WO2022193188A1 - Negative electrode plate, electrochemical device, and electronic device - Google Patents

Negative electrode plate, electrochemical device, and electronic device Download PDF

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Publication number
WO2022193188A1
WO2022193188A1 PCT/CN2021/081366 CN2021081366W WO2022193188A1 WO 2022193188 A1 WO2022193188 A1 WO 2022193188A1 CN 2021081366 W CN2021081366 W CN 2021081366W WO 2022193188 A1 WO2022193188 A1 WO 2022193188A1
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Prior art keywords
lithium
layer
functional layer
pole piece
negative electrode
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PCT/CN2021/081366
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French (fr)
Chinese (zh)
Inventor
林小萍
陈茂华
谢远森
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宁德新能源科技有限公司
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Priority to CN202180004451.0A priority Critical patent/CN114127986B/en
Priority to PCT/CN2021/081366 priority patent/WO2022193188A1/en
Publication of WO2022193188A1 publication Critical patent/WO2022193188A1/en

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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
    • 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 application relates to the technical field of lithium batteries, and in particular, to a negative pole piece, an electrochemical device, and an electronic device.
  • Lithium batteries have the characteristics of high energy density and high power density, and are used more and more widely in electric vehicles and mobile electronic devices. With the continuous development of science and technology, in addition to energy density and power density, people pay more and more attention to the cycle life and safety performance of lithium batteries.
  • lithium ions are continuously reduced by electrons at the negative electrode. This process is prone to produce lithium dendrites. Lithium dendrites pierce through the separator, which will lead to a short circuit in the lithium battery and bring safety risks. Moreover, the continuously generated lithium dendrites are prone to fall off, resulting in "dead lithium” that cannot continue to participate in the reaction, resulting in a decrease in the capacity of lithium batteries during cycling. In addition, as the lithium battery is continuously charged and discharged, the volume of lithium continues to expand and shrink, and the negative electrode structure of the lithium battery is easily damaged, resulting in a sharp decrease in the capacity of the lithium battery, and there is a risk of potential safety hazards in severe cases.
  • the present application provides a negative pole piece, by designing the functional layer in the negative pole piece, the volume expansion of the negative pole piece is relieved, and the formation of lithium dendrites is suppressed, so that the battery including the negative pole piece is Chemical units have excellent cycle life and safety performance.
  • the present application also provides an electrochemical device, the electrochemical device includes the above-mentioned negative electrode plate, so the electrochemical device has excellent cycle life and safety performance.
  • the present application also provides an electronic device, the electronic device includes the above electrochemical device, so the electronic device has a long service life, strong endurance, high safety performance, and good user experience.
  • the application provides a negative pole piece, wherein the negative pole piece includes a functional layer; the functional layer includes M conductive layers and N dielectric layers arranged in layers, and the conductive layers include a lithium wetting material;
  • the functional layer of the negative electrode sheet of the present application includes a dielectric layer and a conductive layer to which a lithium wetting material is attached.
  • the dielectric layer can reduce the electron concentration of the functional layer and prevent lithium ions from forming dendrites at a large current density.
  • the dielectric layer can also reduce the electron concentration on the surface of the functional layer, forcing lithium ions to enter the functional layer.
  • the lithium wetting material can induce lithium ions to enter the functional layer for deposition, reducing the formation of lithium dendrites at the negative electrode interface Therefore, the cycle life and safety performance of the electrochemical device can be improved.
  • the three-dimensional skeleton formed by the stacking of the conductive layer and the dielectric layer can reduce the extrusion and expansion damage of the negative electrode pole piece by the lithium dendrite formed in the functional layer, and relieve the volume expansion of the negative pole piece during the cycle. Therefore, it can further Improve the cycle life and safety performance of electrochemical devices.
  • the conductive layer has equipotentiality.
  • the conductive layer can disperse the electric field at the top of the lithium dendrite, further restrain the continuous growth of the lithium dendrite, and realize the "self-correction" of the dendrite.
  • the cycle life and safety performance of the electrochemical device are improved.
  • the content of the lithium wetting material is distributed in a gradient in the stacking direction.
  • the deposition site of lithium ions is controlled by the distribution of the content of the lithium wetting material, which further induces the deposition of lithium ions at sites far away from the negative electrode interface, and suppresses the formation of lithium dendrites at the interface, thereby improving the safety performance and cycle life of the electrochemical device.
  • the negative pole piece further includes a lithium metal layer or a current collector, the functional layer is arranged on the functional surface of the lithium metal layer or the functional surface of the current collector, and the lithium metal layer is The extension direction or the extension direction of the current collector is perpendicular to the lamination direction;
  • the content of the lithium wetting material is gradually decreasing in a direction away from the lithium metal layer or current collector.
  • the dielectric layer can more effectively reduce the electron concentration on the surface of the functional layer, forcing lithium ions to enter the functional layer for deposition, reducing the deposition of lithium at the negative electrode interface, thereby suppressing lithium dendrites at the negative electrode interface
  • the formation of electrochemical devices improves the cycle life and safety performance of electrochemical devices.
  • the lithium wetting material has a high content near the lithium metal layer or current collector, and a low content near the anode interface, which further reduces the deposition of lithium at the anode interface, thereby suppressing the formation of lithium dendrites at the anode interface, enabling electrochemical devices.
  • the safety performance has been further improved.
  • the M conductive layers and the N dielectric layers are alternately stacked.
  • the alternate stacking of conductive layers and dielectric layers makes it easier for the lithium dendrites generated in the functional layer to contact the conductive layer, thereby realizing the conductive layer pair.
  • the "self-correction" of lithium dendrites prevents further growth of lithium dendrites in the functional layer, thus improving the cycle life and safety performance of electrochemical devices including the negative electrode.
  • the first edge layer and/or the second edge layer of the functional layer is a dielectric layer.
  • the lithium wetting material is distributed in the conductive layer. Therefore, when the first edge layer and/or the second edge layer of the functional layer is a dielectric layer, lithium ions are more likely to be deposited inside the functional layer, thereby reducing the negative electrode interface.
  • the deposition can inhibit the formation of lithium dendrites at the negative electrode interface, and therefore, the cycle life and safety performance of the electrochemical device including the negative electrode pole piece can be effectively improved.
  • the electrical conductivity of the conductive layer is 10 -7 S/cm to 10 6 S/cm, and/or,
  • the electrical conductivity of the dielectric layer is less than 10 -8 S/cm.
  • the conductivity of the conductive layer and/or the dielectric layer is in the above range, the current density in the functional layer is more conducive to the deposition of lithium ions inside the functional layer, and the formation of lithium dendrites is suppressed.
  • the device has excellent cycle life and safety performance.
  • the porosity of the functional layer is 5% to 90%, optionally 50% to 90%.
  • the functional layer can induce lithium ions to enter its interior and provide deposition sites for lithium ions, thereby suppressing interfacial lithium dendrites.
  • the formation of electrochemical devices improves the cycle life and safety performance of electrochemical devices.
  • the mass of the lithium wetting material is 5% to 95% of the mass of the functional layer, optionally 30% to 60%.
  • the content of lithium wetting material is too low, the ability to induce lithium ions to enter the internal deposition is low, and the functional pairing has limited ability to improve the cycle life and safety performance of electrochemical devices, and the content of lithium wetting material is too large. It has a negative effect on the energy density of the electrochemical device and the energy density of the electrochemical device; when the content of the lithium wetting material is 30% to 60%, it can induce lithium ions into the functional layer without affecting the energy density of the electrochemical device and the structural stability of the functional layer.
  • the inner layer is deposited, thereby reducing the probability of lithium ions staying at the negative electrode interface, reducing the formation of lithium dendrites at the interface, and improving the cycle life and safety performance of the electrochemical device.
  • the functional layer further includes lithium metal, and the content of the lithium metal in the functional layer is 0.25 mg/cm 2 to 25 mg/cm 2 .
  • the lithium metal in the functional layer can continuously replenish lithium for the negative electrode plate during the cycle, offset the irreversible lithium loss during the charging and discharging process, thereby further improving the cycle life of the electrochemical device including the negative electrode plate.
