, the polymer diaphragm layer is combined with the metal negative electrode through a spinning process to form an integrated structure.
  • the negative electrode material of the integrated structure of the separator includes a metal negative electrode, a polymer separator layer bonded to any side of the metal negative electrode, and the separator layer is a polymer separator layer,
  • the polymer separator layer has good flexibility, and has a certain degree of toughness and controllable porosity, which can better suppress the volume expansion and pulverization of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form burrs and thorns.
  • the polymer diaphragm layer is directly combined with the metal negative electrode, which further increases the effective contact between the diaphragm and the metal negative electrode, and makes the thickness of the prepared integrated structure of the diaphragm negative electrode material And the shape can be designed at will, the flexibility is good, to a certain extent, the secondary battery cycle, the metal foil negative electrode is easy to cause the problem of swelling and powdering, and the safety performance and coulomb efficiency of the secondary battery are improved.
  • the metal negative electrode is selected from a metal negative electrode in which a negative electrode current collector and a negative electrode material are integrated, and the metal negative electrode is used as a negative electrode current collector and a negative electrode material at the same time, and the negative electrode active material and the current collector are integratedly designed as a new type of battery system , Can effectively reduce the weight and volume of the battery, significantly improve the quality and volume energy density of the battery, and greatly reduce the production cost of the battery.
  • the material of the metal negative electrode is selected from one of aluminum, tin, magnesium, zinc, copper, iron, nickel, titanium, manganese, antimony, bismuth, etc. that undergo alloying battery reactions, or contains at least one of the metals The alloy of the elements.
  • the thickness of the metal negative electrode is 10-1000 ⁇ m.
  • the material of the gold substrate is selected from aluminum materials with a thickness of 50 ⁇ m.
  • the metal negative electrode is selected from a metal negative electrode that has not undergone pretreatment or a metal negative electrode that has undergone pretreatment.
  • the pretreated metal negative electrode is selected from any one of a polished metal negative electrode, a polished metal negative electrode, a sandblasted metal negative electrode, and a plasma-treated metal negative electrode. Selecting the pretreated metal negative electrode as the negative electrode material can further improve the binding capacity of the metal negative electrode and the polymer separator layer, improve the overall performance of the prepared integrated structure separator negative electrode material, and ensure stronger adhesion. It is not easy to fall off between the metal negative electrode and the polymer separator layer.
  • the polymer separator layer has good flexibility, and has certain toughness and controllable porosity, which can better inhibit the use of the negative metal negative electrode.
  • the problem of medium volume expansion and pulverization ensures that the metal negative electrode will not form burrs and pierce the separator, ensuring the safety performance of the secondary battery.
  • the material of the polymer diaphragm layer is selected from polymethyl methacrylate, tetrahydroperfluorooctyl acrylate, polyvinyl alcohol, polyvinyl phenol, polyvinyl chloride, polyvinyl carbazole, polyvinylidene fluoride At least one of ethylene, polyvinylidene fluoride-hexafluoropropylene, polyacrylonitrile, and polylactic acid.
  • Select high molecular polymers that can exhibit a certain degree of flexibility, toughness and controllable porosity as the raw material of the polymer membrane layer to ensure that the prepared polymer membrane layer has good flexibility, and has certain toughness and flexibility.
  • the controlled porosity can better suppress the volume expansion and pulverization of the negative metal negative electrode during use.
  • the thickness of the polymer membrane layer is 50 ⁇ m to 150 ⁇ m. If the thickness of the polymer separator layer is too thin, the separator layer is easy to break down or break, thereby affecting the safety performance of the prepared secondary battery; if the thickness of the polymer separator layer is too thick, it will cause The ionic conductivity of the prepared secondary battery will decrease, which affects the performance of the battery.
  • the integrated structure of the separator negative electrode material includes a metal negative electrode, and a polymer separator layer bonded to either side of the metal negative electrode, wherein the polymer separator layer is formed by combining with the metal negative electrode through a spinning process Integrated structure.
  • the spinning process is selected from the electrospinning process.
  • the separator anode material with the integrated structure provided by the embodiment of the present invention can be prepared by the following method.
  • the embodiment of the present invention also provides a method for preparing a separator negative electrode material with an integrated structure.
  • the method includes the following steps:
  • the preparation method of the diaphragm negative electrode material of the integrated structure of the present invention firstly prepares a high molecular polymer solution, adopts the preparation method of electrostatic spinning, and controls the power supply voltage of the electrostatic spinning and the distance between the syringe and the metal negative electrode. And the flow rate of the high molecular polymer solution to prepare the integrated structure of the negative electrode material for the diaphragm.
  • Porosity and controllable porosity can better suppress the volume expansion and pulverization of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form burrs and pierce the separator, ensuring the safety performance of the secondary battery; secondly, through The electrospinning process is combined with the metal negative electrode to form an integrated structure, so that the diaphragm and the metal negative electrode are combined, which further increases the effective contact between the polymer diaphragm layer and the metal negative electrode, and makes the obtained integrated structure
  • the thickness and shape of the structured separator anode material can be designed at will, and the flexibility is good, which to a certain extent inhibits the problem of expansion and pulverization of the metal foil anode during the cycle of the secondary battery, and improves the safety performance and coulomb efficiency of the secondary battery. .
  • the preparation method materials are easily available, the production method is environmentally friendly, and the production process is simple and the conditions are controllable.
  • a high-molecular polymer solution is prepared.
  • the high-molecular polymer solution includes a high-molecular polymer solute, an additive, and a solvent.
  • the high molecular polymer solution includes a high molecular polymer solute selected from the group consisting of polymethyl methacrylate, tetrahydroperfluorooctyl acrylate, polyvinyl alcohol, polyvinyl phenol, At least one of polyvinyl chloride, polyvinylcarbazole, polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene, polyacrylonitrile, and polylactic acid.
  • Select high molecular polymers that can exhibit a certain degree of flexibility, toughness and controllable porosity as the raw material of the polymer membrane layer to ensure that the prepared polymer membrane layer has good flexibility, and has certain toughness and flexibility.
  • the controlled porosity can better suppress the volume expansion and pulverization of the negative metal negative electrode during use.
  • the high molecular polymer solution includes additives, and the purpose of adding the additives is to enhance the conductivity of the ions and further improve the conductivity of the prepared secondary battery.
  • the additives are selected from Al 2 O 3 , SiO 2 , materials with perovskite configuration ABO 3 such as Li 0.5 La 0.5 TiO 3 , materials with LISICON structure such as Li 14 Zn(GeO 4 ) 4 , such as Na 3 Zr 2 Si 2 PO 12 NASICON structure material, such as at least one kind of Li 7 La 3 Zr 2 O 12 garnet type oxide material.
  • the high-molecular polymer solution includes a solvent, and the addition of the solvent can better dissolve the high-molecular polymer for preparation of the high-molecular polymer solution.
  • the solvent is selected from at least one of tetrahydrofuran, acetone, dimethylformamide, dimethylacetamide, toluene, water, dichloromethane, and chloroform.
  • the volume percentage concentration of the high molecular polymer solution is 1%-30%. If the concentration of the solution is too low, the adhesion amount of the polymer on the surface of the metal negative electrode will be less. Too little adhesion will affect the flexibility of the polymer diaphragm layer, and also cause the thickness of the prepared polymer diaphragm layer to be too thin , Affect the prepared integrated structure of the separator anode material. If the concentration of the solution is too high, the solubility of the high molecular polymer will be poor, which will easily lead to uneven dissolution of the prepared high molecular polymer solution, which in turn affects the properties of the polymer membrane layer and the integrated structure obtained The separator anode material.
  • the preparation of the high molecular polymer solution includes the following steps: mixing the selected high molecular polymer, additives, and solvent according to the volume percentage concentration of the high molecular polymer solution, and performing the mixing treatment at a temperature between 50 and 80°C to ensure that each The substance dissolves. Further preferably, the time of the mixing treatment is 12 to 48 hours.
  • the mixing treatment method includes, but is not limited to, conventional methods such as stirring.
  • the high molecular polymer solution is placed in the syringe of the electrostatic spinning device for standby.
  • the metal negative electrode is placed in the electrospinning device, the power supply voltage for electrospinning is set to 5-30kV, and the distance between the syringe and the metal negative electrode is 5-50cm,
  • the flow rate of the high molecular polymer solution is controlled to be 300-1000 ⁇ L/h, and a high molecular diaphragm layer is prepared by electrostatic spinning on the surface of the metal negative electrode to obtain the diaphragm negative electrode material of the integrated structure.
  • the material of the metal negative electrode is selected from one of aluminum, tin, magnesium, zinc, copper, iron, nickel, titanium, manganese, antimony, bismuth, etc. that undergo alloying battery reactions, or contains at least one of the metals The alloy of the elements.
  • the metal negative electrode is selected from a metal negative electrode that has not undergone pretreatment or a metal negative electrode that has undergone pretreatment.
  • the pretreated metal negative electrode is selected from any one of a polished metal negative electrode, a polished metal negative electrode, a sandblasted metal negative electrode, and a plasma-treated metal negative electrode. Selecting the pretreated metal negative electrode as the negative electrode material can further improve the binding capacity of the metal negative electrode and the polymer separator layer, improve the overall performance of the prepared integrated structure separator negative electrode material, and ensure stronger adhesion. It is not easy to fall off between the metal negative electrode and the polymer separator layer.
  • placing the metal negative electrode in the electrospinning device includes the following steps: cutting the metal negative electrode to obtain an appropriate size, and fixing the metal negative electrode to the collection screen in the electrospinning device. surface.
  • the electrospinning device is shown in FIG. 2.
  • 1 is a high-voltage power supply
  • 2 is a syringe containing a polymer solution
  • 3 is the polymer diaphragm layer
  • 4 is the metal negative electrode
  • 5 is the receiving screen.
  • the electrospinning power supply voltage is set to 5-30kV
  • the distance between the syringe and the metal negative electrode is 5-50cm
  • the flow rate of the polymer solution is controlled to be 300-1000 ⁇ L/h.
  • the surface of the metal negative electrode is electrostatically spun to prepare a polymer diaphragm layer to obtain the diaphragm negative electrode material of the integrated structure.
  • the electrospinning power supply voltage, the distance between the syringe and the metal negative electrode, and the flow rate of the polymer solution are important factors that jointly determine whether the spinning solution can be ejected smoothly and reach the collection screen. Therefore, , Limiting the above conditions is conducive to the smooth progress of the test.
  • the power supply voltage for electrospinning is set to 5-30kV, and the voltage is 5-30kV for the spinning solution to be sprayed smoothly during work. If the power supply voltage is too low, an effective electric field cannot be formed, resulting in the solution not being sprayed. , The product cannot be prepared; if the power supply voltage is too high, it will affect the normal spinning process, and there is a certain degree of danger. Further, the distance between the syringe and the metal negative electrode is 5-50 cm.
  • the distance between the syringe and the metal negative electrode is too far, it will affect the preparation of the diaphragm layer structure, resulting in the thickness of the diaphragm layer structure being too thin, and thus affecting A membrane negative electrode material with an integrated structure; in a preferred embodiment of the present invention, the distance between the syringe and the metal negative electrode is 10-20 cm.
  • the flow rate of the high-molecular polymer solution is 300-1000 ⁇ L/h. If the flow rate of the high-molecular polymer solution is too fast, the uniformity of the spun fiber on the surface of the metal negative electrode will be affected, and the integration will be affected.
  • the performance of the structured diaphragm negative electrode material affects the contact between the polymer diaphragm layer and the metal negative electrode, and cannot well suppress the problem of volume expansion and pulverization of the negative metal negative electrode during use, thereby affecting the safety performance of the secondary battery; If the flow rate of the high molecular polymer solution is too slow, it will affect the continuity of the spinning fiber and cause the high molecular diaphragm layer to be easily broken, and thus it cannot be guaranteed that the metal negative electrode will not form burrs and pierce the diaphragm, affecting the The performance of the separator anode material of the integrated structure leads to the poor safety performance of the secondary battery.
  • the polymer membrane layer is a polymer spinning structure layer or a multi-layer polymer spinning structure layer.
  • the multi-layer polymer spinning structure layer is a multi-layer spinning structure layer of the same polymer material or a multi-layer spinning structure layer of different polymer materials.
  • the integrated structure of the separator negative electrode material includes a metal negative electrode, and a polymer separator layer bonded to any side of the metal negative electrode, wherein the polymer separator layer is a layer of polymer spun Silk structure layer. Combining a polymer spinning structure layer on the surface of the metal negative electrode as a polymer separator layer can better suppress the problem of volume expansion and pulverization of the negative metal negative electrode during use.
  • the membrane negative electrode material of the integrated structure includes a metal negative electrode, and a polymer membrane layer bonded to any side of the metal negative electrode, wherein the polymer membrane layer is a multilayer of the same polymer.
  • Material spinning structure layer The polymer separator layer is set as a multi-layer spinning structure layer of the same polymer material to form a separator material with higher flexibility, and further suppress the problem of volume expansion and powdering of the metal negative electrode.
  • the integrated structure of the separator negative electrode material includes a metal negative electrode, and a polymer separator layer bonded to any side of the metal negative electrode, wherein the polymer separator layer is a multilayer of different polymers. Material spinning structure layer.
  • the polymer membrane layer is set as a multi-layer spinning structure layer of different polymer materials. According to different needs, different polymer materials are selected to prepare different spinning structure layers, and the formed polymer membrane layer can be different The advantages of polymer spinning are combined to effectively optimize the performance of the integrated structure of the separator anode material, such as adjusting the binding force, wettability, porosity, flexibility and other properties, which is more conducive to a wide range of applications.
  • the method further includes drying the negative electrode material of the separator with the integrated structure under the condition of 30-100°C. More preferably, the dried material is cut into a certain size to prepare an integrated structure of the separator negative electrode material.
  • the present invention also provides a secondary battery.
  • the secondary battery includes a positive electrode, an integrated structured separator negative electrode material and an electrolyte; wherein the integrated structured separator negative electrode material is composed of the integrated structure
  • the structured separator negative electrode material is prepared by the preparation method or is the integrated structure separator negative electrode material.
  • the secondary battery includes a positive electrode, an integrated structured separator negative electrode material and an electrolyte; wherein the integrated structured separator negative electrode material is composed of the integrated structured separator negative electrode material
  • the preparation method is obtained by the preparation method or is the separator negative electrode material with the integrated structure.
  • the use of the above-mentioned integrated structure of the diaphragm negative electrode material or the battery negative electrode prepared by the preparation method of the above-mentioned integrated structure of the diaphragm negative electrode material is used as the negative electrode material of the secondary battery, which simplifies the internal structure and assembly process of the battery, and greatly improves the metal
  • the interface contact characteristics of the negative electrode and the separator, the prepared secondary battery ensures that the metal negative electrode material is not easy to pulverize and can maintain integrity; at the same time, the effective contact distance between the metal negative electrode and the separator is increased, and the cycle stability of the secondary battery is enhanced. Coulomb efficiency.
  • the secondary battery includes a positive electrode, a separator negative electrode material with an integrated structure, and an electrolyte.
  • the integrated structured separator negative electrode material is the integrated structured separator negative electrode material or is prepared by the integrated structured separator negative electrode material preparation method.
  • the negative electrode material of the integrated structure includes a metal negative electrode, and a polymer separator layer bonded to any side of the metal negative electrode.
  • the separator layer is a polymer
  • the diaphragm layer and the polymer diaphragm layer have good flexibility, certain toughness and controllable porosity, which can better suppress the volume expansion and powdering of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form The burr pierces the diaphragm to ensure the safety performance of the secondary battery;
  • the polymer diaphragm layer is combined with the metal negative electrode through a spinning process to form an integrated structure, so that the diaphragm and the metal negative electrode are combined, It further increases the effective contact between the separator and the metal negative electrode, and makes the thickness and shape of the prepared integrated structure of the separator negative electrode material can be designed at will, with good flexibility, and to a certain extent inhibit the metal
  • the foil negative electrode is
  • the positive electrode is made by coating a positive electrode material on a metal foil current collector.
  • the positive electrode material is selected from lithium-containing metal oxides, lithium manganese oxide, lithium cobalt oxide, lithium iron phosphate, ternary materials, natural graphite, activated carbon, carbon nanotubes, graphene, activated carbon fibers, carbon molecular sieves, mesoporous At least one of carbon, carbon foam, and expanded graphite.
  • the metal foil current collector is selected from any one of aluminum, tin, magnesium, zinc, copper, iron, nickel, titanium, manganese, antimony, and bismuth, or an alloy containing at least one of the foregoing metal elements. Further preferably, the thickness of the metal foil current collector is 10-1000 ⁇ m.
  • the electrolyte level contains a solution of a certain concentration of electrolyte salt.
  • concentration of the electrolyte salt in the electrolyte is 0.1-10 mol/L.
  • the electrolyte salt is selected from one or more of lithium salt, sodium salt, potassium salt, and calcium salt.
  • the decomposing salt is selected from lithium hexafluorophosphate, potassium hexafluorophosphate, sodium hexafluorophosphate, calcium hexafluorophosphate, lithium tetrafluoroborate, potassium tetrafluoroborate, sodium tetrafluoroborate, lithium fluoride , One or more of lithium perchlorate, lithium oxalate borate, lithium difluorooxalate borate, etc.
  • the solvent of the electrolyte is selected from organic solvents or ionic liquids.
  • the organic solvent is selected from one or more of esters, ethers, sulfones, and nitriles.