  • the present application also provides an electrochemical device, the electrochemical device comprising the above-mentioned negative electrode plate.
  • the electrochemical device of the present application includes the above-mentioned negative electrode plate, so the electrochemical device has more excellent cycle life and safety performance.
  • the present application also provides an electronic device, wherein the driving source or energy storage unit of the electronic device is the above-mentioned electrochemical device.
  • the driving source or energy storage unit of the electronic device of the present application adopts the above-mentioned electrochemical device, so the battery life, cycle life and safety performance are excellent, and the user experience is excellent.
  • FIG. 2 is a schematic diagram of a functional layer in another embodiment of the present application.
  • FIG. 3 is a schematic structural diagram of a negative pole piece in an embodiment of the application.
  • FIG. 4 is a schematic structural diagram of a negative pole piece in another embodiment of the present application.
  • FIG. 5 is a schematic structural diagram of a negative pole piece in yet another embodiment of the application.
  • Example 6 is a scanning electron microscope image of a negative pole piece in Example 8 of the application.
  • Example 7 is a scanning electron microscope image of the lithium deposition of the negative electrode pole piece in Example 11 of the application.
  • FIG. 8 is a scanning electron microscope image of the lithium deposition of the negative pole piece in Comparative Example 1 of the present application.
  • a first aspect of the present application provides a negative pole piece, the negative pole piece includes a functional layer; the functional layer includes M conductive layers and N dielectric layers arranged in layers, and the conductive layer includes a lithium wetting material;
  • FIG. 1 is a schematic diagram of a functional layer in an embodiment of the application.
  • the functional layer includes a stacked conductive layer a and a dielectric layer b, and the conductive layer a includes a lithium wetting material c;
  • FIG. 2 is a schematic diagram of a functional layer in another embodiment of the present application.
  • the functional layer includes a conductive layer a1, a conductive layer a2 and a dielectric layer b that are stacked in layers.
  • lithium is continuously deposited and dissolved in the negative pole piece, and the volume of lithium also increases and decreases, so that the volume of the negative pole piece expands and contracts.
  • lithium metal tends to form lithium dendrites on the negative pole piece, which creates the risk of piercing the separator and causing a short circuit.
  • the functional layer of the negative electrode piece of the present application includes a dielectric layer and a conductive layer attached with a lithium wetting material, wherein the dielectric layer can reduce the electron concentration on the surface of the functional layer and prevent lithium ions from forming dendrites at a large electron concentration; Moreover, the dielectric layer can prevent electrons from being transported to the surface of the functional layer, forcing lithium ions into the functional layer for deposition, thereby reducing the amount of lithium ion deposition at the negative electrode interface and inhibiting the formation of lithium dendrites at the negative electrode interface; and, in the induction of lithium wetting materials In this way, lithium ions can quickly enter the functional layer when migrating to the negative electrode, which further reduces the probability of lithium ions staying at the negative electrode interface, thereby maintaining the integrity of the negative electrode interface by further inhibiting the growth of interfacial lithium dendrites, not only avoiding the The potential safety hazard caused by the growth of interfacial lithium dendrites piercing the separator can effectively prevent the deteriorat
  • the structure of the functional layer of the negative electrode pole piece of the present application corresponds to a skeleton formed by stacking a conductive layer and a dielectric layer, so the functional layer has a certain space inside.
  • the skeleton structure of the functional layer can provide a certain growth space for lithium dendrites, which reduces the volume of lithium dendrites to a certain extent.
  • the extrusion and expansion damage of the negative pole piece maintains the cycle performance and safety performance of the electrochemical device.
  • the conductive layer also has a certain "self-correcting function".
  • the functional layer formed by the conductive layer and the dielectric layer including the lithium-wetting material not only reduces the formation of lithium dendrites in the functional layer, but also inhibits the growth of lithium dendrites at the interface, which is more
  • the volume expansion of the negative electrode plate during long-term application is effectively improved, so it is beneficial to the optimization of the cycle performance and safety performance of the electrochemical device.
  • the electrochemical device can also have good Coulomb efficiency.
  • the conductive layer can be a conductor material, such as copper, nickel, chromium, titanium, tungsten, zirconium, aluminum and its alloys and other metal materials; the material of the conductive layer can also be a semiconductor material, such as solid carbon spheres, hollow Carbon spheres, porous carbon, single-walled carbon nanotubes, multi-layered carbon nanotubes, pure carbon fibers, doped carbon fibers (including carbon fibers doped with oxides, sulfides, carbides, nitrides, metal elements, functional groups, etc.), graphite Carbon-based materials such as graphene cages, doped graphene and doped graphene derivatives.
  • This application can choose, but is not limited to the above-mentioned materials.
  • the dielectric layer can be made of polymer materials, such as polyvinylidene fluoride, polyimide, polyamide, polyacrylonitrile, polyethylene glycol, polyphenylene ether, polypropylene carbonate, Polymethyl methacrylate, polyethylene terephthalate, polyethylene oxide, polyvinylidene fluoride-hexafluoropropylene, polyvinylidene fluoride-chlorotrifluoroethylene, polyvinylidene fluoride-hexafluoropropylene At least one of fluoropropylene and polyvinylidene fluoride; the dielectric layer can also be an inorganic material, such as at least one of sodium silicate and its derivatives, aluminum oxide and its derivatives, silicon oxide and its derivatives. This application can choose, but is not limited to the above-mentioned materials.
  • the lithium wetting material can be a metal element, for example, silver, aluminum, gold, barium, calcium, indium, platinum, silicon, tin, zinc, cobalt, gallium; the lithium wetting material can also be a nitride such as molybdenum nitride, sulfide Such as molybdenum sulfide, tin sulfide.
  • the present application can also modify the conductive layer so that the conductive layer includes hydroxyl (-OH), ester (-COOR), carboxyl (-COOH), amino (-NH 2 ), sulfo (-SO) 3 H) and other lithiophilic functional groups to make the conductive layer include lithium wetting materials.
  • the present application does not strictly limit the manner of obtaining the conductive layer.
  • the present application can obtain the conductive layer by a combination of electrospinning and heat treatment. Specifically, a spinning solution is prepared by using a precursor capable of generating conductive substances and a solvent, electrospinning is performed by an electrospinning device to obtain a fiber film, and then the fiber film is heat-treated in an inert atmosphere to obtain a conductive layer.
  • a conductive paste containing a conductive substance and an adhesive it is also possible to formulate a conductive paste containing a conductive substance and an adhesive, and then select a suitable substrate, and coat the conductive paste on the substrate to obtain a conductive layer.
  • dielectric layer can also be obtained by means of electrospinning or coating, which will not be repeated in this application.
  • the present application does not impose strict restrictions on the manner of including the lithium wetting material in the conductive layer.
  • the present application may adopt the method of preparing the conductive layer by combining the above-mentioned electrospinning and heat treatment. Electrospinning is carried out by adding a precursor of a lithium-wetting material to electrospinning to obtain a fiber membrane including a lithium-wetting material precursor, and then when the fiber membrane is heat-treated, the lithium-wetting material precursor is converted into a lithium-wetting material, thereby making conductive
  • the layer includes a lithium wetting material.
  • a certain amount of lithium wetting material may be added to the conductive paste during the process of coating and preparing the conductive layer, so that the obtained conductive layer includes the lithium wetting material.
  • the present application does not strictly limit the method of stacking conductive layers and dielectric layers to obtain functional layers.
  • the present application can stack M conductive layers and N dielectric layers by means of hot pressing. Get functional layers.
  • the present application can also obtain a functional layer in which a conductive layer and a dielectric layer are stacked by coating.
  • a suitable substrate is selected to form M conductive layers and N dielectric layers.
  • the layered pastes are sequentially layered and applied on the surface of the substrate.
  • the present application further limits the content distribution of the lithium wetting material in the conductive layer, which is beneficial to further improve the safety performance and cycle life of the electrochemical device.
  • the content of the lithium wetting material in the negative pole piece is distributed in a gradient in the stacking direction.
  • the gradient distribution of the content of the lithium wetting material in the stacking direction includes an increasing gradient and a decreasing gradient, wherein the increasing gradient means that the content of the lithium wetting material in the jth conductive layer is less than the (j+1)th
  • the gradient decreasing means that the content of the lithium wetting material in the jth conductive layer is greater than the content of the lithium wetting material in the (j+1)th conductive layer, 1 ⁇ j ⁇ M.
  • the location where lithium ions are deposited in the functional layer can be controlled. It can be understood that lithium ions tend to be deposited in parts with a large content of lithium wetting material.
  • the content of lithium wetting material in the conductive layer far from the negative electrode interface is controlled to be greater than that in the conductive layer close to the negative electrode interface.
  • the content of lithium wetting material can reduce the deposition of lithium ions near the negative electrode interface, inhibit the formation of lithium dendrites at the negative electrode interface, maintain the integrity of the negative electrode interface, and avoid the formation of interfacial lithium dendrites piercing the diaphragm and causing short circuit.
  • the safety performance of the electrochemical device is further improved.
  • the content of the lithium wetting material is distributed in a gradient along the stacking direction inside the conductive layer a.
  • the concentration of the precursor of the lithium wetting material added to the electrospinning device at different time periods changes in a gradient.
  • the spinning solution can make the content of the lithium-wetting material gradient distributed along the thickness direction of the conductive layer a, and then stack the conductive layer a and the dielectric layer b along the thickness direction of the conductive layer a to obtain a functional layer, so that the conductive layer
  • the content of Li-wetting material in a is distributed gradiently in the stacking direction.
  • the functional layer includes two or more conductive layers (M ⁇ 2)
  • the content of the lithium-wetting material in each conductive layer is distributed in a gradient in the stacking direction, and the content of the lithium-wetting material in each conductive layer is uniformly distributed .
  • the content of the lithium wetting material is uniformly distributed in the conductive layer a1, the content of the lithium wetting material is uniformly distributed in the conductive layer a2, and the lithium wetting material in the conductive layer a1 is uniformly distributed
  • the content of the material is greater than the content of the lithium wetting material in the conductive layer a2, so that in the negative pole piece, the content of the lithium wetting material is distributed in a gradient in the stacking direction.
  • the content of the lithium wetting material precursor in the M spinning solutions is changed in a gradient, and then in the lamination process During the process, the conductive layer is laminated with the dielectric layer in the order of increasing or decreasing content of the precursor of the lithium-wetting material in the spinning solution.
  • the content of the lithium-wetting material in the M conductive pastes in the stacking direction can be changed in a gradient, so that the content of the lithium-wetting material in the stacking direction is changed. upper gradient distribution.
  • the content of the lithium-wetting material in one conductive layer can also be distributed in a gradient along the stacking direction, and, considering the induced deposition of lithium ions, the lithium-wetting material in one conductive layer
  • the gradient distribution of the content of the wetting material in the stacking direction is the same as the gradient distribution of the content of the lithium wetting material in the different conductive layers in the stacking direction, for example, the gradient is increasing simultaneously or the gradient is decreasing simultaneously.
  • the mass of the lithium-wetting material may be 5% to 95% of the mass of the functional layer, alternatively, 30% to 60%.
  • the higher the quality of the lithium-wetting material in the functional layer the better the lithophilicity of the functional layer, which is more conducive to inducing lithium ions to rapidly enter the functional layer for deposition.
  • blindly improving the quality of the lithium-wetting material is not conducive to the improvement of the mass energy density of the electrochemical device and the structural stability of the functional layer. Therefore, the quality of the lithium-wetting material can be controlled in the range of 30% to 60% of the quality of the functional layer. Therefore, without affecting the mass energy density of the electrochemical device, the probability of lithium ions at the negative electrode interface is reduced, the formation of lithium dendrites at the negative electrode interface is suppressed, and the cycle life and safety performance of the electrochemical device are improved.
  • some materials with good lithiophilic effect and low density can also be selected to further realize the unity of cycle life, safety performance and mass energy density of electrochemical devices.
  • the negative electrode sheet of the present application also includes a lithium metal layer or a current collector.
  • the lithium metal layer or current collector is in the form of flakes, and the two larger and opposite faces of the lithium metal layer or current collector are the functional surfaces.
  • the functional layer is provided on the functional surface.
  • the functional layer can be arranged on the functional surface by hot pressing; or as mentioned above, when the functional layer is obtained by coating, a lithium metal layer or a lithium metal layer can be used.
  • the current collector acts as a substrate.
  • the functional layer can also be placed directly on the functional surface of the lithium metal layer or current collector without forming a substantial connection between the functional layer and the functional surface. It can be understood that a substantial connection can be formed between the functional layer and the functional surface by means of hot pressing or coating, which is beneficial to further maintain the structural stability of the negative pole piece and the stability of the conductive network during the charging and discharging process.
  • whether the negative electrode plate includes a lithium metal layer or a current collector can be selected according to the purpose of the negative electrode plate.
  • the negative pole piece of the present application when used in a button battery, it is possible to choose not to use a lithium metal layer or a current collector, and use the functional layer directly as the negative electrode of the battery, so that the button battery can be lighter in weight. The mass energy density is further improved.
  • the negative pole piece of the present application when used in a wound type battery, the negative pole piece includes a lithium metal layer or a current collector to facilitate the arrangement of the tabs.
  • the current collector can be made of but not limited to copper foil.
  • the functional layer is arranged on the lithium metal layer.
  • the surface or the functional surface of the current collector and the extension direction of the lithium metal layer or the extension direction of the current collector is perpendicular to the stacking direction;
  • the content of the lithium wetting material is gradually decreasing in the direction away from the lithium metal layer or current collector.
  • FIG. 3 is a schematic structural diagram of a negative pole piece in an embodiment of the application.
  • the negative pole piece includes a lithium metal layer or current collector d and a functional layer e, and the functional layer e is disposed on the lithium metal layer or current collector A functional surface of d.
  • the direction of the middle arrow is the stacking direction, and the content of the lithium-wetting material gradually decreases in the direction away from the lithium metal layer or the current collector d.
  • the extending direction of the dielectric layer is parallel to the extending direction of the lithium metal layer or the current collector, and the area of the dielectric layer for blocking electron transfer is large, so the dielectric layer can more effectively reduce the
  • the electron concentration in the functional layer can effectively prevent the combination of lithium ions and electrons, and inhibit the formation of lithium dendrites in the functional layer; and the dielectric layer can more effectively reduce the electron concentration on the surface of the functional layer, forcing lithium ions into the functional layer for deposition.
  • the formation of lithium dendrites at the anode interface is reduced; thus, the cycle life and safety performance of electrochemical devices can be improved.
  • the content of Li-wetting material is low in the region away from the Li metal layer or current collector and high in the region close to the Li metal layer or current collector, therefore, lithium ions are more inclined to deposit in the region close to the Li metal layer or current collector , thereby reducing the formation of lithium dendrites near the negative electrode interface area, preventing lithium dendrites from piercing the separator and causing safety risks, thereby improving the safety performance of the electrochemical device.
  • the thickness of the functional layer along the stacking direction will have a certain influence on the electrical properties of the electrochemical device. If the thickness of the functional layer along the stacking direction is too large, the energy density of the electrochemical device will decrease. , while the thickness is too small, the improvement of the functional layer on the cycle life and safety performance of the electrochemical device is limited. When the thickness of the functional layer is between 50 ⁇ m and 100 ⁇ m, the electrochemical device can not only have good energy density, but also have excellent cycle life and safety performance.
  • the stacking direction and the extending direction of the lithium metal layer or the extending direction of the current collector may be parallel or at any acute angle.
  • FIG. 4 is a schematic structural diagram of a negative electrode pole piece in another embodiment of the present application.
  • the negative electrode pole piece includes a lithium metal layer or a current collector d and a functional layer e, and the functional layer e is disposed on the lithium metal layer or the current collector.
  • FIG. 5 is a schematic structural diagram of a negative electrode pole piece in another embodiment of the application.
  • the negative electrode pole piece includes a lithium metal layer or a current collector d and a functional layer e, and the functional layer e is disposed on the lithium metal layer or the collector.