  • the organic solvent is selected from propylene carbonate (PC), ethylene carbonate (EC), fluoroethylene carbonate (FEC), dimethyl carbonate (DMC), diethyl carbonate ( DEC), ethyl methyl carbonate (EMC), ethyl acetate (EA), methyl acetate (MA), methyl formate (MF), methyl propionate (MP), ethyl propionate (EP), tetrahydrofuran ( THF), Dimethoxymethane (DMM), 1,3-Dioxolane (DOL), 4-Methyl-1,3-dioxolane (4MeDOL), 1,2-Dimethoxypropane (DMP), dimethyl ether (DME),
  • PC propylene carbonate
  • EC
  • the ionic liquid includes 1-ethyl-3-methylimidazole-hexafluorophosphate, 1-butyl-1-methylpyrrolidine-bistrifluoromethylsulfonimide Salt, 1-ethyl-3-methylimidazole-tetrafluoroborate, 1-butyl-1-methylimidazole-hexafluorophosphate, 1-propyl-3-methylimidazole-hexafluorophosphate , N-methyl, butyl piperidine-bistrifluoromethanesulfonimide salt, N-methyl-N-propylpyrrolidine-bistrifluoromethanesulfonimide salt, 1-propyl-3 -Methylimidazole-bistrifluoromethanesulfonimide salt, 1-propyl-3-methylimidazole-tetrafluoroborate, 1-ethyl-3-methylimidazole-bistrifluoromethanesulfon
  • the present invention also provides a method for preparing a secondary battery, which includes the following steps:
  • G01 Grind the positive electrode active material, binder and conductive carbon black into a slurry according to a certain ratio, and coat it on the metal foil current collector, then dry and cut to obtain the desired size of the positive electrode;
  • G03. Provide the diaphragm negative electrode material of the integrated structure of the present invention, and cut the diaphragm negative electrode material of the integrated structure to obtain the diaphragm negative electrode material of the integrated structure of a suitable size;
  • Charge and discharge the secondary battery prepared by the preparation method of the secondary battery and set different cycle times of charge and discharge, and further test and analyze the performance of the secondary battery.
  • a metal aluminum foil as a metal negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
  • the electrospinning power supply voltage is set to 15kV
  • the distance between the syringe and the metal negative electrode is 15cm
  • the flow rate of the polymer solution is controlled to 600 ⁇ L/h.
  • the integrated structure of the separator negative electrode material is a single-layered polymer material with a spinning structure layer.
  • a new battery is assembled by using the separator negative electrode material of the integrated structure prepared in the above-mentioned Example 1 through matching with the positive electrode.
  • the prepared positive electrode, positive electrode battery case, integrated structure of the separator and negative electrode materials are closely stacked in a certain order, the electrolyte is dripped to completely infiltrate the separator, and finally the assembly of the lithium ion battery is completed by packaging.
  • the electrospinning power supply voltage is set to 15kV
  • the distance between the syringe and the metal negative electrode is 15cm
  • the flow rate of the polymer solution is controlled to 600 ⁇ L/h.
  • the integrated structure of the separator negative electrode material is a single-layered polymer material with a spinning structure layer.
  • a new battery is assembled by using the integrated structure separator negative electrode material prepared in the above-mentioned Example 2 through matching with the positive electrode.
  • EC ethylene carbonate
  • EMC ethyl methyl carbonate
  • DMC dimethyl carbonate
  • the prepared positive electrode and the positive electrode battery case, the integrated structure of the separator and negative electrode materials are closely stacked in a certain order, the electrolyte is dripped to make the separator completely infiltrated, and finally the assembly of the lithium ion battery is completed by packaging.
  • a metal tin foil as a metal negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
  • the electrospinning power supply voltage is set to 15kV
  • the distance between the syringe and the metal negative electrode is 15cm
  • the flow rate of the polymer solution is controlled to 600 ⁇ L/h.
  • the integrated structure of the separator negative electrode material is a single-layered polymer material with a spinning structure layer.
  • the prepared positive electrode, the positive electrode battery case, the integrated structure of the separator and the negative electrode material are closely stacked in a certain order, the electrolyte is dripped to make the separator completely infiltrated, and finally the potassium dual-ion battery is assembled by packaging.
  • a metal aluminum foil as a metal negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
  • the structured separator negative electrode material 3 is composed of two spinning structure layers of different polymer materials, namely a spinning structure layer 3-1 of polyvinyl alcohol material and a spinning structure layer 3-2 of polyacrylonitrile material.
  • the prepared positive electrode and the positive electrode battery case, the integrated structure of the separator and negative electrode materials are closely stacked in a certain order, the electrolyte is dripped to make the separator completely infiltrated, and finally the assembly of the lithium ion battery is completed by packaging.
  • a metal aluminum foil as a metal negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
  • the negative electrode material as shown in Figure 4, wherein the integrated structure of the separator negative electrode material 3 is three layers of spinning structure layers of different polymer materials, namely the polyvinyl phenol material structure layer 3-3, polyvinyl alcohol The spinning structure layer 3-1 of the material and the spinning structure layer 3-2 of the polyacrylonitrile material.
  • a new battery can be assembled by matching with the positive electrode.
  • the prepared positive electrode and the positive electrode battery case, the integrated structure of the separator and negative electrode materials are closely stacked in a certain order, the electrolyte is dripped to make the separator completely infiltrated, and finally the assembly of the lithium ion battery is completed by packaging.
  • Example 2 Compared with Example 1, in the process of preparing an integrated structure of the separator negative electrode material, the volume mass concentration of the polymer solution was changed from “10%” to "5%”. All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 2 Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery” is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 6 is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "6%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 1 in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 7 is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "7%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 1 in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 8 is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to “8%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 9 Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery” is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 9 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to “9%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 10 Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery” is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 10 is matched with the positive electrode to assemble a new battery". All other steps, materials used, and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "11%”. All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 1 in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 11 is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing an integrated structure of the negative electrode material for the separator, the volume mass concentration of the polymer solution was changed from “10%” to "12%”. All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 2 Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery” is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 12 is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "13%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 2 Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery” is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 13 is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "14%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 14 Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery” is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 14 is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 2 Compared with Example 1, in the process of preparing an integrated structure of the separator negative electrode material, the volume mass concentration of the polymer solution was changed from “10%” to “15%”, and all other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 1 in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 15 is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
  • Example 1 Compared with Example 1, the volume mass concentration of the high molecular polymer solution is the same as 10%, and a separate separator material is prepared, and the separator and the negative electrode are not integrated materials.
  • Example 2 Compared with Example 1, in the process of preparing a lithium dual-ion battery, a lithium dual-ion battery assembled in the form of a separator and a negative electrode separated is used.
  • Example 2 in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode” is modified to "Using the above embodiment 17.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
  • Example 2 in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 18 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
  • Example 2 in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 19 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
  • Example 2 in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode” is modified to "Using the above embodiment 20.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
  • Example 2 in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 21.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
  • Example 2 in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 22.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
  • Example 2 in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 23.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
  • Example 2 in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode” is modified to "Using the above embodiment 24.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
  • Example 2 Compared with Example 2, in the process of preparing a lithium dual-ion battery, a lithium-ion battery assembled with a separator and a negative electrode separated is used.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "3%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 26 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "4%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 27.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "5%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 28 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "6%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 29.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "7%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 30 The prepared integrated structure of the separator negative electrode material is matched with the positive electrode to assemble a new battery.” All other steps, materials used and process parameters are the same, and a potassium dual-ion battery is prepared.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to “8%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 31.
  • the prepared integrated structure of the diaphragm negative electrode material is matched with the positive electrode to assemble a new battery.” All other steps, materials used and process parameters are the same, and a potassium dual-ion battery is prepared.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to “9%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 32 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "11%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 33.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery.” All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing an integrated structure of the separator negative electrode material, the volume mass concentration of the polymer solution was changed from “10%” to "12%”. All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 34 The prepared negative electrode material of the integrated structure of the diaphragm is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution is changed from “10%” to "13%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 35.
  • the prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing an integrated structure of the negative electrode material for the separator, the volume mass concentration of the polymer solution was changed from “10%” to "14%”. All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 36 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from “10%” to "15%”. All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
  • Example 3 in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery” is modified to "Using the above embodiment 37 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery”. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
  • Example 3 Compared with Example 3, "the volume mass concentration of the polymer solution is 10%" is the same, and a separate separator material is prepared, and the separator and the negative electrode are not an integrated material.
  • Example 3 in the process of preparing the potassium dual ion battery, a potassium ion battery assembled in the form of separation of the separator and the negative electrode is used.
  • the secondary battery is prepared by using PP material as the separator, and the separator of the secondary battery is separated from the negative electrode material.
  • the secondary batteries prepared in the foregoing Examples 1 to 3 were respectively subjected to charge and discharge tests, and analyzed and compared.
  • the secondary batteries prepared in Example 1, Example 4, Example 5, and Example 6 to Example 16 were respectively subjected to charge and discharge tests, and analyzed and compared. The results are shown in Table 1 below, which can be obtained from Table 1.
  • the secondary battery prepared in Example 1 is a single-layer polymer material spun structure layer integrated structure separator anode material. When the number of cycles is 300, the capacity retention rate is 84%, and the coulombic efficiency is 95%;
  • the secondary battery prepared in Example 4 is an integrated structure of the separator anode material with a double-layer spinning structure layer of different polymer materials.
  • the secondary battery prepared in Example 5 is an integrated structure of the separator anode material with three layers of different polymer material spinning structure layers.
  • the capacity is maintained The rate is 70%, and the Coulomb efficiency is 87.2%.
  • the secondary batteries prepared in Analyzing Example 1, Example 6 to Example 15 can be obtained from Table 1.
  • the volume of the polyacrylonitrile (PAN) when the volume of the polyacrylonitrile (PAN) is When the mass concentration increases from 5% to 10%, the capacity retention and coulombic efficiency of the secondary battery prepared accordingly show an upward trend.
  • the volume mass concentration of the polyacrylonitrile (PAN) increases from 10% to 15% %, the capacity retention and coulombic efficiency of the secondary battery prepared accordingly show a downward trend.
  • the volume mass concentration of the polyacrylonitrile (PAN) is 10%
  • the prepared secondary battery (the prepared in Example 1 The capacity retention rate and coulombic efficiency of the secondary battery reached the maximum value, which were 84% and 95%, respectively.
  • Example 16 Analyze the secondary batteries prepared in Example 1 and Example 16. Among them, the volume mass concentration of polyacrylonitrile (PAN) used in Example 16 is the same as that in Example 1. The difference is that Example 16 is a diaphragm and The method of separating the negative electrode can be obtained from Table 1.
  • the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 16 are 60% and 80%, respectively, which are far lower than the capacity of the secondary battery prepared in Example 1. The retention rate and the Coulomb efficiency, therefore, indicate that the use of an integrated structure of the separator anode material can greatly improve the battery charge and discharge performance and safety performance of the secondary battery.
  • the secondary batteries prepared in Example 2 and Example 17 to Example 25 were respectively subjected to charge and discharge tests, and analyzed and compared. The results are shown in Table 2 below.
  • the secondary battery can be obtained from Table 2.
  • the capacity retention rate and coulombic efficiency of the secondary battery are 82% and 91.2, respectively %.
  • the capacity retention rate and coulombic efficiency of the secondary battery are 82% and 91.2, respectively %.
  • Example 25 Analyze the secondary batteries prepared in Example 2 and Example 25. Among them, the concentration ratio of PAN and PVDF used in Example 25 is the same as that in Example 2. The difference is that Example 25 uses a method in which the separator is separated from the negative electrode. As shown in Table 2, the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 25 are 63% and 76.1%, respectively, which are far lower than the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 2 Therefore, it shows that the use of an integrated structure of the separator anode material can greatly improve the battery charge and discharge performance and safety performance of the secondary battery.
  • the secondary batteries prepared in Example 3 and Example 26 to Example 38 were respectively subjected to charge and discharge tests, and analyzed and compared. The results are shown in Table 3 below.
  • the results are prepared in Example 3 and Example 26 to Example 37
  • the secondary battery can be obtained from Table 3.
  • the capacity retention rate and the coulombic efficiency of the secondary battery are 80% and 81.0, respectively %.
  • the capacity retention rate and coulombic efficiency of the secondary battery prepared accordingly also change.
  • the volume mass concentration of PAN rises from 3% to 10%, the capacity retention and coulombic efficiency of the secondary battery prepared accordingly show an upward trend.
  • Example 38 Analyze the secondary batteries prepared in Example 3 and Example 38. Among them, the volume mass concentration of PAN used in Example 38 is the same as that in Example 3. The difference is that Example 38 uses a method in which the separator is separated from the negative electrode. From Table 3, the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 38 are 60% and 70%, respectively, which are far lower than the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 3 Therefore, it is explained that the use of an integrated structure of the separator negative electrode material can greatly improve the battery charging and discharging performance and safety performance of the secondary battery.
  • the integrated structure diaphragm anode material and the secondary battery prepared in Example 1 are further analyzed, and the integrated structure diaphragm anode material prepared in Example 1 is analyzed, and it can be obtained from the electron microscope analysis that the integrated structure
  • the morphology of the polymer spinning structure layer of the separator negative electrode material is shown in Figure 6, and the cross-sectional schematic diagram of the polymer spinning structure layer of the integrated structure separator negative electrode material is shown in Figure 7, from Figures 6 and 7
  • the morphology of the separator anode material with integrated structure can be clearly analyzed. Further analysis of the charge-discharge cycle stability performance of the secondary battery containing the separator negative electrode material of the integrated structure prepared in Example 1 and the secondary battery whose separator material is a PP separator.
  • Example 1 is the integrated structure of Example 1
  • the spun separator of the negative electrode material of the separator is the spun separator of the integrated structure of the negative electrode material of the separator described in Example 2
  • (c) is the PP separator, which can be judged by the color in Figure 8, (a) And (b) infiltration is more thorough, and the infiltration effect is better than (c).
  • the negative electrode material of the integrated structure of the separator includes a metal negative electrode, and a polymer separator layer bonded to either side of the metal negative electrode.
  • the separator layer is The polymer membrane layer, the polymer membrane layer has good flexibility, and has a certain degree of toughness and controllable porosity, which can better inhibit the volume expansion and pulverization of the negative metal negative electrode during use, and ensure that the metal negative electrode is not It will form burrs and pierce the diaphragm to ensure the safety performance of the secondary battery;
  • the polymer diaphragm layer is combined with the metal negative electrode through a spinning process to form an integrated structure, so that both the diaphragm and the metal negative electrode are combined.
  • the combination further increases the effective contact between the separator and the metal negative electrode, and the thickness and shape of the prepared integrated structure separator negative electrode material can be designed at will, and the flexibility is good, which to a certain extent prevents the secondary battery from cycling.
  • the metal foil negative electrode is easy to cause the problem of swelling and pulverization, which improves the safety performance and coulomb efficiency of the secondary battery.

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Abstract

A diaphragm-negative electrode material of an integrated structure, and a preparation method therefor. The preparation method comprises the following steps: preparing a high-molecular polymer solution and putting same in an injector (2) of an electrostatic spinning apparatus; and placing a metal negative electrode (4) inside the electrostatic spinning apparatus, setting the power source voltage of electrostatic spinning to be 5-30 kV, and the distance between the injector (2) and the metal negative electrode (4) to be 5-50 cm, controlling the flow rate of the high-molecular polymer solution to be 300-1000 μL/h, and preparing a high-molecular diaphragm layer (3) on the surface of the metal negative electrode (4) by means of electrostatic spinning, so as to obtain a diaphragm-negative electrode material of an integrated structure.

Description

一体化结构的隔膜负极材料及其制备方法和二次电池Diaphragm negative electrode material of integrated structure, preparation method thereof and secondary battery 技术领域Technical field
本发明涉及锂离子电池领域,尤其涉及一种一体化结构的隔膜负极材料及其制备方法和二次电池。The present invention relates to the field of lithium ion batteries, and in particular to a diaphragm negative electrode material with an integrated structure, a preparation method thereof, and a secondary battery.
背景技术Background technique
锂离子电池作为一种新型储能器件,具有高能量密度、长循环寿命、无记忆效应以及自放电小等优点,并广泛应用于各类便携式移动设备以及电动汽车中。锂离子电池主要由正负电极、隔膜、电解液等部分组成,并通过负极、隔膜、正极依次堆叠的形式进行组装。充电时,锂离子从正极材料中脱出,迁移到负极活性材料中;放电时,锂离子从负极活性材料中脱出,回到正极。传统锂离子电池负极通常以石墨作为活性物质,并以金属铜箔作为集流体。最近的研究表明,采用金属箔材作为负极,将负极活性物质和负极集流体进行一体化设计,这种新型的电池体系,能够有效降低电池的自重和体积,显著提高电池的质量和体积能量密度。As a new type of energy storage device, lithium-ion batteries have the advantages of high energy density, long cycle life, no memory effect, and small self-discharge, and are widely used in various portable mobile devices and electric vehicles. Lithium-ion batteries are mainly composed of positive and negative electrodes, separators, electrolyte and other parts, and are assembled by stacking negative electrodes, separators, and positive electrodes in sequence. When charging, lithium ions are removed from the positive electrode material and migrate to the negative electrode active material; when discharging, lithium ions are removed from the negative electrode active material and return to the positive electrode. Traditional lithium-ion battery negative electrodes usually use graphite as the active material and metal copper foil as the current collector. Recent studies have shown that the use of metal foil as the negative electrode and the integrated design of the negative electrode active material and the negative current collector. This new type of battery system can effectively reduce the weight and volume of the battery, and significantly improve the quality and volume energy density of the battery. .
然而,采用金属箔材作为负极,虽然有以上优点,但同时也存在着以下问题:(1)金属负极的合金化/去合金化过程容易造成体积膨胀及粉化现象;(2)金属负极在膨胀粉化的过程中产生的毛刺可能刺穿隔膜,导致安全问题;(3)金属负极表面所形成的SEI膜不断的生成-破裂-再生成,消耗大量的离子和电解液,造成电池的库伦效率低。However, the use of metal foil as a negative electrode has the above advantages, but it also has the following problems: (1) The alloying/dealloying process of the metal negative electrode is likely to cause volume expansion and pulverization; (2) The metal negative electrode is The burrs produced in the process of swelling and pulverization may pierce the separator and cause safety problems; (3) The SEI film formed on the surface of the metal negative electrode is continuously generated-broken-regenerated, consuming a large amount of ions and electrolyte, and causing the coulomb of the battery. low efficiency.