  • the direction of extension is an acute angle, and the direction of the arrow in the figure is the stacking direction.
  • the inventors found that, compared with the embodiments shown in FIGS. 4 and 5 , the embodiment shown in FIG. 3 can be more conducive to the functional layer’s ability to inhibit the formation of lithium dendrites at the interface, so that the electrochemical performance can be improved.
  • the cycle life and safety performance of the device are better.
  • the functional layer disposed on the functional surface of the lithium metal layer or current collector includes the functional layer disposed on the lithium metal layer or current collector.
  • One functional surface and two functional surfaces of the fluid In the specific implementation process, one functional layer is provided on one functional surface of the lithium metal layer or current collector, or two functional layers are provided on two functional surfaces, and the stacking direction of the functional layers provided on different functional surfaces is related to the lithium metal layer or the current collector. The relationship of the fluid extension direction can be selected according to the needs of the negative pole piece.
  • the stacking sequence of the M conductive layers and the N dielectric layers has a certain influence on the performance of the functional layer.
  • the M conductive layers and the N dielectric layers of the present application are alternately stacked.
  • the cross-stacking arrangement of conductive layers and dielectric layers can make the generation of noise generated in the functional layer.
  • Lithium dendrites are easier to contact the conductive layer, which is more conducive to the "self-correction" of lithium dendrites by the conductive layer, thereby inhibiting the further growth of lithium dendrites, reducing the risk of lithium dendrites puncturing the separator and causing short circuits, and lithium dendrites.
  • the energy density loss caused by crystals can be improved, and the safety performance and cycle life of electrochemical devices can be improved.
  • the first edge layer and/or the second edge layer of the functional layer is a dielectric layer.
  • the first edge layer and/or the second edge layer of the functional layer respectively refers to the first layer and/or the last layer of the functional layer in the stacking direction.
  • the first edge layer and/or the second edge layer of the functional layer must be a dielectric layer.
  • M the first edge layer and/or the second edge layer of the functional layer in the present application is a dielectric layer.
  • the lithium wetting material is distributed in the conductive layer, when the first edge layer and/or the second edge layer is a dielectric layer, lithium ions are more likely to be deposited inside the functional layer, so the amount of lithium deposition at the negative electrode interface In this way, the formation of lithium dendrites at the negative electrode interface is suppressed, so that the cycle life and safety of the electrochemical device can be further improved.
  • the inventors found that when the conductivity of the conductive layer is 10 -7 S/cm to 10 6 S/cm, and/or, when the conductivity of the dielectric layer is less than 10 -8 S/cm, the electrochemical device has Better energy density, cycle life and safety performance.
  • the present application can optimize the current density in the functional layer by controlling the conductivity of the conductive layer and/or the conductivity of the dielectric layer, which is more conducive to the deposition of lithium ions inside the functional layer and inhibits the formation of lithium dendrites.
  • the conductivity of the conductive layer and/or the conductivity of the dielectric layer is within the above range, the current density in the functional layer will neither be too high, thereby increasing the risk of lithium dendrite formation in the functional layer, nor will the current density in the functional layer be too high. Therefore, the organic unity of safety performance, cycle performance and capacity of electrochemical devices can be realized.
  • the conductivity of the conductive layer is 10 -3 S/cm to 10 6 S/cm; when the material of the conductive layer is a semiconductor material, the conductivity of the conductive layer is 10 -7 to 10 3 .
  • the selection of conductive layer materials or dielectric layer materials, the selection of appropriate parameters in the preparation process of the conductive layer and/or the dielectric layer, the selection of the conductive layer and/or the dielectric layer preparation process The conductivity of the conductive layer and/or the dielectric layer is adjusted by adding a certain amount of conductive agent or insulating material, etc., so that the conductivity of the conductive layer and/or the dielectric layer is within the above range.
  • the porosity of the functional layer has a certain influence on the deposition of lithium metal in the functional layer.
  • the porosity of the functional layer the more favorable it is for the shuttle of lithium ions in the functional layer, inducing lithium ions to enter the functional layer more quickly for deposition, and the functional layer can have a larger specific surface area for the deposition of lithium ions. Provide more sites.
  • the large porosity of the functional layer often means that the functional layer has a large volume, which is not conducive to the improvement of the volumetric energy density of electrochemical devices. Therefore, the porosity of the functional layer is controlled in the range of 50% to 90%, so that lithium ions can be induced to enter the functional layer and deposited without affecting the volume energy density of the electrochemical device, and the interfacial lithium dendrite can be suppressed. formed to improve the cycle life and safety performance of electrochemical devices.
  • the materials of the conductive layer and the dielectric layer with suitable porosity, the thickness of the conductive layer and the dielectric layer, and the appropriate preparation process of the conductive layer and the dielectric layer can be selected. , spinning solution concentration), and the lamination process (eg, pressure and temperature of hot pressing) of the conductive layer and the dielectric layer make the porosity of the functional layer between 50% and 90%.
  • the good mechanical strength of the functional layer can realize the stability of the structure of the functional layer during the charge-discharge cycle, prevent the functional layer from being broken during the cycle, so that the functional layer can continue to function, and ensure the stable structure of the negative pole piece.
  • the mechanical strength of the functional layer can be adjusted by selecting the materials of the conductive layer and the dielectric layer with appropriate strength, combining the preparation process of the conductive layer and the dielectric layer, and the stacking process of the conductive layer and the dielectric layer.
  • the functional layer of the negative pole piece of the present application further includes lithium metal, and the content of lithium metal in the functional layer is 0.25 mg/cm 2 to 25 mg/cm 2 , that is, per square centimeter of the functional layer
  • the area includes 0.25mg to 25mg lithium metal.
  • the area of the functional layer refers to the area of the surface of the functional layer closest to the functional surface of the current collector.
  • the lithium lost in the discharge cycle can be supplemented, and the cycle life of the electrochemical device including the negative electrode plate can be further improved.
  • the functional layer may include the above-mentioned content of lithium metal by means of a melting method, a physical vapor deposition method, an electrochemical method, or the like.
  • a second aspect of the present application further provides an electrochemical device, the electrochemical device comprising the above-mentioned negative electrode plate.
  • an electrochemical device generally includes a positive electrode, an electrolyte (electrolyte), a separator, and the like in addition to the negative electrode.
  • the electrochemical device may be a wound battery, a laminated battery, a solid-state battery, and the like.
  • a suitable electrochemical device can be constructed by using the negative electrode plate of the present application, matched with a suitable positive electrode plate, electrolyte (electrolyte), separator, etc., as required.
  • the negative pole piece may only have a functional layer.
  • the extending direction of the functional layer may be parallel to the extending direction of the positive pole piece, so that the negative pole piece and the positive pole piece of the electrochemical device are opposite to each other. , and cooperate with the diaphragm and electrolyte (quality) to obtain an electrochemical device with excellent cycle life and safety performance.
  • the negative pole piece includes a functional layer and a current collector, and the functional layer is arranged on the functional surface of the current collector.
  • the functional layer included in the negative electrode plate can effectively reduce the volume expansion of the negative electrode plate and the formation of lithium dendrites during charge-discharge cycles, so that the electrochemical device has excellent cycle life and safety performance.
  • a third aspect of the present application further provides an electronic device, which includes the above electrochemical device.
  • An electrochemical device can be used as a driving source or an energy storage unit for the electronic device.
  • the electronic devices in this application can be, but are not limited to, mobile devices (eg, smart watches, mobile phones, notebook computers, etc.), electric vehicles (eg, electric bicycles, hybrid electric vehicles, power-assisted bicycles, etc.), and the like.
  • the electronic device of the present application includes the aforementioned electrochemical device, it has excellent endurance, service life and safety performance, and has a good user experience.
  • buttons cells of Examples 1-17 were all prepared according to the following methods.
  • the working state of the electrospinning device is set to control the thickness of the polyacrylonitrile fiber film;
  • the fiber membrane was placed in a muffle furnace, and the muffle furnace was heated to 230 °C at a heating rate of 1 °C per minute in an air atmosphere, and then kept for 2 hours.
  • the polyacrylonitrile fiber membrane was pre-oxidized, and the pre-oxidized polypropylene was The nitrile fiber film is heated to 800°C at a heating rate of 5°C per minute under an argon atmosphere in a tube furnace for 4 hours, and tin dioxide (lithium wetting material) is distributed in the obtained carbon fiber film to obtain a conductive layer;
  • a polyacrylonitrile fiber membrane can be obtained along the A polyacrylonitrile fiber film with a uniform distribution of tin tetrachloride content in the thickness direction;
  • the concentration of tin tetrachloride in the spinning solution was adjusted at different time periods so that the concentration of tin tetrachloride showed a gradient change, which could be obtained along the thickness direction of the polyacrylonitrile fiber film.
  • dielectric layer 0.8 parts by mass of polyvinylidene fluoride was dissolved in 10 parts by mass of N,N-dimethyl amide to obtain a spinning solution, and the spinning solution was injected into an electrospinning device for electrospinning The polyvinylidene fluoride fiber membrane was obtained, the working state of the electrospinning device was set, and the thickness of the polyvinylidene fluoride fiber membrane was controlled; electric layer;
  • step D the functional layer obtained in step C is arranged on a functional surface of the negative electrode current collector copper foil by means of hot pressing to obtain a negative electrode pole piece;
  • the stacking direction of the conductive layer and the dielectric layer is perpendicular to the extending direction of the copper foil current collector.
  • the positive electrode active material lithium iron phosphate, conductive carbon black, and polyvinylidene fluoride are mixed in a mass ratio of 97.5:1.0:1.5 and added to N-methylpyrrolidone to prepare a positive electrode slurry with a solid content of 0.75, and stir evenly.
  • the positive electrode slurry is uniformly coated on the functional surface of the current collector aluminum foil, the aluminum foil is dried at 90°C to obtain a positive electrode piece, and the positive electrode piece is punched into a sheet with a diameter of 14 mm;
  • the loading amount of the positive electrode active material on the positive electrode sheet is 1 mg/cm 2 .
  • the diameter of the battery case is 20mm, the height is 3.2mm, and the thickness is 0.25mm; the above-mentioned negative pole piece, positive pole piece, and separator are assembled according to the button battery assembly method commonly used in the field, and the side is assembled after assembly. Sealing - top sealing - liquid injection - packaging, and finally a button battery is obtained;
  • the separator is a polyethylene film with a thickness of 15 ⁇ m.
  • the preparation of the button battery in this example is basically the same as that in Example 1. The only difference is that this example does not pre-supplement lithium after obtaining the functional layer in step C of (1) preparing the negative pole piece.
  • the preparation of the button battery in this example is basically the same as that in Example 1. The only difference is that in this example, in the step D of (1) preparing the negative pole piece, the functional layer obtained in the step C is formed by hot pressing. When a negative electrode pole piece is obtained on a functional surface of the negative electrode current collector copper foil, the stacking direction of the dielectric layer and the conductive layer is parallel to the extending direction of the current collector.
  • the preparation steps of the button battery in this example are basically the same as those in Example 1. The only difference is that in (1) the preparation step D of the negative pole piece in this example, the functional layer is arranged before the negative electrode current collector copper foil. , using a 1.5T roller machine to roll the functional layer, and the rolling speed is 1m/min.
  • the preparation process of the button battery of this comparative example is as follows:
  • the carbon fiber film is punched into thin sheets with a diameter of 18 mm to obtain a conductive layer, which is placed on a functional surface of the negative electrode current collector copper foil by hot pressing, and lithium is pre-supplemented in the functional layer by an electrochemical method, so that lithium metal is functional.
  • the content in the layer is 4.1 mg/cm 2 to obtain a negative pole piece;
  • the preparation process of the button battery in this comparative example is as follows:
  • the preparation process of the button battery in this comparative example is as follows:
  • the liquid was injected into the electrospinning device for electrospinning to obtain a polyacrylonitrile fiber membrane, and the working state of the electrospinning device was set so that the thickness of the polyacrylonitrile fiber membrane was 60 ⁇ m; after that, the polyacrylonitrile fiber membrane was placed in a muffle furnace , in the air atmosphere at a heating rate of 1 °C per minute, the muffle furnace is heated to 230 °C and kept for 2 hours, the polyacrylonitrile fiber film is pre-oxidized, and the pre-oxidized polyacrylonitrile fiber film is placed in the tube furnace.
  • the temperature was raised to 800°C at a heating rate of 5°C per minute and held for 4 hours.
  • tin dioxide was uniformly distributed along the thickness direction of the carbon fiber film, and the carbon fiber film was punched into pieces with a diameter of 18 mm. , obtain a conductive layer, and set the conductive layer on a functional surface of the negative electrode current collector copper foil by hot pressing to obtain a negative electrode pole piece;
  • the composition of the negative pole piece, the concentration of tin tetrachloride in the spinning solution added to the electrospinning device at different spinning time periods when preparing each conductive layer, and the content of the lithium wetting material in the conductive layer in the direction away from the current collector The distribution and other parameters are shown in Table 1.
  • the thickness of the functional layer in the stacking direction in Table 1 was obtained by using the argon ion polishing CP method to prepare a sample of the negative pole piece and then observing it with a scanning electron microscope.
  • the porosity of the functional layer is tested by mercury intrusion method
  • thermogravimetric analyzer According to the national standard method GB/T 27761-2011, the content of tin dioxide in the material was tested by thermogravimetric analyzer.
  • Example 8 The microscopic morphology of the negative pole piece obtained in Example 8 was observed using a scanning electron microscope, and the results are shown in Figure 6;
  • the functional layer of the present application is formed by stacking a dielectric layer and a conductive layer, and has three-dimensional structure;
  • Example 11 and Comparative Example 1 The negative pole pieces obtained in Example 11 and Comparative Example 1 were charged to 3.7V with a constant current of 0.2C, then charged to 0.025C with a constant voltage, left for 5 minutes, and discharged to 2.55V with a constant current of 0.5C; cycle 10 times After that, let it stand for 5 minutes, and charge it with a constant current of 0.1C to a full charge state of 3.7V; the sample of the negative electrode piece was prepared by the argon ion polishing CP method, and then the sample was observed by scanning electron microscope. The results are shown in Figures 7 and 7, respectively. 8;
  • the deposition of lithium in the functional layer is very dense, and the deposition amount is large; while in the negative pole piece of Fig. 8, the deposition of lithium ions is very loose, and the deposition amount is also less;
  • the comparison shows that the negative electrode plate of the present application can effectively induce lithium deposition inside the functional layer, and the lithium deposition is very dense; moreover, as can be seen from Figure 7, lithium is not easily deposited in the area close to the negative electrode interface, therefore, the negative electrode interface
  • the formation of lithium dendrites is suppressed; therefore, it can be shown that when the stacking direction is perpendicular to the extension direction of the current collector, and the gradient of the lithium-wetting material decreases in the stacking direction, the negative electrode plate can induce the deposition of lithium ions in the region close to the current collector, reducing the The probability of lithium ions depositing on the negative electrode interface suppresses the formation of lithium dendrites on the negative electrode interface; thus the electrochemical device including the negative electrode pole piece can show better cycle life and
  • Example 6 100 80 99.48% Example 7 150 60 99.67% Example 8 130 80 99.64% Example 9 200 35 99.86% Example 10 180 40 99.78% Example 11 200 30 99.87% Example 12 180 35 99.81% Example 13 205 25 99.9% Example 14 180 30 99.84% Example 15 220 20 99.92% Example 16 180 50 99.7% Example 17 152 40 99.69% Example 18 50 30 97% Example 19 80 90 97.8% Example 20 128 90 99.63% Comparative Example 1 60 300 97.1% Comparative Example 2 70 100 97.5% Comparative Example 3 80 180 97.96% Comparative Example 4 50 500 96%
  • the batteries of the examples have a larger number of cycles and a smaller volume expansion rate, indicating that the negative pole piece of the electrochemical device satisfies the requirements of the present application.