为了解决上述问题,目前已有多种相关的解决方法,包括高分子涂层、多孔化设计、高浓度电解液等。如有研究报道一种高分子涂层提高铝负极性能的方法。通过涂覆的高分子涂层抑制铝负极在充放电过程中的膨胀粉化,同时该涂层能够有效隔离电解液和铝负极,防止铝负极受到侵蚀和反应。该技术保证 了铝负极结构的完整性,缓解了铝负极体积膨胀粉化以及不稳定SEI膜不断再生引起的容量衰减问题。但是,高分子涂层能够抑制铝负极充放电过程中的体积膨胀粉化,且有效隔离电解液和铝负极,改善了SEI膜不断再生引起的容量衰减问题,但该技术下的高分子涂层与金属负极结合性能一般,效果有限,且操作过程较为复杂。又如,一种三维多孔金属负极,该负极的多孔结构设计具有较高的孔隙率和优良的空间结构。有利于缓解应力集中造成的金属负极膨胀粉化问题。同时,该结构具有很高的比表面积,在充放电过程中,能够增强电解液的储存与传输能力,有利于电化学反应的进行,提高了金属负极的利用效率。但是,三维多孔结构金属负极虽然能在充放电过程中起到缓解负极体积膨胀的作用,但这种多孔结构的合成制备工艺比较复杂,且SEI膜不断再生引起的容量衰减问题仍然存在。In order to solve the above problems, there are many related solutions, including polymer coating, porous design, high-concentration electrolyte and so on. If there is a research report on a method of polymer coating to improve the performance of aluminum anode. The coated polymer coating inhibits the expansion and pulverization of the aluminum negative electrode during charging and discharging, and at the same time, the coating can effectively isolate the electrolyte and the aluminum negative electrode, and prevent the aluminum negative electrode from being corroded and reacted. This technology ensures the integrity of the aluminum anode structure and alleviates the capacity attenuation caused by the volume expansion and pulverization of the aluminum anode and the continuous regeneration of the unstable SEI film. However, the polymer coating can inhibit the volume expansion and pulverization during the charging and discharging process of the aluminum anode, and effectively isolate the electrolyte from the aluminum anode, and improve the capacity attenuation caused by the continuous regeneration of the SEI film. However, the polymer coating under this technology The combination performance with the metal negative electrode is general, the effect is limited, and the operation process is more complicated. Another example is a three-dimensional porous metal negative electrode, the porous structure of the negative electrode is designed to have high porosity and excellent spatial structure. It is helpful to alleviate the problem of metal negative electrode expansion and powdering caused by stress concentration. At the same time, the structure has a high specific surface area, which can enhance the storage and transport capacity of the electrolyte during the charge and discharge process, facilitate the progress of the electrochemical reaction, and improve the utilization efficiency of the metal negative electrode. However, although the metal anode with a three-dimensional porous structure can play a role in alleviating the volume expansion of the anode during the charge and discharge process, the synthesis and preparation process of this porous structure is more complicated, and the problem of capacity attenuation caused by the continuous regeneration of the SEI film still exists.
再如,一种使用高浓度电解液提高金属负极循环寿命的方法。在充放电的过程中,高浓度电解液能够在金属负极表面形成结构稳定的SEI膜,从而提高金属负极材料的使用寿命,以及新型电池的比容量和循环稳定性。此外,采用高浓度电解液能够有效提高电解液的电化学窗口。然而,采用高浓度电解液虽然也能提高金属负极的循环稳定性,但高浓度电解液对常规隔膜材料浸润性不足,在实际使用过程中并不理想。因此,目前的制备方法仍然不能完全解决金属负极存在的问题。For another example, a method for improving the cycle life of a metal negative electrode using a high-concentration electrolyte. In the process of charging and discharging, the high-concentration electrolyte can form a structurally stable SEI film on the surface of the metal negative electrode, thereby improving the service life of the metal negative electrode material and the specific capacity and cycle stability of the new battery. In addition, the use of high-concentration electrolyte can effectively increase the electrochemical window of the electrolyte. However, although the use of high-concentration electrolyte can also improve the cycle stability of the metal negative electrode, the high-concentration electrolyte has insufficient wettability for conventional separator materials, which is not ideal in actual use. Therefore, the current preparation method still cannot completely solve the problems existing in the metal negative electrode.
发明内容Summary of the invention
本发明的目的在于提供一种一体化结构的隔膜负极材料及其制备方法和二次电池,旨在解决现有技术中金属箔材负极易造成膨胀粉化,形成毛刺而刺穿隔膜,导致电池安全性能差和库伦效率低的问题。The purpose of the present invention is to provide a separator negative electrode material with an integrated structure, a preparation method thereof, and a secondary battery. Poor battery safety performance and low Coulomb efficiency.
为实现上述发明目的,本发明采用的技术方案如下:In order to achieve the above-mentioned purpose of the invention, the technical solutions adopted by the present invention are as follows:
一种一体化结构的隔膜负极材料的制备方法,所述制备方法包括如下步骤:A method for preparing a separator anode material with an integrated structure. The preparation method includes the following steps:
配制高分子聚合物溶液并置于静电纺丝装置的注射器中;Prepare the high molecular polymer solution and place it in the syringe of the electrostatic spinning device;
将所述金属负极放置于静电纺丝装置设备内,设置静电纺丝的电源电压为5~30kV,所述注射器与所述金属负极的距离为5~50cm,控制所述高分子聚合物溶液的流速为300~1000μL/h,在所述金属负极的表面静电纺丝制备高分子隔膜层,得到所述一体化结构的隔膜负极材料。Place the metal negative electrode in an electrospinning device, set the electrospinning power supply voltage to be 5-30kV, the distance between the syringe and the metal negative electrode is 5-50cm, and control the polymer solution The flow rate is 300-1000 μL/h, and the polymer diaphragm layer is prepared by electrostatic spinning on the surface of the metal negative electrode to obtain the diaphragm negative electrode material of the integrated structure.
以及,一种一体化结构的隔膜负极材料,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层。And, an integrated structured separator negative electrode material, the integrated structured separator negative electrode material includes a metal negative electrode, and a polymer separator layer bonded on any side of the metal negative electrode.
以及,一种二次电池,所述二次电池包括正极,一体化结构的隔膜负极材料以及电解液;其中,所述一体化结构的隔膜负极材料由所述的一体化结构的隔膜负极材料的制备方法制备获得的或为所述的一体化结构的隔膜负极材料。And, a secondary battery, the secondary battery comprising a positive electrode, an integrated structure of the separator negative electrode material and an electrolyte; wherein the integrated structure of the separator negative electrode material is made of the integrated structure of the separator negative electrode material The preparation method is prepared or obtained by the separator negative electrode material of the integrated structure.
本发明所述一体化结构的隔膜负极材料的制备方法,先配制高分子聚合物溶液,采用静电纺丝的制备方法,通过控制所述静电纺丝的电源电压、注射器与所述金属负极的距离以及所述高分子聚合物溶液的流速制备得到所述一体化结构的隔膜负极材料,首先,所述高分子聚合物溶液为隔膜的原材料,高分子聚合物具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题,保证金属负极不会形成毛刺而刺穿隔膜,保证二次电池的安全性能;其次,通过静电纺丝工艺与所述金属负极结合形成一体化结构,使隔膜与金属负极负极二者进行结合,进一步增加了高分子隔膜层与金属负极负极之间的有效接触,并且使制备得到的一体化结构的隔膜负极材料的厚度和形状可随意设计,柔韧性良好,一定程度上抑制了二次电池循环中,金属箔材负极易造成膨胀粉化的问题,提高二次电池安全性能和库伦效率。所述制备方法材料易得,生产方法环保,生产工艺简单条件可控。The preparation method of the diaphragm negative electrode material of the integrated structure of the present invention firstly prepares a high molecular polymer solution, adopts the preparation method of electrostatic spinning, and controls the power supply voltage of the electrostatic spinning and the distance between the syringe and the metal negative electrode. And the flow rate of the high molecular polymer solution to prepare the integrated structure of the negative electrode material for the diaphragm. Porosity and controllable porosity can better suppress the volume expansion and pulverization of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form burrs and pierce the separator, ensuring the safety performance of the secondary battery; secondly, through The electrospinning process is combined with the metal negative electrode to form an integrated structure, so that the diaphragm and the metal negative electrode are combined, which further increases the effective contact between the polymer diaphragm layer and the metal negative electrode, and makes the obtained integrated structure The thickness and shape of the structured separator anode material can be designed at will, and the flexibility is good, which to a certain extent inhibits the problem of expansion and pulverization of the metal foil anode during the cycle of the secondary battery, and improves the safety performance and coulomb efficiency of the secondary battery. . The preparation method materials are easily available, the production method is environmentally friendly, and the production process is simple and the conditions are controllable.
本发明所述一体化结构的隔膜负极材料,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层,所述隔膜层为高分子隔膜层,高分子隔膜层具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题, 保证金属负极不会形成毛刺而刺穿隔膜,保证二次电池的安全性能;且高分子隔膜层与金属负极直接结合,进一步增加了隔膜与金属负极负极之间的有效接触,并且使制备得到的一体化结构的隔膜负极材料的厚度和形状可随意设计,柔韧性良好,一定程度上抑制了二次电池循环中,金属箔材负极易造成膨胀粉化的问题,提高二次电池安全性能和库伦效率。According to the integrated structure of the negative electrode material of the separator of the present invention, the negative electrode material of the integrated structure of the separator includes a metal negative electrode, a polymer separator layer bonded to any side of the metal negative electrode, and the separator layer is a polymer separator layer, The polymer separator layer has good flexibility, and has a certain degree of toughness and controllable porosity, which can better inhibit the volume expansion and powdering of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form burrs and thorns. Wear the diaphragm to ensure the safety performance of the secondary battery; and the polymer diaphragm layer is directly combined with the metal negative electrode, which further increases the effective contact between the diaphragm and the metal negative electrode, and makes the thickness of the prepared integrated structure of the diaphragm negative electrode material And the shape can be designed at will, the flexibility is good, to a certain extent, the secondary battery cycle, the metal foil negative electrode is easy to cause the problem of swelling and powdering, and the safety performance and coulomb efficiency of the secondary battery are improved.
本发明所述的二次电池,所述二次电池包括正极,一体化结构的隔膜负极材料以及电解液;其中,所述一体化结构的隔膜负极材料由所述的一体化结构的隔膜负极材料的制备方法制备获得的或为所述的一体化结构的隔膜负极材料。采用上述一体化结构的隔膜负极材料或由上述一体化结构的隔膜负极材料的制备方法制备得到的电池负极作为所述二次电池的负极材料,简化电池内部结构和装配工艺,极大改善了金属负极与隔膜的界面接触特性,制备得到的二次电池,保证金属负极材料不易粉化,能够保持完整性;同时提高金属负极与隔膜之间有效地接触距离,增强二次电池的循环稳定性和库伦效率。In the secondary battery of the present invention, the secondary battery includes a positive electrode, an integrated structured separator negative electrode material and an electrolyte; wherein the integrated structured separator negative electrode material is composed of the integrated structured separator negative electrode material The preparation method is obtained by the preparation method or is the separator negative electrode material with the integrated structure. The use of the above-mentioned integrated structure of the diaphragm negative electrode material or the battery negative electrode prepared by the preparation method of the above-mentioned integrated structure of the diaphragm negative electrode material is used as the negative electrode material of the secondary battery, which simplifies the internal structure and assembly process of the battery, and greatly improves the metal The interface contact characteristics of the negative electrode and the separator, the prepared secondary battery ensures that the metal negative electrode material is not easy to pulverize and can maintain integrity; at the same time, the effective contact distance between the metal negative electrode and the separator is increased, and the cycle stability of the secondary battery is enhanced. Coulomb efficiency.
附图说明Description of the drawings
图1是本发明实施例提供的一体化结构的隔膜负极材料的结构示意图。FIG. 1 is a schematic diagram of the structure of a separator negative electrode material with an integrated structure provided by an embodiment of the present invention.
图2是本发明实施例提供的静电纺丝装置的设备图。Fig. 2 is an equipment diagram of an electrospinning device provided by an embodiment of the present invention.
图3是本发明实施例4提供的包括2层高分子隔膜层的一体化结构的隔膜负极材料的结构示意图。FIG. 3 is a schematic structural diagram of a separator negative electrode material with an integrated structure including two polymer separator layers provided by Embodiment 4 of the present invention.
图4是本发明实施例5提供的包括3层高分子隔膜层的一体化结构的隔膜负极材料的结构示意图。4 is a schematic structural diagram of a separator negative electrode material with an integrated structure including three polymer separator layers provided by Embodiment 5 of the present invention.
图5是本发明实施例提供的二次电池的结构示意图。Fig. 5 is a schematic structural diagram of a secondary battery provided by an embodiment of the present invention.
图6是本发明实施例提供的一体化结构的隔膜负极材料的电镜图。Fig. 6 is an electron micrograph of a separator negative electrode material with an integrated structure provided by an embodiment of the present invention.
图7是本发明实施例提供的一体化结构的隔膜负极材料的横截面图。FIG. 7 is a cross-sectional view of a separator negative electrode material with an integrated structure provided by an embodiment of the present invention.
图8是本发明实施例1提供的二次电池的充放电的性能分析图。FIG. 8 is a performance analysis diagram of charging and discharging of the secondary battery provided in Example 1 of the present invention.
图9是本发明对比例提供的二次电池的充放电的性能分析图。Fig. 9 is a performance analysis diagram of the charging and discharging of the secondary battery provided by the comparative example of the present invention.
图10是本发明实施例1、实施例2提供的一体化结构的隔膜负极材料的浸润性分析图。FIG. 10 is an analysis diagram of the wettability of the separator negative electrode material of the integrated structure provided in the embodiment 1 and the embodiment 2 of the present invention.
具体实施方式Detailed ways
为使本发明实施例的目的、技术方案和技术效果更加清楚,下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。结合本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the objectives, technical solutions and technical effects of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be described clearly and completely below. Obviously, the described embodiments are part of the embodiments of the present invention, not All examples. In combination with the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work shall fall within the protection scope of the present invention.
在本发明的描述中,需要理解的是,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括一个或者更多个该特征。在本发明的描述中,“多个”的含义是两个或两个以上,除非另有明确具体的限定。In the description of the present invention, it should be understood that the terms "first" and "second" are only used for description purposes, and cannot be understood as indicating or implying relative importance or implicitly indicating the number of indicated technical features. Thus, the features defined with "first" and "second" may explicitly or implicitly include one or more of these features. In the description of the present invention, "plurality" means two or more than two, unless otherwise specifically defined.
本发明实例提供一种一体化结构的隔膜负极材料,如图1所示,所述一体化结构的隔膜负极材料包括一金属负极4,结合在所述金属负极任意一面的高分子隔膜层3,其中,所述高分子隔膜层通过纺丝工艺与所述金属负极结合形成一体化结构。An example of the present invention provides a separator negative electrode material with an integrated structure. As shown in FIG. Wherein, the polymer diaphragm layer is combined with the metal negative electrode through a spinning process to form an integrated structure.
本发明所述一体化结构的隔膜负极材料,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层,所述隔膜层为高分子隔膜层,高分子隔膜层具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题,保证金属负极不会形成毛刺而刺穿隔膜,保证二次电池的安全性能;且高分子隔膜层与金属负极直接结合,进一步增加了隔膜与金属负极负极之间的有效接触,并且使制备得到的一体化结构的隔膜负极材料的厚度和形状可随意设计,柔韧性良好,一定程度上抑制了二次电池循环中,金属箔材负极易造成膨胀粉 化的问题,提高二次电池安全性能和库伦效率。According to the integrated structure of the negative electrode material of the separator of the present invention, the negative electrode material of the integrated structure of the separator includes a metal negative electrode, a polymer separator layer bonded to any side of the metal negative electrode, and the separator layer is a polymer separator layer, The polymer separator layer has good flexibility, and has a certain degree of toughness and controllable porosity, which can better suppress the volume expansion and pulverization of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form burrs and thorns. Wear the diaphragm to ensure the safety performance of the secondary battery; and the polymer diaphragm layer is directly combined with the metal negative electrode, which further increases the effective contact between the diaphragm and the metal negative electrode, and makes the thickness of the prepared integrated structure of the diaphragm negative electrode material And the shape can be designed at will, the flexibility is good, to a certain extent, the secondary battery cycle, the metal foil negative electrode is easy to cause the problem of swelling and powdering, and the safety performance and coulomb efficiency of the secondary battery are improved.
优选的,所述金属负极选自负极集流体和负极材料一体化的金属负极,以所述金属负极同时作为负极集流体和负极材料,将负极活性物质和集流体进行一体化设计的新型电池体系,能够有效降低电池的自重和体积,显著提高电池的质量和体积能量密度,并大幅度降低电池的生产制造成本。Preferably, the metal negative electrode is selected from a metal negative electrode in which a negative electrode current collector and a negative electrode material are integrated, and the metal negative electrode is used as a negative electrode current collector and a negative electrode material at the same time, and the negative electrode active material and the current collector are integratedly designed as a new type of battery system , Can effectively reduce the weight and volume of the battery, significantly improve the quality and volume energy density of the battery, and greatly reduce the production cost of the battery.
优选的,所述金属负极的材料选自铝、锡、镁、锌、铜、铁、镍、钛、锰、锑、铋等发生合金化电池反应的的一种或含有至少一种所述金属元素的合金。进一步优选的,所述金属负极的厚度为10~1000μm。在本发明优选实施例中,所述金基材的材料选自厚度为50μm的铝材料。Preferably, the material of the metal negative electrode is selected from one of aluminum, tin, magnesium, zinc, copper, iron, nickel, titanium, manganese, antimony, bismuth, etc. that undergo alloying battery reactions, or contains at least one of the metals The alloy of the elements. Further preferably, the thickness of the metal negative electrode is 10-1000 μm. In a preferred embodiment of the present invention, the material of the gold substrate is selected from aluminum materials with a thickness of 50 μm.
优选的,所述金属负极选自未经过预处理的金属负极或经过预处理的金属负极。进一步优选的,所述经过预处理的金属负极选自经过抛光的金属负极、经过打磨处理的金属负极、经过喷砂处理的金属负极、进过等离子体处理的金属负极的任意一种。选择经过预处理的金属负极作为负极材料,能够进一步提高金属负极与所述高分子隔膜层的结合能力,提高所述制备得到的一体化结构的隔膜负极材料的整体性能,保证黏附性更强,金属负极与高分子隔膜层之间不易脱落。Preferably, the metal negative electrode is selected from a metal negative electrode that has not undergone pretreatment or a metal negative electrode that has undergone pretreatment. Further preferably, the pretreated metal negative electrode is selected from any one of a polished metal negative electrode, a polished metal negative electrode, a sandblasted metal negative electrode, and a plasma-treated metal negative electrode. Selecting the pretreated metal negative electrode as the negative electrode material can further improve the binding capacity of the metal negative electrode and the polymer separator layer, improve the overall performance of the prepared integrated structure separator negative electrode material, and ensure stronger adhesion. It is not easy to fall off between the metal negative electrode and the polymer separator layer.
具体的,结合在所述金属负极任意一面的高分子隔膜层,高分子隔膜层具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题,保证金属负极不会形成毛刺而刺穿隔膜,保证二次电池的安全性能。Specifically, combined with the polymer separator layer on either side of the metal negative electrode, the polymer separator layer has good flexibility, and has certain toughness and controllable porosity, which can better inhibit the use of the negative metal negative electrode. The problem of medium volume expansion and pulverization ensures that the metal negative electrode will not form burrs and pierce the separator, ensuring the safety performance of the secondary battery.
优选的,所述高分子隔膜层的材料选自聚甲基丙烯酸甲酯、丙烯酸四氢全氟辛酯、聚乙烯醇、聚乙烯基苯酚、聚氯乙烯、聚乙烯咔唑、聚偏二氟乙烯、聚偏二氟乙烯-六氟丙烯、聚丙烯腈、聚乳酸的至少一种。选择能表现出一定的柔性,坚韧性和可控的孔隙率的高分子聚合物作为高分子隔膜层的原材料,确保制备得到的高分子隔膜层具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题。Preferably, the material of the polymer diaphragm layer is selected from polymethyl methacrylate, tetrahydroperfluorooctyl acrylate, polyvinyl alcohol, polyvinyl phenol, polyvinyl chloride, polyvinyl carbazole, polyvinylidene fluoride At least one of ethylene, polyvinylidene fluoride-hexafluoropropylene, polyacrylonitrile, and polylactic acid. Select high molecular polymers that can exhibit a certain degree of flexibility, toughness and controllable porosity as the raw material of the polymer membrane layer to ensure that the prepared polymer membrane layer has good flexibility, and has certain toughness and flexibility. The controlled porosity can better suppress the volume expansion and pulverization of the negative metal negative electrode during use.
优选的,所述高分子隔膜层的厚度为50μm~150μm。若所述高分子隔膜层厚度太薄,则所述隔膜层容易击穿或者易破碎,进而影响制备得到的二次电池的安全性能;若所述高分子隔膜层的厚度太厚,则会导致制备得到的二次电池的离子电导率会降低,影响电池的性能。Preferably, the thickness of the polymer membrane layer is 50 μm to 150 μm. If the thickness of the polymer separator layer is too thin, the separator layer is easy to break down or break, thereby affecting the safety performance of the prepared secondary battery; if the thickness of the polymer separator layer is too thick, it will cause The ionic conductivity of the prepared secondary battery will decrease, which affects the performance of the battery.
优选的,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层,其中,所述高分子隔膜层通过纺丝工艺与所述金属负极结合形成一体化结构。在本发明优选实施例中,所述纺丝工艺选自静电纺丝工艺。Preferably, the integrated structure of the separator negative electrode material includes a metal negative electrode, and a polymer separator layer bonded to either side of the metal negative electrode, wherein the polymer separator layer is formed by combining with the metal negative electrode through a spinning process Integrated structure. In a preferred embodiment of the present invention, the spinning process is selected from the electrospinning process.
本发明实施例提供的一体化结构的隔膜负极材料,可以通过下述方法制备获得。The separator anode material with the integrated structure provided by the embodiment of the present invention can be prepared by the following method.
相应的,本发明实施例还提供了一种一体化结构的隔膜负极材料的制备方法。该方法包括如下步骤:Correspondingly, the embodiment of the present invention also provides a method for preparing a separator negative electrode material with an integrated structure. The method includes the following steps:
S01.配制高分子聚合物溶液并置于静电纺丝装置的注射器中;S01. Prepare a high molecular polymer solution and place it in the syringe of the electrostatic spinning device;
S02.将所述金属负极放置于静电纺丝装置设备内,设置静电纺丝的电源电压为5~30kV,所述注射器与所述金属负极的距离为5~50cm,控制所述高分子聚合物溶液的流速为300~1000μL/h,在所述金属负极的表面静电纺丝制备高分子隔膜层,得到所述一体化结构的隔膜负极材料。S02. Place the metal negative electrode in the electrospinning device, set the electrospinning power supply voltage to be 5-30kV, the distance between the syringe and the metal negative electrode is 5-50cm, and control the polymer The flow rate of the solution is 300-1000 μL/h, and the polymer diaphragm layer is prepared by electrostatic spinning on the surface of the metal negative electrode to obtain the diaphragm negative electrode material of the integrated structure.
本发明所述一体化结构的隔膜负极材料的制备方法,先配制高分子聚合物溶液,采用静电纺丝的制备方法,通过控制所述静电纺丝的电源电压、注射器与所述金属负极的距离以及所述高分子聚合物溶液的流速制备得到所述一体化结构的隔膜负极材料,首先,所述高分子聚合物溶液为隔膜的原材料,高分子聚合物具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题,保证金属负极不会形成毛刺而刺穿隔膜,保证二次电池的安全性能;其次,通过静电纺丝工艺与所述金属负极结合形成一体化结构,使隔膜与金属负极负极二者进行结合,进一步增加了高分子隔膜层与金属负极负极之间的有效接触,并且使制备得到的一体 化结构的隔膜负极材料的厚度和形状可随意设计,柔韧性良好,一定程度上抑制了二次电池循环中,金属箔材负极易造成膨胀粉化的问题,提高二次电池安全性能和库伦效率。所述制备方法材料易得,生产方法环保,生产工艺简单条件可控。The preparation method of the diaphragm negative electrode material of the integrated structure of the present invention firstly prepares a high molecular polymer solution, adopts the preparation method of electrostatic spinning, and controls the power supply voltage of the electrostatic spinning and the distance between the syringe and the metal negative electrode. And the flow rate of the high molecular polymer solution to prepare the integrated structure of the negative electrode material for the diaphragm. Porosity and controllable porosity can better suppress the volume expansion and pulverization of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form burrs and pierce the separator, ensuring the safety performance of the secondary battery; secondly, through The electrospinning process is combined with the metal negative electrode to form an integrated structure, so that the diaphragm and the metal negative electrode are combined, which further increases the effective contact between the polymer diaphragm layer and the metal negative electrode, and makes the obtained integrated structure The thickness and shape of the structured separator anode material can be designed at will, and the flexibility is good, which to a certain extent inhibits the problem of expansion and pulverization of the metal foil anode during the cycle of the secondary battery, and improves the safety performance and coulomb efficiency of the secondary battery. . The preparation method materials are easily available, the production method is environmentally friendly, and the production process is simple and the conditions are controllable.
具体的,在上述步骤S01中,配制高分子聚合物溶液,优选的,所述高分子聚合物溶液包括高分子聚合物溶质、添加剂和溶剂。Specifically, in the above step S01, a high-molecular polymer solution is prepared. Preferably, the high-molecular polymer solution includes a high-molecular polymer solute, an additive, and a solvent.
优选的,所述高分子聚合物溶液包括高分子聚合物溶质,所述高分子聚合物溶质选自聚甲基丙烯酸甲酯、丙烯酸四氢全氟辛酯、聚乙烯醇、聚乙烯基苯酚、聚氯乙烯、聚乙烯咔唑、聚偏二氟乙烯、聚偏二氟乙烯-六氟丙烯、聚丙烯腈、聚乳酸的至少一种。选择能表现出一定的柔性,坚韧性和可控的孔隙率的高分子聚合物作为高分子隔膜层的原材料,确保制备得到的高分子隔膜层具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题。Preferably, the high molecular polymer solution includes a high molecular polymer solute selected from the group consisting of polymethyl methacrylate, tetrahydroperfluorooctyl acrylate, polyvinyl alcohol, polyvinyl phenol, At least one of polyvinyl chloride, polyvinylcarbazole, polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene, polyacrylonitrile, and polylactic acid. Select high molecular polymers that can exhibit a certain degree of flexibility, toughness and controllable porosity as the raw material of the polymer membrane layer to ensure that the prepared polymer membrane layer has good flexibility, and has certain toughness and flexibility. The controlled porosity can better suppress the volume expansion and pulverization of the negative metal negative electrode during use.
优选的,所述高分子聚合物溶液包括添加剂,添加添加剂的目的是为了增强离子的电导率,进一步提高制备得到的二次电池的导电性。所述添加剂选自Al 2O 3、SiO 2、如Li 0.5La 0.5TiO 3的钙钛矿构型ABO 3的物质、如Li 14Zn(GeO 4) 4的LISICON结构的物质、如Na 3Zr 2Si 2PO 12的NASICON结构的物质、如Li 7La 3Zr 2O 12的石榴石型氧化物物质的至少一种。 Preferably, the high molecular polymer solution includes additives, and the purpose of adding the additives is to enhance the conductivity of the ions and further improve the conductivity of the prepared secondary battery. The additives are selected from Al 2 O 3 , SiO 2 , materials with perovskite configuration ABO 3 such as Li 0.5 La 0.5 TiO 3 , materials with LISICON structure such as Li 14 Zn(GeO 4 ) 4 , such as Na 3 Zr 2 Si 2 PO 12 NASICON structure material, such as at least one kind of Li 7 La 3 Zr 2 O 12 garnet type oxide material.
优选的,所述高分子聚合物溶液包括溶剂,添加所述溶剂能够较好得溶解上述高分子聚合物进行高分子聚合物溶液的配制。所述溶剂选自四氢呋喃、丙酮、二甲基甲酰胺、二甲基乙酰胺、甲苯、水、二氯甲烷、氯仿的至少一种。Preferably, the high-molecular polymer solution includes a solvent, and the addition of the solvent can better dissolve the high-molecular polymer for preparation of the high-molecular polymer solution. The solvent is selected from at least one of tetrahydrofuran, acetone, dimethylformamide, dimethylacetamide, toluene, water, dichloromethane, and chloroform.
优选的,所述高分子聚合物溶液的体积百分比浓度为1%~30%。若溶液的浓度过低,则高分子聚合物在金属负极表面的附着量较少,附着量过少会影响高分子隔膜层的柔性,同时也会导致制备得到的高分子隔膜层的厚度太薄,影响制备得到的一体化结构的隔膜负极材料。若溶液的浓度过高,则高分子聚合物的溶解性较差,易导致配制得到的高分子聚合物溶液溶解不均匀,进而影响 所述高分子隔膜层的性质,影响制备得到的一体化结构的隔膜负极材料。Preferably, the volume percentage concentration of the high molecular polymer solution is 1%-30%. If the concentration of the solution is too low, the adhesion amount of the polymer on the surface of the metal negative electrode will be less. Too little adhesion will affect the flexibility of the polymer diaphragm layer, and also cause the thickness of the prepared polymer diaphragm layer to be too thin , Affect the prepared integrated structure of the separator anode material. If the concentration of the solution is too high, the solubility of the high molecular polymer will be poor, which will easily lead to uneven dissolution of the prepared high molecular polymer solution, which in turn affects the properties of the polymer membrane layer and the integrated structure obtained The separator anode material.
优选的,配制高分子聚合物溶液包括如下步骤:将选用的高分子聚合物、添加剂与溶剂按照高分子聚合物溶液的体积百分比浓度进行混合,于50~80℃之间进行混合处理,保证各物质溶解。进一步优选的,所述混合处理的时间为12~48小时。在本发明优选实施例中,所述混合处理的方式包括但不限于搅拌等常规方法。Preferably, the preparation of the high molecular polymer solution includes the following steps: mixing the selected high molecular polymer, additives, and solvent according to the volume percentage concentration of the high molecular polymer solution, and performing the mixing treatment at a temperature between 50 and 80°C to ensure that each The substance dissolves. Further preferably, the time of the mixing treatment is 12 to 48 hours. In a preferred embodiment of the present invention, the mixing treatment method includes, but is not limited to, conventional methods such as stirring.
进一步地,待形成澄清的高分子聚合物溶液后,将所述高分子聚合物溶液置于静电纺丝装置的注射器中,备用。Further, after the clear high molecular polymer solution is formed, the high molecular polymer solution is placed in the syringe of the electrostatic spinning device for standby.
具体的,在上述步骤S02中,将所述金属负极放置于静电纺丝装置设备内,设置静电纺丝的电源电压为5~30kV,所述注射器与所述金属负极的距离为5~50cm,控制所述高分子聚合物溶液的流速为300~1000μL/h,在所述金属负极的表面静电纺丝制备高分子隔膜层,得到所述一体化结构的隔膜负极材料。Specifically, in the above step S02, the metal negative electrode is placed in the electrospinning device, the power supply voltage for electrospinning is set to 5-30kV, and the distance between the syringe and the metal negative electrode is 5-50cm, The flow rate of the high molecular polymer solution is controlled to be 300-1000 μL/h, and a high molecular diaphragm layer is prepared by electrostatic spinning on the surface of the metal negative electrode to obtain the diaphragm negative electrode material of the integrated structure.
优选的,所述金属负极的材料选自铝、锡、镁、锌、铜、铁、镍、钛、锰、锑、铋等发生合金化电池反应的的一种或含有至少一种所述金属元素的合金。Preferably, the material of the metal negative electrode is selected from one of aluminum, tin, magnesium, zinc, copper, iron, nickel, titanium, manganese, antimony, bismuth, etc. that undergo alloying battery reactions, or contains at least one of the metals The alloy of the elements.
优选的,所述金属负极选自未经过预处理的金属负极或经过预处理的金属负极。进一步优选的,所述经过预处理的金属负极选自经过抛光的金属负极、经过打磨处理的金属负极、经过喷砂处理的金属负极、进过等离子体处理的金属负极的任意一种。选择经过预处理的金属负极作为负极材料,能够进一步提高金属负极与所述高分子隔膜层的结合能力,提高所述制备得到的一体化结构的隔膜负极材料的整体性能,保证黏附性更强,金属负极与高分子隔膜层之间不易脱落。Preferably, the metal negative electrode is selected from a metal negative electrode that has not undergone pretreatment or a metal negative electrode that has undergone pretreatment. Further preferably, the pretreated metal negative electrode is selected from any one of a polished metal negative electrode, a polished metal negative electrode, a sandblasted metal negative electrode, and a plasma-treated metal negative electrode. Selecting the pretreated metal negative electrode as the negative electrode material can further improve the binding capacity of the metal negative electrode and the polymer separator layer, improve the overall performance of the prepared integrated structure separator negative electrode material, and ensure stronger adhesion. It is not easy to fall off between the metal negative electrode and the polymer separator layer.
优选的,将所述金属负极放置于静电纺丝装置设备内包括如下步骤:将所述金属负极进行裁剪,得到大小适当,并将所述金属负极进行固定至静电纺丝装置设备内的收集屏幕表面。Preferably, placing the metal negative electrode in the electrospinning device includes the following steps: cutting the metal negative electrode to obtain an appropriate size, and fixing the metal negative electrode to the collection screen in the electrospinning device. surface.
在本发明优选实施例中,所述静电纺丝装置如附图2所示,如图2所示,1为高压电源,2为装有高分子溶液的注射器,3为所述高分子隔膜层,4为所述 金属负极,5为接收屏幕。In a preferred embodiment of the present invention, the electrospinning device is shown in FIG. 2. As shown in FIG. 2, 1 is a high-voltage power supply, 2 is a syringe containing a polymer solution, and 3 is the polymer diaphragm layer. , 4 is the metal negative electrode, and 5 is the receiving screen.
具体的,设置静电纺丝的电源电压为5~30kV,所述注射器与所述金属负极的距离为5~50cm,控制所述高分子聚合物溶液的流速为300~1000μL/h,在所述金属负极的表面静电纺丝制备高分子隔膜层,得到所述一体化结构的隔膜负极材料。在静电纺丝工作中,静电纺丝的电源电压、注射器与所述金属负极的距离以及高分子聚合物溶液的流速是共同决定纺丝溶液是否能够顺利喷出并到达收集屏幕的重要因素,因此,对上述条件进行限定有利于试验顺利进行。Specifically, the electrospinning power supply voltage is set to 5-30kV, the distance between the syringe and the metal negative electrode is 5-50cm, and the flow rate of the polymer solution is controlled to be 300-1000μL/h. The surface of the metal negative electrode is electrostatically spun to prepare a polymer diaphragm layer to obtain the diaphragm negative electrode material of the integrated structure. In the electrospinning work, the electrospinning power supply voltage, the distance between the syringe and the metal negative electrode, and the flow rate of the polymer solution are important factors that jointly determine whether the spinning solution can be ejected smoothly and reach the collection screen. Therefore, , Limiting the above conditions is conducive to the smooth progress of the test.