  • the cycle performance and safety performance of the electrochemical device can be improved because: on the one hand, the dielectric layer can reduce the electron concentration of the functional layer, prevent lithium ions from forming dendrites at high current density, thereby inhibiting lithium dendrites In addition, the dielectric layer can also reduce the electron concentration on the surface of the functional layer, forcing lithium ions to deposit inside the functional layer, thus reducing the formation of lithium dendrites at the negative interface; on the other hand, the lithium wetting material can also induce lithium The ions are deposited inside the functional layer to reduce the formation of lithium dendrites at the negative electrode interface; in addition, the three-dimensional skeleton formed by the stacking of the conductive layer and the dielectric layer can reduce the extrusion and expansion damage of the negative electrode pole pieces by the
  • Example 3 Compared with Example 1 and 3, the battery of Example 3 has a larger number of cycles and a smaller volume expansion. When the content of the lithium wetting material is gradually decreased in the stacking direction, the cycle life of the electrochemical device is affected. The improvement of safety performance and safety performance is better, because the higher content of lithium wetting material in the region near the current collector can more effectively induce lithium ions to enter the functional layer to deposit, inhibit the formation of lithium dendrites at the negative electrode interface, so the electrochemical device It has better cycle life and safety performance; the same conclusion can also be drawn from the comparison of Example 4 and Example 6;
  • Example 9 Compared with Example 11, the battery of Example 9 shows a smaller volume expansion rate, and the safety performance of the electrochemical device is better. The reason is that the lithium wetting material is distributed in the conductive layer, so the functional When the first edge layer and/or the second edge layer of the layer is a dielectric layer, lithium ions are more inclined to be deposited in the inner conductive layer, thereby inhibiting the formation of lithium branches at the negative electrode interface and improving the safety performance of the electrochemical device;
  • Example 9 Compared with Example 9 and Example 10, the battery of Example 9 has better cycle life and safety performance. The reason is that when the layer of the functional layer closest to the negative electrode interface is a dielectric layer, the dielectric layer can Effectively inhibit the formation of interfacial lithium dendrites;
  • Example 15 the cycle number of the battery obtained in Example 18 is significantly larger than that in Example 15. This is because when lithium metal is included in the functional layer of the negative pole piece, lithium metal can supplement the cycle process. Therefore, the cycle life of electrochemical devices can be significantly improved;
  • Example 19 shows that the battery obtained in Example 19 has a small number of cycles and a large volume expansion rate, which shows that the cycle performance and safety performance of the battery are worse.
  • the functional layer in the other examples is The stacking direction is perpendicular to the extension direction of the current collector, and the dielectric layer can more effectively reduce the electron concentration of the functional layer and inhibit the formation of lithium dendrites at the anode interface, thereby improving the cycle life and safety performance of the electrochemical device.
  • Example 16 and Example 17 have worse cycle performance and safety performance than Example 13, because the content of lithium wetting material is too high (Example 13). 17), the structural stability of the functional layer is reduced, which is not conducive to the improvement of the cycle life and safety performance of the electrochemical device, and the energy density of the electrochemical device will also be affected; Therefore, when the quality of the lithium-wetting material is controlled to be 30% to 60% of the quality of the functional layer, it is more beneficial to improve the cycle life and safety of electrochemical devices. performance;
  • Example 20 has poor cycle performance and safety performance of the electrochemical device obtained in Example 20.
  • the reason is that the porosity of the functional layer is low, and lithium cannot smoothly enter the functional layer for deposition. Therefore, lithium tends to be deposited on the negative electrode interface, and it is easy to form interfacial lithium dendrites, which is not conducive to the cycle performance and safety performance of electrochemical devices.

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Abstract

The present application provides a negative electrode plate, an electrochemical device, and a related electronic device. The negative electrode plate comprises a functional layer. The functional layer comprises M conductive layers and N dielectric layers which are provided in a stacked manner, and each conductive layer comprises a lithium wetting material, wherein M≥1 and N≥1. The functional layer of the negative electrode plate of the present application can not only relieve the volume expansion of the negative electrode plate in a charging and discharging cycle, but also inhibit the formation of lithium dendrites; and the electrochemical device comprising the negative electrode plate can have good cycle life and safety performance, and thus can be more widely used in electronic devices.

Description

一种负极极片、电化学装置及电子装置A kind of negative pole piece, electrochemical device and electronic device 技术领域technical field
本申请涉及锂电池技术领域,尤其涉及一种负极极片、电化学装置及电子装置。The present application relates to the technical field of lithium batteries, and in particular, to a negative pole piece, an electrochemical device, and an electronic device.
背景技术Background technique
锂电池具有高能量密度、高功率密度等特点,在电动汽车和可移动电子设备中的使用越来越广泛。随着科学技术的不断发展,除了能量密度与功率密度以外,人们对锂电池的循环寿命和安全性能也越来重视。Lithium batteries have the characteristics of high energy density and high power density, and are used more and more widely in electric vehicles and mobile electronic devices. With the continuous development of science and technology, in addition to energy density and power density, people pay more and more attention to the cycle life and safety performance of lithium batteries.
在锂电池充电过程中,锂离子在负极不断发生得电子还原,这一过程易产生锂枝晶,锂枝晶刺穿隔膜会导致锂电池发生短路,带来安全风险。而且,不断生成的锂枝晶易发生脱落,产生不能继续参与反应的“死锂”,导致锂电池在循环过程中容量降低。此外,随着锂电池不断地充放电,锂不断地发生体积膨胀和收缩,锂电池的负极结构易被破坏,导致锂电池容量急剧下降,严重时有产生安全隐患的风险。During the charging process of lithium batteries, lithium ions are continuously reduced by electrons at the negative electrode. This process is prone to produce lithium dendrites. Lithium dendrites pierce through the separator, which will lead to a short circuit in the lithium battery and bring safety risks. Moreover, the continuously generated lithium dendrites are prone to fall off, resulting in "dead lithium" that cannot continue to participate in the reaction, resulting in a decrease in the capacity of lithium batteries during cycling. In addition, as the lithium battery is continuously charged and discharged, the volume of lithium continues to expand and shrink, and the negative electrode structure of the lithium battery is easily damaged, resulting in a sharp decrease in the capacity of the lithium battery, and there is a risk of potential safety hazards in severe cases.
因此,如何提高锂电池的循环寿命和安全性能是锂电池技术领域亟待解决的问题。Therefore, how to improve the cycle life and safety performance of lithium batteries is an urgent problem to be solved in the field of lithium battery technology.
发明内容SUMMARY OF THE INVENTION
为了解决上述技术问题,本申请提供一种负极极片,通过对负极极片中功能层进行设计,缓解负极极片的体积膨胀,抑制锂枝晶的形成,从而使得包括该负极极片的电化学装置具有优良的循环寿命和安全性能。In order to solve the above-mentioned technical problems, the present application provides a negative pole piece, by designing the functional layer in the negative pole piece, the volume expansion of the negative pole piece is relieved, and the formation of lithium dendrites is suppressed, so that the battery including the negative pole piece is Chemical units have excellent cycle life and safety performance.
本申请还提供一种电化学装置,该电化学装置包括上述负极极片,因此该电化学装置的循环寿命和安全性能表现优异。The present application also provides an electrochemical device, the electrochemical device includes the above-mentioned negative electrode plate, so the electrochemical device has excellent cycle life and safety performance.
本申请还提供一种电子装置,该电子装置包括上述的电化学装置,因此该电子装置使用寿命长、续航能力强、安全性能高,用户体验好。The present application also provides an electronic device, the electronic device includes the above electrochemical device, so the electronic device has a long service life, strong endurance, high safety performance, and good user experience.
本申请提供一种负极极片,其中,所述负极极片包括功能层;所述功能层包括层叠设置的M个导电层和N个介电层,所述导电层中包括锂润湿材料;The application provides a negative pole piece, wherein the negative pole piece includes a functional layer; the functional layer includes M conductive layers and N dielectric layers arranged in layers, and the conductive layers include a lithium wetting material;
其中,M≥1,N≥1。Among them, M≥1, N≥1.