进一步地,设置静电纺丝的电源电压为5~30kV,电压5~30KV是为了在工作中纺丝溶液可以顺利喷出,若电源电压过低,则无法形成有效电场,导致溶液不会喷出,无法制备得到产品;若电源电压过高,会影响纺丝正常那进行,且有一定的危险性。进一步地,所述注射器与所述金属负极的距离为5~50cm,若注射器与所述金属负极的距离太远,则会影响隔膜层结构的制备,导致隔膜层结构的厚度过薄,进而影响一体化结构的隔膜负极材料;在本发明优选实施例中,所述注射器与所述金属负极的距离为10~20cm。进一步地,所述高分子聚合物溶液的流速为300~1000μL/h,若所述高分子聚合物溶液的流速过快,会影响纺丝纤维在金属负极表面的均匀性,影响所述一体化结构的隔膜负极材料的性能,影响高分子隔膜层与所述金属负极的接触,无法较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题,进而影响二次电池的安全性能;若所述高分子聚合物溶液的流速过慢,则会影响纺丝纤维的连续性,导致所述高分子隔膜层易发生断裂,进而无法保证金属负极不会形成毛刺而刺穿隔膜,影响所述一体化结构的隔膜负极材料的性能,导致二次电池的安全性能较差。Furthermore, the power supply voltage for electrospinning is set to 5-30kV, and the voltage is 5-30kV for the spinning solution to be sprayed smoothly during work. If the power supply voltage is too low, an effective electric field cannot be formed, resulting in the solution not being sprayed. , The product cannot be prepared; if the power supply voltage is too high, it will affect the normal spinning process, and there is a certain degree of danger. Further, the distance between the syringe and the metal negative electrode is 5-50 cm. If the distance between the syringe and the metal negative electrode is too far, it will affect the preparation of the diaphragm layer structure, resulting in the thickness of the diaphragm layer structure being too thin, and thus affecting A membrane negative electrode material with an integrated structure; in a preferred embodiment of the present invention, the distance between the syringe and the metal negative electrode is 10-20 cm. Further, the flow rate of the high-molecular polymer solution is 300-1000 μL/h. If the flow rate of the high-molecular polymer solution is too fast, the uniformity of the spun fiber on the surface of the metal negative electrode will be affected, and the integration will be affected. The performance of the structured diaphragm negative electrode material affects the contact between the polymer diaphragm layer and the metal negative electrode, and cannot well suppress the problem of volume expansion and pulverization of the negative metal negative electrode during use, thereby affecting the safety performance of the secondary battery; If the flow rate of the high molecular polymer solution is too slow, it will affect the continuity of the spinning fiber and cause the high molecular diaphragm layer to be easily broken, and thus it cannot be guaranteed that the metal negative electrode will not form burrs and pierce the diaphragm, affecting the The performance of the separator anode material of the integrated structure leads to the poor safety performance of the secondary battery.
优选的,所述高分子隔膜层为一层高分子纺丝结构层或多层高分子纺丝结构层。进一步优选的,所述多层高分子纺丝结构层为多层相同高分子材料的纺丝结构层或多层不同高分子材料的纺丝结构层。在本发明一些实施例中,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层,其中,所述高分子隔膜层为一层高分子纺丝结构层。在所述金 属负极表面结合一层高分子纺丝结构层作为高分子隔膜层,可较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题。在本发明一些实施例中,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层,其中,所述高分子隔膜层为多层相同高分子材料的纺丝结构层。设置所述高分子隔膜层为多层相同高分子材料的纺丝结构层,以形成柔韧性更高的隔膜材料,进一步抑制金属负极的体积膨胀粉化的问题。在本发明一些实施例中,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层,其中,所述高分子隔膜层为多层不同高分子材料的纺丝结构层。设置所述高分子隔膜层为多层不同高分子材料的纺丝结构层,根据不同的需求,进而选择不同的高分子材料制备得到不同的纺丝结构层,形成的高分子隔膜层能够将不同聚合物纺丝的优势结合起来,有效地对一体化结构的隔膜负极材料的性能,比如调节结合力、浸润性、孔隙率、柔性等性能进行优化,更有利于广泛应用。Preferably, the polymer membrane layer is a polymer spinning structure layer or a multi-layer polymer spinning structure layer. Further preferably, the multi-layer polymer spinning structure layer is a multi-layer spinning structure layer of the same polymer material or a multi-layer spinning structure layer of different polymer materials. In some embodiments of the present invention, the integrated structure of the separator negative electrode material includes a metal negative electrode, and a polymer separator layer bonded to any side of the metal negative electrode, wherein the polymer separator layer is a layer of polymer spun Silk structure layer. Combining a polymer spinning structure layer on the surface of the metal negative electrode as a polymer separator layer can better suppress the problem of volume expansion and pulverization of the negative metal negative electrode during use. In some embodiments of the present invention, the membrane negative electrode material of the integrated structure includes a metal negative electrode, and a polymer membrane layer bonded to any side of the metal negative electrode, wherein the polymer membrane layer is a multilayer of the same polymer. Material spinning structure layer. The polymer separator layer is set as a multi-layer spinning structure layer of the same polymer material to form a separator material with higher flexibility, and further suppress the problem of volume expansion and powdering of the metal negative electrode. In some embodiments of the present invention, the integrated structure of the separator negative electrode material includes a metal negative electrode, and a polymer separator layer bonded to any side of the metal negative electrode, wherein the polymer separator layer is a multilayer of different polymers. Material spinning structure layer. The polymer membrane layer is set as a multi-layer spinning structure layer of different polymer materials. According to different needs, different polymer materials are selected to prepare different spinning structure layers, and the formed polymer membrane layer can be different The advantages of polymer spinning are combined to effectively optimize the performance of the integrated structure of the separator anode material, such as adjusting the binding force, wettability, porosity, flexibility and other properties, which is more conducive to a wide range of applications.
优选的,还包括将得到所述一体化结构的隔膜负极材料于30~100℃下的条件下进行烘干处理。进一步优选的,将烘干后的材料裁成一定的大小,制备成一体化结构的隔膜负极材料。Preferably, the method further includes drying the negative electrode material of the separator with the integrated structure under the condition of 30-100°C. More preferably, the dried material is cut into a certain size to prepare an integrated structure of the separator negative electrode material.
相应的,本发明还提供了一种二次电池,所述二次电池包括正极,一体化结构的隔膜负极材料以及电解液;其中,所述一体化结构的隔膜负极材料由所述的一体化结构的隔膜负极材料的制备方法制备获得的或为所述的一体化结构的隔膜负极材料。Correspondingly, the present invention also provides a secondary battery. The secondary battery includes a positive electrode, an integrated structured separator negative electrode material and an electrolyte; wherein the integrated structured separator negative electrode material is composed of the integrated structure The structured separator negative electrode material is prepared by the preparation method or is the integrated structure separator negative electrode material.
本发明所述的二次电池,所述二次电池包括正极,一体化结构的隔膜负极材料以及电解液;其中,所述一体化结构的隔膜负极材料由所述的一体化结构的隔膜负极材料的制备方法制备获得的或为所述的一体化结构的隔膜负极材料。采用上述一体化结构的隔膜负极材料或由上述一体化结构的隔膜负极材料的制备方法制备得到的电池负极作为所述二次电池的负极材料,简化电池内部结构和装配工艺,极大改善了金属负极与隔膜的界面接触特性,制备得到的二 次电池,保证金属负极材料不易粉化,能够保持完整性;同时提高金属负极与隔膜之间有效地接触距离,增强二次电池的循环稳定性和库伦效率。In the secondary battery of the present invention, the secondary battery includes a positive electrode, an integrated structured separator negative electrode material and an electrolyte; wherein the integrated structured separator negative electrode material is composed of the integrated structured separator negative electrode material The preparation method is obtained by the preparation method or is the separator negative electrode material with the integrated structure. The use of the above-mentioned integrated structure of the diaphragm negative electrode material or the battery negative electrode prepared by the preparation method of the above-mentioned integrated structure of the diaphragm negative electrode material is used as the negative electrode material of the secondary battery, which simplifies the internal structure and assembly process of the battery, and greatly improves the metal The interface contact characteristics of the negative electrode and the separator, the prepared secondary battery ensures that the metal negative electrode material is not easy to pulverize and can maintain integrity; at the same time, the effective contact distance between the metal negative electrode and the separator is increased, and the cycle stability of the secondary battery is enhanced. Coulomb efficiency.
具体的,如图5所示,所述二次电池包括正极,一体化结构的隔膜负极材料以及电解液。Specifically, as shown in FIG. 5, the secondary battery includes a positive electrode, a separator negative electrode material with an integrated structure, and an electrolyte.
具体的,所述一体化结构的隔膜负极材料为所述的一体化结构的隔膜负极材料或由所述的一体化结构的隔膜负极材料的制备方法制备获得的。Specifically, the integrated structured separator negative electrode material is the integrated structured separator negative electrode material or is prepared by the integrated structured separator negative electrode material preparation method.
本发明所述一体化结构的隔膜负极材料,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层,一方面,所述隔膜层为高分子隔膜层,高分子隔膜层具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题,保证金属负极不会形成毛刺而刺穿隔膜,保证二次电池的安全性能;另一方面,所述高分子隔膜层通过纺丝工艺与所述金属负极结合形成一体化结构,使隔膜与金属负极负极二者进行结合,进一步增加了隔膜与金属负极负极之间的有效接触,并且使制备得到的一体化结构的隔膜负极材料的厚度和形状可随意设计,柔韧性良好,一定程度上抑制了二次电池循环中,金属箔材负极易造成膨胀粉化的问题,提高二次电池安全性能和库伦效率。In the integrated structure of the negative electrode material of the separator of the present invention, the negative electrode material of the integrated structure includes a metal negative electrode, and a polymer separator layer bonded to any side of the metal negative electrode. On the one hand, the separator layer is a polymer The diaphragm layer and the polymer diaphragm layer have good flexibility, certain toughness and controllable porosity, which can better suppress the volume expansion and powdering of the negative metal negative electrode during use, and ensure that the metal negative electrode will not form The burr pierces the diaphragm to ensure the safety performance of the secondary battery; on the other hand, the polymer diaphragm layer is combined with the metal negative electrode through a spinning process to form an integrated structure, so that the diaphragm and the metal negative electrode are combined, It further increases the effective contact between the separator and the metal negative electrode, and makes the thickness and shape of the prepared integrated structure of the separator negative electrode material can be designed at will, with good flexibility, and to a certain extent inhibit the metal The foil negative electrode is easy to cause the problem of swelling and pulverization, which improves the safety performance and coulomb efficiency of the secondary battery.
优选的,所述的正极为将正极材料涂覆在金属箔材集流体上。优选的,所述正极材料选自含锂金属氧化物锰酸锂、钴酸锂、磷酸铁锂、三元材料、天然石墨,活性炭、碳纳米管、石墨烯、活性碳纤维、碳分子筛、介孔碳、炭泡沫、膨胀石墨的至少一种。优选的,所述金属箔材集流体选自铝、锡、镁、锌、铜、铁、镍、钛、锰、锑、铋中的任意一种或含有至少一种上述金属元素的合金。进一步优选的,所述金属箔材集流体的厚度为10~1000μm。Preferably, the positive electrode is made by coating a positive electrode material on a metal foil current collector. Preferably, the positive electrode material is selected from lithium-containing metal oxides, lithium manganese oxide, lithium cobalt oxide, lithium iron phosphate, ternary materials, natural graphite, activated carbon, carbon nanotubes, graphene, activated carbon fibers, carbon molecular sieves, mesoporous At least one of carbon, carbon foam, and expanded graphite. Preferably, the metal foil current collector is selected from any one of aluminum, tin, magnesium, zinc, copper, iron, nickel, titanium, manganese, antimony, and bismuth, or an alloy containing at least one of the foregoing metal elements. Further preferably, the thickness of the metal foil current collector is 10-1000 μm.
优选的,所述电解液位含有一定浓度电解质盐的溶液。优选的,所述电解液中,电解质盐的浓度为0.1-10mol/L。Preferably, the electrolyte level contains a solution of a certain concentration of electrolyte salt. Preferably, the concentration of the electrolyte salt in the electrolyte is 0.1-10 mol/L.
进一步优选的,所述电解质盐选自锂盐、钠盐、钾盐、钙盐的一种或几种。在本发明优选实施例中,所述解质盐选自六氟磷酸锂、六氟磷酸钾、六氟磷酸 钠、六氟磷酸钙、四氟硼酸锂、四氟硼酸钾、四氟硼酸钠、氟化锂、高氯酸锂,草酸硼酸锂、二氟草酸硼酸锂等中的一种或多种。Further preferably, the electrolyte salt is selected from one or more of lithium salt, sodium salt, potassium salt, and calcium salt. In a preferred embodiment of the present invention, the decomposing salt is selected from lithium hexafluorophosphate, potassium hexafluorophosphate, sodium hexafluorophosphate, calcium hexafluorophosphate, lithium tetrafluoroborate, potassium tetrafluoroborate, sodium tetrafluoroborate, lithium fluoride , One or more of lithium perchlorate, lithium oxalate borate, lithium difluorooxalate borate, etc.
优选的,所述电解液的溶剂选自有机溶剂或离子液体。进一步优选的,所述有机溶剂选自酯类、醚类、砜类、腈类的一种或多种。在本发明一些实施例中,所述有机溶剂选自碳酸丙烯酯(PC)、碳酸乙烯酯(EC)、氟代碳酸乙烯酯(FEC)、碳酸二甲酯(DMC)、碳酸二乙酯(DEC)、碳酸甲乙酯(EMC)、乙酸乙酯(EA)、乙酸甲酯(MA)、甲酸甲酯(MF)、丙酸甲酯(MP)、丙酸乙酯(EP)、四氢呋喃(THF)、二甲氧甲烷(DMM)、1,3-二氧环戊烷(DOL)、4-甲基-1,3-二氧环戊烷(4MeDOL)、1,2-二甲氧丙烷(DMP)、二甲醚(DME)、三乙二醇二甲醚(DG)、亚硫酸二甲脂(DMS)、亚硫酸乙烯酯(ES)、亚硫酸丙烯脂(PS)、亚硫酸二乙脂(DES)等中的一种或多种。在本发明一些实施例中,所述离子液体包括1-乙基-3-甲基咪唑-六氟磷酸盐、1-丁基-1-甲基吡咯烷-双三氟甲基磺酰亚胺盐、1-乙基-3-甲基咪唑-四氟硼酸盐、1-丁基-1-甲基咪唑-六氟磷酸盐、1-丙基-3-甲基咪唑-六氟磷酸盐、N-甲,丁基哌啶-双三氟甲基磺酰亚胺盐、N-甲基-N-丙基吡咯烷-双三氟甲基磺酰亚胺盐、1-丙基-3-甲基咪唑-双三氟甲基磺酰亚胺盐、1-丙基-3-甲基咪唑-四氟硼酸盐、1-乙基-3-甲基咪唑-双三氟甲基磺酰亚胺盐、1-丁基-1-甲基咪唑-四氟硼酸盐、N-丁基-N-甲基吡咯烷-双三氟甲基磺酰亚胺盐、N-甲,丙基哌啶-双三氟甲基磺酰亚胺盐等中的一种或多种。Preferably, the solvent of the electrolyte is selected from organic solvents or ionic liquids. Further preferably, the organic solvent is selected from one or more of esters, ethers, sulfones, and nitriles. In some embodiments of the present invention, the organic solvent is selected from propylene carbonate (PC), ethylene carbonate (EC), fluoroethylene carbonate (FEC), dimethyl carbonate (DMC), diethyl carbonate ( DEC), ethyl methyl carbonate (EMC), ethyl acetate (EA), methyl acetate (MA), methyl formate (MF), methyl propionate (MP), ethyl propionate (EP), tetrahydrofuran ( THF), Dimethoxymethane (DMM), 1,3-Dioxolane (DOL), 4-Methyl-1,3-dioxolane (4MeDOL), 1,2-Dimethoxypropane (DMP), dimethyl ether (DME), triethylene glycol dimethyl ether (DG), dimethyl sulfite (DMS), vinyl sulfite (ES), propylene sulfite (PS), two sulfite One or more of ethyl ester (DES), etc. In some embodiments of the present invention, the ionic liquid includes 1-ethyl-3-methylimidazole-hexafluorophosphate, 1-butyl-1-methylpyrrolidine-bistrifluoromethylsulfonimide Salt, 1-ethyl-3-methylimidazole-tetrafluoroborate, 1-butyl-1-methylimidazole-hexafluorophosphate, 1-propyl-3-methylimidazole-hexafluorophosphate , N-methyl, butyl piperidine-bistrifluoromethanesulfonimide salt, N-methyl-N-propylpyrrolidine-bistrifluoromethanesulfonimide salt, 1-propyl-3 -Methylimidazole-bistrifluoromethanesulfonimide salt, 1-propyl-3-methylimidazole-tetrafluoroborate, 1-ethyl-3-methylimidazole-bistrifluoromethanesulfonate Imide salt, 1-butyl-1-methylimidazole-tetrafluoroborate, N-butyl-N-methylpyrrolidine-bistrifluoromethanesulfonimide salt, N-methyl, propyl One or more of piperidine-bistrifluoromethanesulfonimide salt and the like.
相应的,本发明还提供了一种二次电池的制备方法,所述制备方法包括如下步骤:Correspondingly, the present invention also provides a method for preparing a secondary battery, which includes the following steps:
G01.将正极活性物质与粘合剂以及导电炭黑按一定的比例研磨成浆料,涂覆在金属箔材集流体上后,进行烘干、裁剪得到所需尺寸的正极;G01. Grind the positive electrode active material, binder and conductive carbon black into a slurry according to a certain ratio, and coat it on the metal foil current collector, then dry and cut to obtain the desired size of the positive electrode;
G02.将一定的电解质盐加入到相应的溶剂中,配制得到电解液;G02. Add a certain electrolyte salt to the corresponding solvent to prepare the electrolyte;
G03.提供本发明所述的一体化结构的隔膜负极材料,将所述一体化结构的隔膜负极材料进行裁剪,得到大小合适的一体化结构的隔膜负极材料;G03. Provide the diaphragm negative electrode material of the integrated structure of the present invention, and cut the diaphragm negative electrode material of the integrated structure to obtain the diaphragm negative electrode material of the integrated structure of a suitable size;
G04.将所述正极、所述电解液、所述大小合适的一体化结构的隔膜负极材料以及其他封装部件组分进行装配得到所述二次电池。G04. Assemble the positive electrode, the electrolyte, the diaphragm negative electrode material of an integrated structure of suitable size, and other packaging components to obtain the secondary battery.
对采用所述二次电池的制备方法制备得到的二次电池进行充放电,并设置不同充放电的循环次数,可进一步测试分析所述二次电池的性能。Charge and discharge the secondary battery prepared by the preparation method of the secondary battery, and set different cycle times of charge and discharge, and further test and analyze the performance of the secondary battery.
下边以具体实施例进一步进行说明。Specific examples are further described below.
实施例1Example 1
制备一体化结构的隔膜负极材料Preparation of diaphragm anode material with integrated structure
按照体积质量浓度为10%,将聚丙烯腈(PAN)溶于二甲基甲酰胺(DMF)中,搅拌均匀后作为高分子聚合物溶液并取3毫升溶液置于静电纺丝装置的注射器中;According to the volume mass concentration of 10%, dissolve polyacrylonitrile (PAN) in dimethylformamide (DMF), stir it evenly and use it as a high molecular polymer solution. Take 3 ml of the solution and place it in the syringe of the electrospinning device. ;
提供金属铝箔作为金属负极,将所述金属负极进行裁剪得到大小适合的材料,并用酒精将表面擦拭干净,固定于静电纺丝装置的基板上;Provide a metal aluminum foil as a metal negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
设置静电纺丝的电源电压为15kV,所述注射器与所述金属负极的距离为15cm,控制所述高分子聚合物溶液的流速为600μL/h的条件下进行制备,再进行干燥处理,裁剪得到所述一体化结构的隔膜负极材料,其中,所述一体化结构的隔膜负极材料为单层高分子材料的纺丝结构层。The electrospinning power supply voltage is set to 15kV, the distance between the syringe and the metal negative electrode is 15cm, and the flow rate of the polymer solution is controlled to 600μL/h. In the integrated structure of the separator negative electrode material, the integrated structure of the separator negative electrode material is a single-layered polymer material with a spinning structure layer.
制备锂的双离子电池Dual-ion battery for preparing lithium
利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池。A new battery is assembled by using the separator negative electrode material of the integrated structure prepared in the above-mentioned Example 1 through matching with the positive electrode.
将0.8g天然石墨、0.1g聚偏氟乙烯、0.1g导电碳黑加入到2mL氮-甲基吡咯烷酮中,将研磨得到均匀浆料涂覆于涂炭铝箔表面,80℃真空干燥12小时,并裁切成电极片。Add 0.8g of natural graphite, 0.1g of polyvinylidene fluoride, and 0.1g of conductive carbon black to 2mL of nitrogen-methylpyrrolidone, coat the uniform slurry obtained by grinding on the surface of the carbon-coated aluminum foil, vacuum dry at 80°C for 12 hours, and cut Cut into electrode pieces.
在手套箱中称取一定量的六氟磷酸锂,加入到碳酸甲乙酯中,配置成4M的六氟磷酸锂电解液。Weigh a certain amount of lithium hexafluorophosphate in the glove box and add it to ethyl methyl carbonate to prepare a 4M lithium hexafluorophosphate electrolyte.
将制备好的正极以及正极电池壳、一体化结构的隔膜负极材料等按一定的顺序依次紧密堆叠,滴加电解液使隔膜完全浸润,最后通过封装完成锂离子电 池的组装。The prepared positive electrode, positive electrode battery case, integrated structure of the separator and negative electrode materials are closely stacked in a certain order, the electrolyte is dripped to completely infiltrate the separator, and finally the assembly of the lithium ion battery is completed by packaging.
实施例2Example 2
制备一体化结构的隔膜负极材料Preparation of diaphragm anode material with integrated structure
按照体积质量浓度为10%,将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中,搅拌均匀后作为高分子聚合物溶液并取3毫升溶液置于静电纺丝装置的注射器中;According to the volume mass concentration of 10%, dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) with a volume mass concentration of 7%: 3% in dimethylformamide (DMF), and stir evenly As a high-molecular polymer solution, take 3 ml of the solution and place it in the syringe of the electrospinning device;
将0.8g天然石墨、0.1g聚偏氟乙烯、0.1g导电碳黑加入到2mL氮-甲基吡咯烷酮中;将研磨得到均匀浆料涂覆于涂炭铜箔表面,80℃真空干燥12小时得到金属负极,将所述金属负极进行裁剪得到大小适合的材料,并用酒精将表面擦拭干净,固定于静电纺丝装置的基板上;Add 0.8g of natural graphite, 0.1g of polyvinylidene fluoride, and 0.1g of conductive carbon black to 2mL of nitrogen-methylpyrrolidone; coat the uniform slurry obtained by grinding on the surface of the carbon-coated copper foil, and vacuum dry at 80°C for 12 hours to obtain the metal For the negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
设置静电纺丝的电源电压为15kV,所述注射器与所述金属负极的距离为15cm,控制所述高分子聚合物溶液的流速为600μL/h的条件下进行制备,再进行干燥处理,裁剪得到所述一体化结构的隔膜负极材料,其中,所述一体化结构的隔膜负极材料为单层高分子材料的纺丝结构层。The electrospinning power supply voltage is set to 15kV, the distance between the syringe and the metal negative electrode is 15cm, and the flow rate of the polymer solution is controlled to 600μL/h. In the integrated structure of the separator negative electrode material, the integrated structure of the separator negative electrode material is a single-layered polymer material with a spinning structure layer.
制备锂离子电池Preparation of lithium-ion batteries
利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池。A new battery is assembled by using the integrated structure separator negative electrode material prepared in the above-mentioned Example 2 through matching with the positive electrode.
将0.8g磷酸铁锂、0.1g聚偏氟乙烯、0.1g导电碳黑加入到2mL氮-甲基吡咯烷酮中。将研磨得到均匀浆料涂覆于铝箔表面,80℃真空干燥12小时,并裁切成电极片作正极。0.8 g of lithium iron phosphate, 0.1 g of polyvinylidene fluoride, and 0.1 g of conductive carbon black were added to 2 mL of nitrogen-methylpyrrolidone. The uniform slurry obtained by grinding was coated on the surface of the aluminum foil, dried in a vacuum at 80° C. for 12 hours, and cut into electrode sheets as positive electrodes.
在手套箱中称取一定量的六氟磷酸锂,加入到碳酸乙烯酯(EC),碳酸甲乙酯(EMC),碳酸二甲酯(DMC)体积比为1:1:1中,配置成1M的六氟磷酸锂电解液。Weigh a certain amount of lithium hexafluorophosphate in the glove box, add it to ethylene carbonate (EC), ethyl methyl carbonate (EMC), and dimethyl carbonate (DMC) in a volume ratio of 1:1:1 to form 1M lithium hexafluorophosphate Electrolyte.
将制备好的正极以及正极电池壳、一体化结构的隔膜负极材料等按一定的顺序依次紧密堆叠,滴加电解液使隔膜完全浸润,最后通过封装完成锂离子电池的组装。The prepared positive electrode and the positive electrode battery case, the integrated structure of the separator and negative electrode materials are closely stacked in a certain order, the electrolyte is dripped to make the separator completely infiltrated, and finally the assembly of the lithium ion battery is completed by packaging.
实施例3Example 3
制备一体化结构的隔膜负极材料Preparation of diaphragm anode material with integrated structure
按照体积质量浓度为10%,将聚丙烯腈(PAN)溶于二甲基甲酰胺(DMF)中,搅拌均匀后作为高分子聚合物溶液并取3毫升溶液置于静电纺丝装置的注射器中;According to the volume mass concentration of 10%, dissolve polyacrylonitrile (PAN) in dimethylformamide (DMF), stir it evenly and use it as a high molecular polymer solution. Take 3 ml of the solution and place it in the syringe of the electrospinning device. ;
提供金属锡箔作为金属负极,将所述金属负极进行裁剪得到大小适合的材料,并用酒精将表面擦拭干净,固定于静电纺丝装置的基板上;Provide a metal tin foil as a metal negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
设置静电纺丝的电源电压为15kV,所述注射器与所述金属负极的距离为15cm,控制所述高分子聚合物溶液的流速为600μL/h的条件下进行制备,再进行干燥处理,裁剪得到所述一体化结构的隔膜负极材料,其中,所述一体化结构的隔膜负极材料为单层高分子材料的纺丝结构层。The electrospinning power supply voltage is set to 15kV, the distance between the syringe and the metal negative electrode is 15cm, and the flow rate of the polymer solution is controlled to 600μL/h. In the integrated structure of the separator negative electrode material, the integrated structure of the separator negative electrode material is a single-layered polymer material with a spinning structure layer.
制备钾的双离子电池Double ion battery for preparing potassium
利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池。Using the integrated structure of the separator negative electrode material prepared in the foregoing Example 3, a new battery can be assembled by matching with the positive electrode.
将0.8g天然石墨、0.1g聚偏氟乙烯、0.1g导电碳黑加入到2mL氮-甲基吡咯烷酮中。将研磨得到均匀浆料涂覆于涂炭铝箔表面,80℃真空干燥12小时,并裁切成电极片作为正极。0.8 g of natural graphite, 0.1 g of polyvinylidene fluoride, and 0.1 g of conductive carbon black were added to 2 mL of nitrogen-methylpyrrolidone. The uniform slurry obtained by grinding was coated on the surface of the carbon-coated aluminum foil, dried in a vacuum at 80° C. for 12 hours, and cut into electrode sheets as the positive electrode.
在手套箱中称取一定量的六氟磷酸钾,加入到碳酸乙烯酯:碳酸二甲酯(v/v=1:1)中,配置成0.8M的六氟磷酸钾电解液。Weigh a certain amount of potassium hexafluorophosphate in the glove box, add it to ethylene carbonate: dimethyl carbonate (v/v=1:1), and configure it into 0.8M potassium hexafluorophosphate electrolyte.
将制备好的正极以及正极电池壳、一体化结构的隔膜负极材料等按一定的顺序依次紧密堆叠,滴加电解液使隔膜完全浸润,最后通过封装完成钾的双离子电池的组装。The prepared positive electrode, the positive electrode battery case, the integrated structure of the separator and the negative electrode material are closely stacked in a certain order, the electrolyte is dripped to make the separator completely infiltrated, and finally the potassium dual-ion battery is assembled by packaging.
实施例4Example 4
制备一体化结构的隔膜负极材料Preparation of diaphragm anode material with integrated structure
按照体积质量浓度为10%,分别将聚乙烯醇(PVA),聚丙烯腈(PAN)溶于二甲基甲酰胺(DMF)中,各自搅拌均匀后,依次制成高分子聚合物溶液 一号和高分子聚合物溶液二号,并取3毫升溶液置于静电纺丝装置的注射器中;According to the volume mass concentration of 10%, respectively dissolve polyvinyl alcohol (PVA) and polyacrylonitrile (PAN) in dimethylformamide (DMF), stir them evenly, and make polymer solution No. 1 in sequence And high molecular polymer solution No. 2, and take 3 ml of the solution and place it in the syringe of the electrospinning device;
提供金属铝箔作为金属负极,将所述金属负极进行裁剪得到大小适合的材料,并用酒精将表面擦拭干净,固定于静电纺丝装置的基板上;Provide a metal aluminum foil as a metal negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
设置静电纺丝的电源电压为15kV,所述注射器与所述金属负极的距离为15cm,控制所述高分子聚合物溶液的流速为600μL/h的条件下,先取3毫升高分子聚合物溶液一号进行制备,制备完毕后,再取3毫升高分子聚合物溶液二号进行制备,再进行干燥处理,裁剪得到所述一体化结构的隔膜负极材料,如图3所示,其中,所述一体化结构的隔膜负极材料3为两层不同高分子材料的纺丝结构层,分别为聚乙烯醇材料的纺丝结构层3-1和聚丙烯腈材料的纺丝结构层3-2。Set the power supply voltage of electrospinning to 15kV, the distance between the syringe and the metal negative electrode is 15cm, and the flow rate of the high molecular polymer solution is controlled to 600 μL/h, first take 3 ml of high molecular polymer solution one No. 2 is prepared. After the preparation is complete, take 3 ml of high molecular polymer solution No. 2 for preparation, and then perform drying treatment, and cut to obtain the diaphragm negative electrode material of the integrated structure, as shown in FIG. 3, wherein the integrated structure The structured separator negative electrode material 3 is composed of two spinning structure layers of different polymer materials, namely a spinning structure layer 3-1 of polyvinyl alcohol material and a spinning structure layer 3-2 of polyacrylonitrile material.
制备锂的双离子电池Dual-ion battery for preparing lithium
利用上述实施例4制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池。Using the integrated structure of the separator negative electrode material prepared in the foregoing Example 4, a new battery can be assembled by matching with the positive electrode.
将0.8g天然石墨、0.1g聚偏氟乙烯、0.1g导电碳黑加入到2mL氮-甲基吡咯烷酮中。将研磨得到均匀浆料涂覆于涂炭铝箔表面,80℃真空干燥12小时,并裁切成电极片。0.8 g of natural graphite, 0.1 g of polyvinylidene fluoride, and 0.1 g of conductive carbon black were added to 2 mL of nitrogen-methylpyrrolidone. The uniform slurry obtained by grinding is coated on the surface of the carbon-coated aluminum foil, dried in a vacuum at 80° C. for 12 hours, and cut into electrode sheets.
在手套箱中称取一定量的六氟磷酸锂,加入到碳酸甲乙酯中,配置成4M的六氟磷酸锂电解液。Weigh a certain amount of lithium hexafluorophosphate in the glove box and add it to ethyl methyl carbonate to prepare a 4M lithium hexafluorophosphate electrolyte.
将制备好的正极以及正极电池壳、一体化结构的隔膜负极材料等按一定的顺序依次紧密堆叠,滴加电解液使隔膜完全浸润,最后通过封装完成锂离子电池的组装。The prepared positive electrode and the positive electrode battery case, the integrated structure of the separator and negative electrode materials are closely stacked in a certain order, the electrolyte is dripped to make the separator completely infiltrated, and finally the assembly of the lithium ion battery is completed by packaging.
实施例5Example 5
制备一体化结构的隔膜负极材料Preparation of diaphragm anode material with integrated structure
按照体积质量浓度为10%,分别将聚乙烯基苯酚(PVP),聚乙烯醇(PVA),聚丙烯腈(PAN)溶于二甲基甲酰胺(DMF)中,各自搅拌均匀后,依次制成高分子聚合物溶液一号、高分子聚合物溶液二号和高分子聚合物溶液三号,并 取3毫升溶液置于静电纺丝装置的注射器中;According to the volume mass concentration of 10%, respectively dissolve polyvinyl phenol (PVP), polyvinyl alcohol (PVA), and polyacrylonitrile (PAN) in dimethylformamide (DMF), stir them evenly, and prepare them in sequence. Make high-molecular polymer solution No. 1, high-molecular polymer solution No. 2 and high-molecular polymer solution No. 3. Take 3 ml of the solution and place it in the syringe of the electrostatic spinning device;
提供金属铝箔作为金属负极,将所述金属负极进行裁剪得到大小适合的材料,并用酒精将表面擦拭干净,固定于静电纺丝装置的基板上;Provide a metal aluminum foil as a metal negative electrode, cut the metal negative electrode to obtain a material of a suitable size, wipe the surface clean with alcohol, and fix it on the substrate of the electrostatic spinning device;
设置静电纺丝的电源电压为15kV,所述注射器与所述金属负极的距离为15cm,控制所述高分子聚合物溶液的流速为600μL/h的条件下,先取3毫升高分子聚合物溶液一号进行制备,制备完毕后,再取3毫升高分子聚合物溶液二号进行制备,再取3毫升高分子聚合物溶液三号进行制备,再进行干燥处理,裁剪得到所述一体化结构的隔膜负极材料,如图4所示,其中,所述一体化结构的隔膜负极材料3为三层不同高分子材料的纺丝结构层,分别为聚乙烯基苯酚材料结构层3-3,聚乙烯醇材料的纺丝结构层3-1和聚丙烯腈材料的纺丝结构层3-2。Set the power supply voltage of electrospinning to 15kV, the distance between the syringe and the metal negative electrode is 15cm, and the flow rate of the high molecular polymer solution is controlled to 600 μL/h, first take 3 ml of high molecular polymer solution one After the preparation is completed, take 3 ml of high molecular polymer solution No. 2 for preparation, and then take 3 ml of high molecular polymer solution No. 3 for preparation, and then perform drying treatment, and cut to obtain the integrated structure diaphragm The negative electrode material, as shown in Figure 4, wherein the integrated structure of the separator negative electrode material 3 is three layers of spinning structure layers of different polymer materials, namely the polyvinyl phenol material structure layer 3-3, polyvinyl alcohol The spinning structure layer 3-1 of the material and the spinning structure layer 3-2 of the polyacrylonitrile material.
制备锂的双离子电池Dual-ion battery for preparing lithium
利用上述实施例5制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池。Using the integrated structure of the separator negative electrode material prepared in the above embodiment 5, a new battery can be assembled by matching with the positive electrode.
将0.8g天然石墨、0.1g聚偏氟乙烯、0.1g导电碳黑加入到2mL氮-甲基吡咯烷酮中。将研磨得到均匀浆料涂覆于涂炭铝箔表面,80℃真空干燥12小时,并裁切成电极片。0.8 g of natural graphite, 0.1 g of polyvinylidene fluoride, and 0.1 g of conductive carbon black were added to 2 mL of nitrogen-methylpyrrolidone. The uniform slurry obtained by grinding is coated on the surface of the carbon-coated aluminum foil, dried in a vacuum at 80° C. for 12 hours, and cut into electrode sheets.
在手套箱中称取一定量的六氟磷酸锂,加入到碳酸甲乙酯中,配置成4M的六氟磷酸锂电解液。Weigh a certain amount of lithium hexafluorophosphate in the glove box and add it to ethyl methyl carbonate to prepare a 4M lithium hexafluorophosphate electrolyte.
将制备好的正极以及正极电池壳、一体化结构的隔膜负极材料等按一定的顺序依次紧密堆叠,滴加电解液使隔膜完全浸润,最后通过封装完成锂离子电池的组装。The prepared positive electrode and the positive electrode battery case, the integrated structure of the separator and negative electrode materials are closely stacked in a certain order, the electrolyte is dripped to make the separator completely infiltrated, and finally the assembly of the lithium ion battery is completed by packaging.