本申请的负极极片的功能层包括介电层、以及附着有锂润湿材料的导电层。一方面,介电层能够降低功能层的电子浓度,防止锂离子在较大电流密度下形成枝晶,而且,介电层还能够降低功能层表面的电子浓度,迫使锂离子进入功能层内部进行沉积,降低功能层表面的锂离子还原量,从而抑制功能层表面锂枝晶的形成;另一方面,锂润湿材料能够诱导锂离子进入功能层内部进行沉积,降低负极界面锂枝晶的形成;因此,能够提升电化学装置的循环寿命和安全性能。此外,导电层与介电层层叠构成的三维骨架能够降低功能层内形成的锂枝晶对负极极片的挤压和膨胀损毁,缓解负极极片在循环过程中的体积膨胀,因此,能够进一步提升电化学装置的循环寿命和安全性能。而且,导电层具有等电位性,当锂枝晶接触导电层时,导电层能够使得锂枝晶顶部的电场得到分散,进一步遏制锂枝晶的继续生长,实现枝晶的“自纠错”,从而 改善电化学装置的循环寿命和安全性能。The functional layer of the negative electrode sheet of the present application includes a dielectric layer and a conductive layer to which a lithium wetting material is attached. On the one hand, the dielectric layer can reduce the electron concentration of the functional layer and prevent lithium ions from forming dendrites at a large current density. Moreover, the dielectric layer can also reduce the electron concentration on the surface of the functional layer, forcing lithium ions to enter the functional layer. deposition, reducing the amount of lithium ion reduction on the surface of the functional layer, thereby inhibiting the formation of lithium dendrites on the surface of the functional layer; on the other hand, the lithium wetting material can induce lithium ions to enter the functional layer for deposition, reducing the formation of lithium dendrites at the negative electrode interface Therefore, the cycle life and safety performance of the electrochemical device can be improved. In addition, the three-dimensional skeleton formed by the stacking of the conductive layer and the dielectric layer can reduce the extrusion and expansion damage of the negative electrode pole piece by the lithium dendrite formed in the functional layer, and relieve the volume expansion of the negative pole piece during the cycle. Therefore, it can further Improve the cycle life and safety performance of electrochemical devices. Moreover, the conductive layer has equipotentiality. When the lithium dendrite contacts the conductive layer, the conductive layer can disperse the electric field at the top of the lithium dendrite, further restrain the continuous growth of the lithium dendrite, and realize the "self-correction" of the dendrite. Thus, the cycle life and safety performance of the electrochemical device are improved.
如上所述的负极极片中,所述锂润湿材料的含量在层叠方向上梯度分布。In the above negative pole piece, the content of the lithium wetting material is distributed in a gradient in the stacking direction.
本申请通过对锂润湿材料含量的分布控制锂离子的沉积部位,进一步诱导锂离子沉积在远离负极界面的部位,抑制界面锂枝晶的生成,从而提高电化学装置的安全性能和循环寿命。In the present application, the deposition site of lithium ions is controlled by the distribution of the content of the lithium wetting material, which further induces the deposition of lithium ions at sites far away from the negative electrode interface, and suppresses the formation of lithium dendrites at the interface, thereby improving the safety performance and cycle life of the electrochemical device.
如上所述的负极极片中,所述负极极片还包括锂金属层或集流体,所述功能层设置在所述锂金属层的功能表面或集流体的功能表面且所述锂金属层的延伸方向或集流体的延伸方向与所述层叠方向垂直;In the above negative pole piece, the negative pole piece further includes a lithium metal layer or a current collector, the functional layer is arranged on the functional surface of the lithium metal layer or the functional surface of the current collector, and the lithium metal layer is The extension direction or the extension direction of the current collector is perpendicular to the lamination direction;
所述锂润湿材料的含量在远离所述锂金属层或集流体的方向上梯度递减。The content of the lithium wetting material is gradually decreasing in a direction away from the lithium metal layer or current collector.
当所述负极极片的按照上述方式实施时,介电层能够更有效降低功能层表面的电子浓度,迫使锂离子进入功能层内部进行沉积,减少负极界面锂沉积,从而抑制负极界面锂枝晶的形成,改善电化学装置的循环寿命和安全性能。此外,锂润湿材料在靠近锂金属层或集流体的区域含量高,靠近负极界面的含量低,更进一步减少锂在负极界面的沉积,从而抑制负极界面锂枝晶的形成,使得电化学装置的安全性能得到进一步提升。When the negative electrode pole piece is implemented in the above manner, the dielectric layer can more effectively reduce the electron concentration on the surface of the functional layer, forcing lithium ions to enter the functional layer for deposition, reducing the deposition of lithium at the negative electrode interface, thereby suppressing lithium dendrites at the negative electrode interface The formation of electrochemical devices improves the cycle life and safety performance of electrochemical devices. In addition, the lithium wetting material has a high content near the lithium metal layer or current collector, and a low content near the anode interface, which further reduces the deposition of lithium at the anode interface, thereby suppressing the formation of lithium dendrites at the anode interface, enabling electrochemical devices. The safety performance has been further improved.
如上所述的负极极片中,所述M个导电层和N个介电层交错层叠设置。In the above negative pole piece, the M conductive layers and the N dielectric layers are alternately stacked.
相比M个导电层与N个介电层的其他层叠方式,导电层和介电层交错层叠设置的方式,使得功能层中产生的锂枝晶更容易接触到导电层,从而实现导电层对锂枝晶进行“自纠错”,遏制功能层中锂枝晶的进一步生长,因此能够改善包括该负极极片的电化学装置的循环寿命和安全性能。Compared with other stacking methods of M conductive layers and N dielectric layers, the alternate stacking of conductive layers and dielectric layers makes it easier for the lithium dendrites generated in the functional layer to contact the conductive layer, thereby realizing the conductive layer pair. The "self-correction" of lithium dendrites prevents further growth of lithium dendrites in the functional layer, thus improving the cycle life and safety performance of electrochemical devices including the negative electrode.
如上所述的负极极片中,所述功能层的第一边缘层和/或第二边缘层为介电层。In the above negative pole piece, the first edge layer and/or the second edge layer of the functional layer is a dielectric layer.
锂润湿材料分布在导电层内,因此,功能层的第一边缘层和/或第二边缘层为介电层时,锂离子更倾向于沉积在功能层内部,从而降低负极界面锂离子的沉积,抑制负极界面锂枝晶的形成,因此,能够有效提高包括该负极极片的电化学装置的循环寿命和安全性能。The lithium wetting material is distributed in the conductive layer. Therefore, when the first edge layer and/or the second edge layer of the functional layer is a dielectric layer, lithium ions are more likely to be deposited inside the functional layer, thereby reducing the negative electrode interface. The deposition can inhibit the formation of lithium dendrites at the negative electrode interface, and therefore, the cycle life and safety performance of the electrochemical device including the negative electrode pole piece can be effectively improved.
如上所述的负极极片中,所述导电层的电导率为10 -7S/cm至10 6S/cm,和/或, In the above negative pole piece, the electrical conductivity of the conductive layer is 10 -7 S/cm to 10 6 S/cm, and/or,
所述介电层的电导率小于10 -8S/cm。 The electrical conductivity of the dielectric layer is less than 10 -8 S/cm.
导电层和/或介电层的电导率在上述范围时,功能层中电流密度更有利于锂离子在功能层内部的沉积,抑制锂枝晶的形成,因此,包括该负极极片的电化学装置具有优良的循环寿命和安全性能。When the conductivity of the conductive layer and/or the dielectric layer is in the above range, the current density in the functional layer is more conducive to the deposition of lithium ions inside the functional layer, and the formation of lithium dendrites is suppressed. The device has excellent cycle life and safety performance.
如上所述的负极极片中,所述功能层的孔隙率为5%至90%,可选为50%至90%。In the above negative pole piece, the porosity of the functional layer is 5% to 90%, optionally 50% to 90%.