实施例6Example 6
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“5%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing an integrated structure of the separator negative electrode material, the volume mass concentration of the polymer solution was changed from "10%" to "5%". All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例6制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 6 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例7Example 7
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“6%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "6%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例7制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 7 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例8Example 8
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“7%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "7%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例8制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 8 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例9Example 9
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“8%”,其他所有步骤、使用的材料 和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "8%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例9制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 9 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例10Example 10
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“9%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "9%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例10制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 10 is matched with the positive electrode to assemble a new battery". All other steps, materials used, and process parameters are the same to prepare a lithium dual-ion battery.
实施例11Example 11
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“11%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "11%". All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例11制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 11 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例12Example 12
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子 聚合物溶液的体积质量浓度由“10%”修改为“12%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing an integrated structure of the negative electrode material for the separator, the volume mass concentration of the polymer solution was changed from "10%" to "12%". All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例12制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 12 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例13Example 13
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“13%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "13%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例13制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 13 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例14Example 14
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“14%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "14%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例14制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 14 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例15Example 15
与实施例1相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“15%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 1, in the process of preparing an integrated structure of the separator negative electrode material, the volume mass concentration of the polymer solution was changed from "10%" to "15%", and all other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例1相比,制备锂的双离子电池的过程中,“利用上述实施例1制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例15制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, "Using the integrated structure of the separator anode material prepared in Example 1 above, through matching with the positive electrode, assemble a new battery" is modified to "Using the above The membrane negative electrode material of the integrated structure prepared in Example 15 is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium dual-ion battery.
实施例16Example 16
与实施例1相比,所述高分子聚合物溶液的体积质量浓度为10%相同,制备单独的隔膜材料,隔膜与负极不是一体化材料。Compared with Example 1, the volume mass concentration of the high molecular polymer solution is the same as 10%, and a separate separator material is prepared, and the separator and the negative electrode are not integrated materials.
与实施例1相比,制备锂的双离子电池的过程中,所采用的是隔膜与负极分离的形式装配得到的锂的双离子电池。Compared with Example 1, in the process of preparing a lithium dual-ion battery, a lithium dual-ion battery assembled in the form of a separator and a negative electrode separated is used.
实施例17Example 17
与实施例2相比,制备一体化结构的隔膜负极材料的过程中,“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”修改为“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为1%:9%的浓度溶于二甲基甲酰胺(DMF)中”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 2, in the process of preparing the membrane negative electrode material of the integrated structure, "polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in two at a volume mass concentration of 7%: 3%. "Methylformamide (DMF)" is amended to "Dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) with a volume mass concentration of 1%: 9% in dimethylformamide (DMF) ", all other steps, materials used, and process parameters are the same, and the separator negative electrode material with the integrated structure is prepared.
与实施例2相比,制备锂离子电池的过程中,“利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例17制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂离子电池。Compared with Example 2, in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 17. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
实施例18Example 18
与实施例2相比,制备一体化结构的隔膜负极材料的过程中,“将聚丙烯腈 (PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”修改为“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为2%:8%的浓度溶于二甲基甲酰胺(DMF)中”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 2, in the process of preparing the membrane negative electrode material of the integrated structure, "polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in two at a volume mass concentration of 7%: 3%. "Methylformamide (DMF)" is revised to "Dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) with a volume mass concentration of 2%: 8% in dimethylformamide (DMF) ", all other steps, materials used, and process parameters are the same, and the separator negative electrode material with the integrated structure is prepared.
与实施例2相比,制备锂离子电池的过程中,“利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例18制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂离子电池。Compared with Example 2, in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 18 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
实施例19Example 19
与实施例2相比,制备一体化结构的隔膜负极材料的过程中,“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”修改为“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为3%:7%的浓度溶于二甲基甲酰胺(DMF)中”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 2, in the process of preparing the membrane negative electrode material of the integrated structure, "polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in two at a volume mass concentration of 7%: 3%. "Methylformamide (DMF)" is amended to "Dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) at a volume mass concentration of 3%: 7% concentration in dimethylformamide (DMF) ", all other steps, materials used, and process parameters are the same, and the separator negative electrode material with the integrated structure is prepared.
与实施例2相比,制备锂离子电池的过程中,“利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例19制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂离子电池。Compared with Example 2, in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 19 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
实施例20Example 20
与实施例2相比,制备一体化结构的隔膜负极材料的过程中,“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”修改为“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为4%:6%的浓度溶于二甲基甲酰胺(DMF)中”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 2, in the process of preparing the membrane negative electrode material of the integrated structure, "polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in two at a volume mass concentration of 7%: 3%. "Methylformamide (DMF)" is amended to "Dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) at a volume mass concentration of 4%: 6% concentration in dimethylformamide (DMF) ", all other steps, materials used, and process parameters are the same, and the separator negative electrode material with the integrated structure is prepared.
与实施例2相比,制备锂离子电池的过程中,“利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例20制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂离子电池。Compared with Example 2, in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 20. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
实施例21Example 21
与实施例2相比,制备一体化结构的隔膜负极材料的过程中,“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”修改为“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为5%:5%的浓度溶于二甲基甲酰胺(DMF)中”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 2, in the process of preparing the membrane negative electrode material of the integrated structure, "polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in two at a volume mass concentration of 7%: 3%. "Methylformamide (DMF)" amended to "Dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) at a volume mass concentration of 5%: 5% concentration in dimethylformamide (DMF) ", all other steps, materials used, and process parameters are the same, and the separator negative electrode material with the integrated structure is prepared.
与实施例2相比,制备锂离子电池的过程中,“利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例21制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂离子电池。Compared with Example 2, in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 21. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
实施例22Example 22
与实施例2相比,制备一体化结构的隔膜负极材料的过程中,“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”修改为“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为6%:4%的浓度溶于二甲基甲酰胺(DMF)中”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 2, in the process of preparing the membrane negative electrode material of the integrated structure, "polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in two at a volume mass concentration of 7%: 3%. "Methylformamide (DMF)" is amended to "Dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) with a volume mass concentration of 6%: 4% in dimethylformamide (DMF) ", all other steps, materials used, and process parameters are the same, and the separator negative electrode material with the integrated structure is prepared.
与实施例2相比,制备锂离子电池的过程中,“利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例22制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到 锂离子电池。Compared with Example 2, in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 22. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
实施例23Example 23
与实施例2相比,制备一体化结构的隔膜负极材料的过程中,“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”修改为“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为8%:2%的浓度溶于二甲基甲酰胺(DMF)中”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 2, in the process of preparing the membrane negative electrode material of the integrated structure, "polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in two at a volume mass concentration of 7%: 3%. "Methylformamide (DMF)" is amended to "Dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) at a volume mass concentration of 8%: 2% in dimethylformamide (DMF) ", all other steps, materials used, and process parameters are the same, and the separator negative electrode material with the integrated structure is prepared.
与实施例2相比,制备锂离子电池的过程中,“利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例23制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂离子电池。Compared with Example 2, in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 23. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
实施例24Example 24
与实施例2相比,制备一体化结构的隔膜负极材料的过程中,“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”修改为“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为9%:1%的浓度溶于二甲基甲酰胺(DMF)中”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 2, in the process of preparing the membrane negative electrode material of the integrated structure, "polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in two at a volume mass concentration of 7%: 3%. "Methylformamide (DMF)" is revised to "Dissolve polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) with a volume mass concentration of 9%:1% in dimethylformamide (DMF) ", all other steps, materials used, and process parameters are the same, and the separator negative electrode material with the integrated structure is prepared.
与实施例2相比,制备锂离子电池的过程中,“利用上述实施例2制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例24制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到锂离子电池。Compared with Example 2, in the process of preparing a lithium ion battery, "Using the integrated structure of the separator negative electrode material prepared in the above Example 2 to assemble a new battery by matching with the positive electrode" is modified to "Using the above embodiment 24. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a lithium ion battery.
实施例25Example 25
与实施例2相比,“将聚丙烯腈(PAN)与聚偏氟乙烯(PVDF)按体积质量浓度为7%:3%的浓度溶于二甲基甲酰胺(DMF)中”相同,制备单独的隔膜 材料,隔膜与负极不是一体化材料。Compared with Example 2, "Polyacrylonitrile (PAN) and polyvinylidene fluoride (PVDF) are dissolved in dimethylformamide (DMF) at a concentration of 7% by volume mass concentration: 3%". The preparation Separate separator material, separator and negative electrode are not integrated materials.
与实施例2相比,制备锂的双离子电池的过程中,所采用的是隔膜与负极分离的形式装配得到的锂离子电池。Compared with Example 2, in the process of preparing a lithium dual-ion battery, a lithium-ion battery assembled with a separator and a negative electrode separated is used.
实施例26Example 26
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“3%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "3%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例26制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 26 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery. All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例27Example 27
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“4%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "4%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例27制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 27. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例28Example 28
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“5%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "5%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的 一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例28制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 28 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例29Example 29
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“6%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "6%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例29制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 29. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例30Example 30
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“7%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "7%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例30制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 30 The prepared integrated structure of the separator negative electrode material is matched with the positive electrode to assemble a new battery." All other steps, materials used and process parameters are the same, and a potassium dual-ion battery is prepared.
实施例31Example 31
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“8%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "8%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例31制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 31. The prepared integrated structure of the diaphragm negative electrode material is matched with the positive electrode to assemble a new battery." All other steps, materials used and process parameters are the same, and a potassium dual-ion battery is prepared.
实施例32Example 32
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“9%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "9%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例32制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 32 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例33Example 33
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“11%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "11%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例33制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 33. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery." All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例34Example 34
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“12%”,其他所有步骤、使用的材料 和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing an integrated structure of the separator negative electrode material, the volume mass concentration of the polymer solution was changed from "10%" to "12%". All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例34制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 34 The prepared negative electrode material of the integrated structure of the diaphragm is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例35Example 35
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“13%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution is changed from "10%" to "13%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例35制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 35. The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例36Example 36
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子聚合物溶液的体积质量浓度由“10%”修改为“14%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing an integrated structure of the negative electrode material for the separator, the volume mass concentration of the polymer solution was changed from "10%" to "14%". All other steps, materials used, and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例36制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 36 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例37Example 37
与实施例3相比,制备一体化结构的隔膜负极材料的过程中,所述高分子 聚合物溶液的体积质量浓度由“10%”修改为“15%”,其他所有步骤、使用的材料和工艺参数均相同,制备得到所述一体化结构的隔膜负极材料。Compared with Example 3, in the process of preparing the membrane negative electrode material of the integrated structure, the volume mass concentration of the polymer solution was changed from "10%" to "15%". All other steps, materials used and The process parameters are the same, and the diaphragm negative electrode material with the integrated structure is prepared.
与实施例3相比,制备钾的双离子电池中,“利用上述实施例3制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”修改为“利用上述实施例37制备得到的一体化结构的隔膜负极材料,通过与正极进行匹配,组装新的电池”,其他所有步骤、使用的材料和工艺参数均相同,制备得到钾的双离子电池。Compared with Example 3, in the preparation of a potassium dual-ion battery, "Using the integrated structure of the separator anode material prepared in the above Example 3, through matching with the positive electrode, to assemble a new battery" is modified to "Using the above embodiment 37 The prepared negative electrode material of the integrated structure of the separator is matched with the positive electrode to assemble a new battery". All other steps, materials used and process parameters are the same to prepare a potassium dual-ion battery.
实施例38Example 38
与实施例3相比,“所述高分子聚合物溶液的体积质量浓度10%”相同,制备单独的隔膜材料,隔膜与负极不是一体化材料。Compared with Example 3, "the volume mass concentration of the polymer solution is 10%" is the same, and a separate separator material is prepared, and the separator and the negative electrode are not an integrated material.
与实施例3相比,制备钾的双离子电池的过程中,所采用的是隔膜与负极分离的形式装配得到的钾离子电池。Compared with Example 3, in the process of preparing the potassium dual ion battery, a potassium ion battery assembled in the form of separation of the separator and the negative electrode is used.
对比例1Comparative example 1
采用PP材料为隔膜制备得到的二次电池,所述二次电池的隔膜与负极材料为分开的。The secondary battery is prepared by using PP material as the separator, and the separator of the secondary battery is separated from the negative electrode material.
结果分析Result analysis
对上述实施例1~实施例3制备得到的二次电池分别进行充放电测试,并进行分析比较。The secondary batteries prepared in the foregoing Examples 1 to 3 were respectively subjected to charge and discharge tests, and analyzed and compared.
将实施例1、实施例4、实施例5、实施例6~实施例16制备得到的二次电池分别进行充放电测试,并进行分析比较,结果如下表1所示,由表1可得,实施例1制备得到的二次电池为单层高分子材料的纺丝结构层的一体化结构的隔膜负极材料,在循环圈数为300圈时,所述容量保持率为84%,库伦效率为95%;实施例4制备得到的二次电池为双层不同高分子材料的纺丝结构层的一体化结构的隔膜负极材料,在循环圈数为300圈时,所述容量保持率为75%,库伦效率为90.1%;实施例5制备得到的二次电池为三层不同高分子材料的纺丝结构层的一体化结构的隔膜负极材料,在循环圈数为300圈时,所述容量保 持率为70%,库伦效率为87.2%;通过对实施例1、实施例4、实施例5制备得到的二次电池进行分析,可以发现,当一体化结构的隔膜负极材料为单层高分子材料的纺丝结构层时,所制备得到的二次电池,其容量保持率、库伦效率最高,分别达到84%和95.0%,保证制备得到的二次电池具有较好的电池性能。The secondary batteries prepared in Example 1, Example 4, Example 5, and Example 6 to Example 16 were respectively subjected to charge and discharge tests, and analyzed and compared. The results are shown in Table 1 below, which can be obtained from Table 1. The secondary battery prepared in Example 1 is a single-layer polymer material spun structure layer integrated structure separator anode material. When the number of cycles is 300, the capacity retention rate is 84%, and the coulombic efficiency is 95%; The secondary battery prepared in Example 4 is an integrated structure of the separator anode material with a double-layer spinning structure layer of different polymer materials. When the number of cycles is 300, the capacity retention rate is 75% , The coulombic efficiency is 90.1%; the secondary battery prepared in Example 5 is an integrated structure of the separator anode material with three layers of different polymer material spinning structure layers. When the number of cycles is 300, the capacity is maintained The rate is 70%, and the Coulomb efficiency is 87.2%. Through the analysis of the secondary batteries prepared in Example 1, Example 4, and Example 5, it can be found that when the integrated structure of the separator anode material is a single-layer polymer material When the spinning structure layer is used, the prepared secondary battery has the highest capacity retention rate and coulombic efficiency, reaching 84% and 95.0%, respectively, which ensures that the prepared secondary battery has better battery performance.
分析实施例1、实施例6~实施例15制备得到的二次电池,由表1中可得,当制备一体化结构的隔膜负极材料的过程中,当所述聚丙烯腈(PAN)的体积质量浓度当从5%上升至10%时,相应制备得到的二次电池的容量保持率和库伦效率呈上升趋势,当所述聚丙烯腈(PAN)的体积质量浓度当从10%上升至15%时,相应制备得到的二次电池的容量保持率和库伦效率呈下降趋势,当所述聚丙烯腈(PAN)的体积质量浓度为10%制备得到的二次电池(实施例1制备得到的二次电池)的容量保持率和库伦效率达到最大值,分别为84%和95%。The secondary batteries prepared in Analyzing Example 1, Example 6 to Example 15 can be obtained from Table 1. When preparing an integrated structure of the separator negative electrode material, when the volume of the polyacrylonitrile (PAN) is When the mass concentration increases from 5% to 10%, the capacity retention and coulombic efficiency of the secondary battery prepared accordingly show an upward trend. When the volume mass concentration of the polyacrylonitrile (PAN) increases from 10% to 15% %, the capacity retention and coulombic efficiency of the secondary battery prepared accordingly show a downward trend. When the volume mass concentration of the polyacrylonitrile (PAN) is 10%, the prepared secondary battery (the prepared in Example 1 The capacity retention rate and coulombic efficiency of the secondary battery reached the maximum value, which were 84% and 95%, respectively.
分析实施例1和实施例16制备得到的二次电池,其中,实施例16所采用的聚丙烯腈(PAN)的体积质量浓度与实施例1一致,不同之处在于,实施例16为隔膜与负极分开的方式,由表1可得,实施例16制备得到的二次电池的容量保持率和库伦效率分别为60%和80%,远远低于实施例1制备得到的二次电池的容量保持率和库伦效率,因此,说明一体化结构的隔膜负极材料的使用能够大幅提高二次电池的电池充放电性能和安全性能。Analyze the secondary batteries prepared in Example 1 and Example 16. Among them, the volume mass concentration of polyacrylonitrile (PAN) used in Example 16 is the same as that in Example 1. The difference is that Example 16 is a diaphragm and The method of separating the negative electrode can be obtained from Table 1. The capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 16 are 60% and 80%, respectively, which are far lower than the capacity of the secondary battery prepared in Example 1. The retention rate and the Coulomb efficiency, therefore, indicate that the use of an integrated structure of the separator anode material can greatly improve the battery charge and discharge performance and safety performance of the secondary battery.
表1Table 1
Figure PCTCN2020139234-appb-000001
Figure PCTCN2020139234-appb-000001
Figure PCTCN2020139234-appb-000002
Figure PCTCN2020139234-appb-000002
将实施例2、实施例17~实施例25制备得到的二次电池分别进行充放电测试,并进行分析比较,结果如下表2所示,分析实施例2、实施例17~实施例24制备得到的二次电池,由表2中可得,实施例2制备得到的二次电池,当电池循环圈数为200圈时,所述二次电池的容量保持率和库伦效率分别为82%和91.2%。当制备一体化结构的隔膜负极材料的过程中,当所述高分子聚合物PAN和PVDF的体积质量浓度发生变化时,相应制备得到的二次电池的容量保持率和库伦效率也发生改变,当从PAN和PVDF的浓度比从(1%:9%)上升至(7%:3%),相应制备得到的二次电池的容量保持率和库伦效率呈上升趋势,当PAN和PVDF的浓度比从(7%:3%)上升至(9%:1%),相应制备得到的二次电池的容量保持率和库伦效率呈下降趋势,当所述PAN和PVDF的浓度比为7%:3%制备得到的二次电池(实施例2制备得到的二次电池)的容量保持率和库伦效率达到最大值,分别为82%和91.2%。The secondary batteries prepared in Example 2 and Example 17 to Example 25 were respectively subjected to charge and discharge tests, and analyzed and compared. The results are shown in Table 2 below. The secondary battery can be obtained from Table 2. For the secondary battery prepared in Example 2, when the number of battery cycles is 200, the capacity retention rate and coulombic efficiency of the secondary battery are 82% and 91.2, respectively %. In the process of preparing an integrated structure of the separator negative electrode material, when the volume mass concentration of the polymer PAN and PVDF changes, the capacity retention rate and coulombic efficiency of the secondary battery prepared accordingly also change. From the concentration ratio of PAN and PVDF from (1%: 9%) to (7%: 3%), the capacity retention rate and coulombic efficiency of the secondary battery prepared accordingly show an upward trend, when the concentration ratio of PAN and PVDF From (7%: 3%) to (9%: 1%), the capacity retention and coulombic efficiency of the secondary battery prepared accordingly show a downward trend, when the concentration ratio of PAN and PVDF is 7%: 3 % The capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 2 (the secondary battery prepared in Example 2) reached the maximum values, which were 82% and 91.2%, respectively.
分析实施例2和实施例25制备得到的二次电池,其中,实施例25所采用PAN和PVDF的浓度比的与实施例2一致,不同之处在于,实施例25为隔膜与负极分开的方式,由表2可得,实施例25制备得到的二次电池的容量保持率和库伦效率分别为63%和76.1%,远远低于实施例2制备得到的二次电池的容量保持率和库伦效率,因此,说明一体化结构的隔膜负极材料的使用能够大幅提高二次电池的电池充放电性能和安全性能。Analyze the secondary batteries prepared in Example 2 and Example 25. Among them, the concentration ratio of PAN and PVDF used in Example 25 is the same as that in Example 2. The difference is that Example 25 uses a method in which the separator is separated from the negative electrode. As shown in Table 2, the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 25 are 63% and 76.1%, respectively, which are far lower than the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 2 Therefore, it shows that the use of an integrated structure of the separator anode material can greatly improve the battery charge and discharge performance and safety performance of the secondary battery.
表2Table 2
Figure PCTCN2020139234-appb-000003
Figure PCTCN2020139234-appb-000003
将实施例3、实施例26~实施例38制备得到的二次电池分别进行充放电测试,并进行分析比较,结果如下表3所示,分析实施例3、实施例26~实施例37制备得到的二次电池,由表3中可得,实施例3制备得到的二次电池,当电池循环圈数为300圈时,所述二次电池的容量保持率和库伦效率分别为80%和81.0%。当制备一体化结构的隔膜负极材料的过程中,当所述高分子聚合物PAN的体积质量浓度发生变化时,相应制备得到的二次电池的容量保持率和库伦效率也发生改变,当从PAN的体积质量浓度从3%上升至10%时,相应制备得到的二次电池的容量保持率和库伦效率呈上升趋势,当PAN的体积质量浓度从10%上升至15%时,相应制备得到的二次电池的容量保持率和库伦效率呈下降趋势,当所述PAN的体积质量浓度为10%制备得到的二次电池(实施例3制备得到的二次电池)的容量保持率和库伦效率达到最大值,分别为80%和81%。The secondary batteries prepared in Example 3 and Example 26 to Example 38 were respectively subjected to charge and discharge tests, and analyzed and compared. The results are shown in Table 3 below. The results are prepared in Example 3 and Example 26 to Example 37 The secondary battery can be obtained from Table 3. For the secondary battery prepared in Example 3, when the number of cycles of the battery is 300, the capacity retention rate and the coulombic efficiency of the secondary battery are 80% and 81.0, respectively %. In the process of preparing an integrated structure of the separator negative electrode material, when the volume mass concentration of the polymer PAN changes, the capacity retention rate and coulombic efficiency of the secondary battery prepared accordingly also change. When the volume mass concentration of PAN rises from 3% to 10%, the capacity retention and coulombic efficiency of the secondary battery prepared accordingly show an upward trend. When the volume mass concentration of PAN rises from 10% to 15%, the correspondingly prepared The capacity retention rate and coulombic efficiency of the secondary battery show a downward trend. When the volume mass concentration of the PAN is 10%, the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 3 (the secondary battery prepared in Example 3) reach The maximum values are 80% and 81%, respectively.
分析实施例3和实施例38制备得到的二次电池,其中,实施例38所采用PAN的体积质量浓度的与实施例3一致,不同之处在于,实施例38为隔膜与负极分开的方式,由表3可得,实施例38制备得到的二次电池的容量保持率和 库伦效率分别为60%和70%,远远低于实施例3制备得到的二次电池的容量保持率和库伦效率,因此,说明一体化结构的隔膜负极材料的使用能够大幅提高二次电池的电池充放电性能和安全性能。Analyze the secondary batteries prepared in Example 3 and Example 38. Among them, the volume mass concentration of PAN used in Example 38 is the same as that in Example 3. The difference is that Example 38 uses a method in which the separator is separated from the negative electrode. From Table 3, the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 38 are 60% and 70%, respectively, which are far lower than the capacity retention rate and coulombic efficiency of the secondary battery prepared in Example 3 Therefore, it is explained that the use of an integrated structure of the separator negative electrode material can greatly improve the battery charging and discharging performance and safety performance of the secondary battery.
表3table 3
Figure PCTCN2020139234-appb-000004
Figure PCTCN2020139234-appb-000004
进一步对实施例1制备得到的一体化结构的隔膜负极材料和二次电池进行分析,对实施例1制备得到的一体化结构的隔膜负极材料进行分析,由电镜分析可得,所述一体化结构的隔膜负极材料的高分子纺丝结构层的形貌如图6所示,所述一体化结构的隔膜负极材料的高分子纺丝结构层的截面示意图如图7所示,由图6和图7可清楚分析得到一体化结构的隔膜负极材料的形态。进一步分析实施例1制备得到的含有一体化结构的隔膜负极材料的二次电池与隔膜材料为PP隔膜的二次电池的充放电循环稳定性能。由图8可得,实施例1制备得到的二次电池,当循环圈数为650圈时,该二次电池的充放电的比容量仍 能保持75~80mAh/g;其库伦效率也能保持在95~96%。由图9可得,隔膜材料为PP隔膜的二次电池,当循环圈数为400圈时,该二次电池的充放电的比容量逐渐下降,仅仅为10~15mAh/g;其库伦效率也只有80%。The integrated structure diaphragm anode material and the secondary battery prepared in Example 1 are further analyzed, and the integrated structure diaphragm anode material prepared in Example 1 is analyzed, and it can be obtained from the electron microscope analysis that the integrated structure The morphology of the polymer spinning structure layer of the separator negative electrode material is shown in Figure 6, and the cross-sectional schematic diagram of the polymer spinning structure layer of the integrated structure separator negative electrode material is shown in Figure 7, from Figures 6 and 7 The morphology of the separator anode material with integrated structure can be clearly analyzed. Further analysis of the charge-discharge cycle stability performance of the secondary battery containing the separator negative electrode material of the integrated structure prepared in Example 1 and the secondary battery whose separator material is a PP separator. It can be seen from Figure 8 that the secondary battery prepared in Example 1, when the number of cycles is 650, the charge and discharge specific capacity of the secondary battery can still maintain 75-80 mAh/g; its coulombic efficiency can also be maintained In 95-96%. It can be seen from Figure 9 that the secondary battery with the separator material made of PP separator, when the number of cycles is 400, the specific capacity of the secondary battery for charging and discharging gradually decreases, only 10-15 mAh/g; its Coulomb efficiency is also Only 80%.
进一步对实施例1、实施例2制备得到的一体化结构的隔膜负极材料和PP材料的隔膜的浸润性进行比较,如图10所示,(a)为实施例1所述的一体化结构的隔膜负极材料的纺丝隔膜,(b)为实施例2所述的一体化结构的隔膜负极材料的纺丝隔膜,(c)为PP隔膜,由图8中的颜色可判断得到,(a)和(b)的浸润更透彻,浸润效果优于(c)。Further compare the wettability of the separator anode material of the integrated structure prepared in Example 1 and Example 2 and the separator of the PP material, as shown in FIG. 10, (a) is the integrated structure of Example 1 The spun separator of the negative electrode material of the separator, (b) is the spun separator of the integrated structure of the negative electrode material of the separator described in Example 2, (c) is the PP separator, which can be judged by the color in Figure 8, (a) And (b) infiltration is more thorough, and the infiltration effect is better than (c).
因此,本发明所述一体化结构的隔膜负极材料,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层,一方面,所述隔膜层为高分子隔膜层,高分子隔膜层具有良好的柔性,并且具有一定的坚韧性和可控的孔隙率,可以较好地抑制负极金属负极在使用过程中体积膨胀粉化的问题,保证金属负极不会形成毛刺而刺穿隔膜,保证二次电池的安全性能;另一方面,所述高分子隔膜层通过纺丝工艺与所述金属负极结合形成一体化结构,使隔膜与金属负极负极二者进行结合,进一步增加了隔膜与金属负极负极之间的有效接触,并且使制备得到的一体化结构的隔膜负极材料的厚度和形状可随意设计,柔韧性良好,一定程度上抑制了二次电池循环中,金属箔材负极易造成膨胀粉化的问题,提高二次电池安全性能和库伦效率。Therefore, in the integrated structure of the negative electrode material of the separator of the present invention, the negative electrode material of the integrated structure of the separator includes a metal negative electrode, and a polymer separator layer bonded to either side of the metal negative electrode. On the one hand, the separator layer is The polymer membrane layer, the polymer membrane layer has good flexibility, and has a certain degree of toughness and controllable porosity, which can better inhibit the volume expansion and pulverization of the negative metal negative electrode during use, and ensure that the metal negative electrode is not It will form burrs and pierce the diaphragm to ensure the safety performance of the secondary battery; on the other hand, the polymer diaphragm layer is combined with the metal negative electrode through a spinning process to form an integrated structure, so that both the diaphragm and the metal negative electrode are combined. The combination further increases the effective contact between the separator and the metal negative electrode, and the thickness and shape of the prepared integrated structure separator negative electrode material can be designed at will, and the flexibility is good, which to a certain extent prevents the secondary battery from cycling. , The metal foil negative electrode is easy to cause the problem of swelling and pulverization, which improves the safety performance and coulomb efficiency of the secondary battery.
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above descriptions are only the preferred embodiments of the present invention and are not intended to limit the present invention. Any modification, equivalent replacement and improvement made within the spirit and principle of the present invention shall be included in the protection of the present invention. Within range.

Claims (10)

  1. 一种一体化结构的隔膜负极材料的制备方法,其特征在于,所述制备方法包括如下步骤:A method for preparing a separator negative electrode material with an integrated structure is characterized in that the preparation method includes the following steps:
    配制高分子聚合物溶液并置于静电纺丝装置的注射器中;Prepare the high molecular polymer solution and place it in the syringe of the electrostatic spinning device;
    将所述金属负极放置于静电纺丝装置设备内,设置静电纺丝的电源电压为5~30kV,所述注射器与所述金属负极的距离为5~50cm,控制所述高分子聚合物溶液的流速为300~1000μL/h,在所述金属负极的表面静电纺丝制备高分子隔膜层,得到所述一体化结构的隔膜负极材料。Place the metal negative electrode in an electrospinning device, set the electrospinning power supply voltage to be 5-30kV, the distance between the syringe and the metal negative electrode is 5-50cm, and control the polymer solution The flow rate is 300-1000 μL/h, and the polymer diaphragm layer is prepared by electrostatic spinning on the surface of the metal negative electrode to obtain the diaphragm negative electrode material of the integrated structure.
  2. 根据权利要求1所述的一体化结构的隔膜负极材料的制备方法,其特征在于,所述高分子隔膜层为一层高分子纺丝结构层或多层高分子纺丝结构层;和/或,The method for preparing an integrated structure separator negative electrode material according to claim 1, wherein the polymer separator layer is a layer of a polymer spinning structure layer or a multi-layer polymer spinning structure layer; and/or ,
    所述金属负极选自负极集流体和负极材料一体化的金属负极。The metal negative electrode is selected from a metal negative electrode in which a negative electrode current collector and a negative electrode material are integrated.
  3. 根据权利要求1所述的一体化结构的隔膜负极材料的制备方法,其特征在于,所述高分子聚合物溶液包括高分子聚合物溶质、添加剂和溶剂;和/或,The method for preparing a separator negative electrode material with an integrated structure according to claim 1, wherein the high molecular polymer solution comprises a high molecular polymer solute, an additive and a solvent; and/or,
    所述金属负极的材料选自铝、锡、镁、锌、铜、铁、镍、钛、锰、锑、铋等发生合金化电池反应的的一种或含有至少一种所述金属元素的合金。The material of the metal negative electrode is selected from one of aluminum, tin, magnesium, zinc, copper, iron, nickel, titanium, manganese, antimony, bismuth, etc. that undergo alloying battery reactions or an alloy containing at least one of the metal elements .
  4. 根据权利要求3所述的一体化结构的隔膜负极材料的制备方法,其特征在于,所述高分子聚合物溶液中高分子聚合物的体积百分比浓度为1%~30%。The method for preparing an integrated structured separator negative electrode material according to claim 3, wherein the volume percentage concentration of the high molecular polymer in the high molecular polymer solution is 1%-30%.
  5. 根据权利要求3所述的一体化结构的隔膜负极材料的制备方法,其特征在于,所述高分子聚合物溶质选自聚甲基丙烯酸甲酯、丙烯酸四氢全氟辛酯、聚乙烯醇、聚乙烯基苯酚、聚氯乙烯、聚乙烯咔唑、聚偏二氟乙烯、聚偏二氟乙烯-六氟丙烯、聚丙烯腈、聚乳酸的至少一种;和/或,The method for preparing an integrated structure separator negative electrode material according to claim 3, wherein the high molecular polymer solute is selected from the group consisting of polymethyl methacrylate, tetrahydroperfluorooctyl acrylate, polyvinyl alcohol, At least one of polyvinylphenol, polyvinyl chloride, polyvinylcarbazole, polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene, polyacrylonitrile, and polylactic acid; and/or,
    所述添加剂选自Al 2O 3、SiO 2、如Li 0.5La 0.5TiO 3的钙钛矿构型ABO 3的物质、如Li 14Zn(GeO 4) 4的LISICON结构的物质、如Na 3Zr 2Si 2PO 12的NASICON结构的物质、如Li 7La 3Zr 2O 12的石榴石型氧化物物质的至少一种;和/或, The additives are selected from Al 2 O 3 , SiO 2 , materials with perovskite configuration ABO 3 such as Li 0.5 La 0.5 TiO 3 , materials with LISICON structure such as Li 14 Zn(GeO 4 ) 4 , such as Na 3 Zr 2 At least one of the NASICON structure material of Si 2 PO 12 , such as the garnet type oxide material of Li 7 La 3 Zr 2 O 12; and/or,
    所述溶剂选自四氢呋喃、丙酮、二甲基甲酰胺、二甲基乙酰胺、甲苯、水、 二氯甲烷、氯仿的至少一种。The solvent is selected from at least one of tetrahydrofuran, acetone, dimethylformamide, dimethylacetamide, toluene, water, dichloromethane, and chloroform.
  6. 根据权利要求1~5任一所述的一体化结构的隔膜负极材料的制备方法,其特征在于,还包括将得到所述一体化结构的隔膜负极材料于30~100℃下的条件下进行烘干处理。The method for preparing an integrated structured separator negative electrode material according to any one of claims 1 to 5, characterized in that it further comprises drying the obtained integrated structured separator negative electrode material at 30-100°C. Dry treatment.
  7. 一种一体化结构的隔膜负极材料,其特征在于,所述一体化结构的隔膜负极材料包括一金属负极,结合在所述金属负极任意一面的高分子隔膜层。A diaphragm negative electrode material with an integrated structure is characterized in that the diaphragm negative electrode material with an integrated structure comprises a metal negative electrode and a polymer diaphragm layer combined on any side of the metal negative electrode.
  8. 根据权利要求7所述的一体化结构的隔膜负极材料,其特征在于,所述高分子隔膜层的材料选自聚甲基丙烯酸甲酯、丙烯酸四氢全氟辛酯、聚乙烯醇、聚乙烯基苯酚、聚氯乙烯、聚乙烯咔唑、聚偏二氟乙烯、聚偏二氟乙烯-六氟丙烯、聚丙烯腈、聚乳酸的至少一种。The integrated structure separator anode material according to claim 7, wherein the material of the polymer separator layer is selected from the group consisting of polymethyl methacrylate, tetrahydroperfluorooctyl acrylate, polyvinyl alcohol, polyethylene At least one of base phenol, polyvinyl chloride, polyvinyl carbazole, polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene, polyacrylonitrile, and polylactic acid.
  9. 根据权利要求7所述的一体化结构的隔膜负极材料,其特征在于,所述高分子隔膜层的厚度为50μm~150μm。7. The integrated structure separator negative electrode material according to claim 7, wherein the thickness of the polymer separator layer is 50 μm to 150 μm.
  10. 一种二次电池,其特征在于,所述二次电池包括正极,一体化结构的隔膜负极材料以及电解液;其中,所述一体化结构的隔膜负极材料由所述权利要求1~6任一所述的一体化结构的隔膜负极材料的制备方法制备获得的或为所述权利要求7-9任一所述的一体化结构的隔膜负极材料。A secondary battery, characterized in that the secondary battery comprises a positive electrode, an integrated structure of the diaphragm negative electrode material and an electrolyte; wherein the integrated structure of the diaphragm negative electrode material is composed of any one of claims 1 to 6 The preparation method of the integrated structure of the negative electrode material of the separator is obtained by the preparation method or the negative electrode material of the integrated structure of any one of claims 7-9.
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