功能层的孔隙率在50%至90%时,在不影响电化学装置体积能量密度的前提下,功能层能够诱导锂离子进入其内部并且为锂离子提供沉积位点,从而抑制界面锂枝晶的形成,改善电化学装置的循环寿命和安全性能。When the porosity of the functional layer is between 50% and 90%, without affecting the volumetric energy density of the electrochemical device, the functional layer can induce lithium ions to enter its interior and provide deposition sites for lithium ions, thereby suppressing interfacial lithium dendrites. The formation of electrochemical devices improves the cycle life and safety performance of electrochemical devices.
如上所述的负极极片中,所述锂润湿材料的质量为所述功能层质量的5%至95%,可选为30%至60%。In the above negative pole piece, the mass of the lithium wetting material is 5% to 95% of the mass of the functional layer, optionally 30% to 60%.
锂润湿材料的含量过低,诱导锂离子进入内部沉积的能力低,功能成对电化学装置循环寿命和安全性能的改善能力有限,锂润湿材料的含量过大,对功能层的结构稳定性以及电化学装置的能量密度有消极影响;锂润湿材料的含量在30%至60%时,能够在不影响电化学装置能量密度和功能层结构稳定性的前提下,诱导锂离子进入功能层内部沉积,从而降低锂离子在负极界面的停留几率,减少界面锂枝晶的形成,提升电化学装的循环寿命和安全性能。The content of lithium wetting material is too low, the ability to induce lithium ions to enter the internal deposition is low, and the functional pairing has limited ability to improve the cycle life and safety performance of electrochemical devices, and the content of lithium wetting material is too large. It has a negative effect on the energy density of the electrochemical device and the energy density of the electrochemical device; when the content of the lithium wetting material is 30% to 60%, it can induce lithium ions into the functional layer without affecting the energy density of the electrochemical device and the structural stability of the functional layer. The inner layer is deposited, thereby reducing the probability of lithium ions staying at the negative electrode interface, reducing the formation of lithium dendrites at the interface, and improving the cycle life and safety performance of the electrochemical device.
如上所述的负极极片中,所述功能层还包括锂金属,所述锂金属在所述功能层中的含量为 0.25mg/cm 2至25mg/cm 2In the above-mentioned negative pole piece, the functional layer further includes lithium metal, and the content of the lithium metal in the functional layer is 0.25 mg/cm 2 to 25 mg/cm 2 .
功能层中的锂金属能够在循环过程中不断为负极极片补充锂,抵消充放电过程中不可逆的锂损失,从而进一步提高包括该负极极片的电化学装置的循环寿命。The lithium metal in the functional layer can continuously replenish lithium for the negative electrode plate during the cycle, offset the irreversible lithium loss during the charging and discharging process, thereby further improving the cycle life of the electrochemical device including the negative electrode plate.
本申请还提供一种电化学装置,所述电化学装置包括上述的负极极片。The present application also provides an electrochemical device, the electrochemical device comprising the above-mentioned negative electrode plate.
本申请的电化学装置,包括上述的负极极片,因此该电化学装置更优异的循环寿命和安全性能。The electrochemical device of the present application includes the above-mentioned negative electrode plate, so the electrochemical device has more excellent cycle life and safety performance.
本申请还提供一种电子装置,所述电子装置的驱动源或能量存储单元为上述的电化学装置。The present application also provides an electronic device, wherein the driving source or energy storage unit of the electronic device is the above-mentioned electrochemical device.
本申请的电子装置的驱动源或能量存储单元采用上述的电化学装置,因此续航能力、循环寿命、安全性能表现优异,用户体验感极佳。The driving source or energy storage unit of the electronic device of the present application adopts the above-mentioned electrochemical device, so the battery life, cycle life and safety performance are excellent, and the user experience is excellent.
附图说明Description of drawings
图1为本申请一实施例中功能层的示意图;1 is a schematic diagram of functional layers in an embodiment of the application;
图2为本申请另一实施例中功能层的示意图;2 is a schematic diagram of a functional layer in another embodiment of the present application;
图3为本申请一实施例中负极极片的结构示意图;3 is a schematic structural diagram of a negative pole piece in an embodiment of the application;
图4为本申请另一实施例中负极极片的结构示意图;4 is a schematic structural diagram of a negative pole piece in another embodiment of the present application;
图5为本申请又一实施例中负极极片的结构示意图;5 is a schematic structural diagram of a negative pole piece in yet another embodiment of the application;
图6为本申请实施例8中负极极片的扫描电镜图;6 is a scanning electron microscope image of a negative pole piece in Example 8 of the application;
图7为本申请实施例11中负极极片锂沉积的扫描电镜图;7 is a scanning electron microscope image of the lithium deposition of the negative electrode pole piece in Example 11 of the application;
图8为本申请对比例1中负极极片锂沉积的扫描电镜图。FIG. 8 is a scanning electron microscope image of the lithium deposition of the negative pole piece in Comparative Example 1 of the present application.
具体实施方式Detailed ways
为使本申请的目的、技术方案和优点更加清楚,下面将结合本申请的实施例,对本申请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申请一部分实施例,而不是全部的实施例。基于本申请中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本申请保护的范围。In order to make the purpose, technical solutions and advantages of the present application clearer, the technical solutions in the embodiments of the present application will be clearly and completely described below in conjunction with the embodiments of the present application. Obviously, the described embodiments are part of the implementation of the present application. examples, but not all examples. Based on the embodiments in the present application, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present application.
本申请的第一方面提供一种负极极片,负极极片包括功能层;功能层包括层叠设置的M个导电层和N个介电层,导电层中包括锂润湿材料;A first aspect of the present application provides a negative pole piece, the negative pole piece includes a functional layer; the functional layer includes M conductive layers and N dielectric layers arranged in layers, and the conductive layer includes a lithium wetting material;
其中,M≥1,N≥1。Among them, M≥1, N≥1.
图1为本申请一实施例中功能层的示意图,如图1所示,在本实施例中,功能层包括层叠设置的导电层a和介电层b,导电层a中包括锂润湿材料c;图1中,M=1,N=1。FIG. 1 is a schematic diagram of a functional layer in an embodiment of the application. As shown in FIG. 1 , in this embodiment, the functional layer includes a stacked conductive layer a and a dielectric layer b, and the conductive layer a includes a lithium wetting material c; In Figure 1, M=1, N=1.
图2为本申请另一实施例中功能层的示意图,如图2所示,在本实施例中,功能层包括层叠设置的导电层a1、导电层a2和介电层b,导电层a1和导电层a2中包括锂润湿材料c;图2中,M=2,N=1。FIG. 2 is a schematic diagram of a functional layer in another embodiment of the present application. As shown in FIG. 2 , in this embodiment, the functional layer includes a conductive layer a1, a conductive layer a2 and a dielectric layer b that are stacked in layers. The conductive layer a1 and The conductive layer a2 includes a lithium wetting material c; in FIG. 2 , M=2, N=1.
一般地,在充电过程中,电子流向负极极片,在负极极片中与Li +相遇,Li +得到电子,从而在负极极片中沉积得到锂金属,放电过程中则相反。因此,在不断地充放电过程中,锂在负极极片中不断发生沉积和溶解,锂的体积也随之增大和减小,从而使得负极极片的体积发生膨胀和收缩。此外,在锂沉积过程中,锂金属容易在负极极片上形成锂枝晶,从 而产生刺穿隔膜,引发短路的风险。 Generally, during the charging process, electrons flow to the negative pole piece, meet with Li + in the negative pole piece, Li + gets electrons, thereby depositing lithium metal in the negative pole piece, and the opposite is true during discharge. Therefore, during the continuous charging and discharging process, lithium is continuously deposited and dissolved in the negative pole piece, and the volume of lithium also increases and decreases, so that the volume of the negative pole piece expands and contracts. In addition, during the lithium deposition process, lithium metal tends to form lithium dendrites on the negative pole piece, which creates the risk of piercing the separator and causing a short circuit.
本申请负极极片的功能层包括介电层和附着有锂润湿材料的导电层,其中,介电层能够降低功能层表面的电子浓度,防止锂离子在较大电子浓度下形成枝晶;而且介电层能够阻止电子传输至功能层表面,迫使锂离子进入功能层内部进行沉积,从而降低负极界面锂离子沉积量,抑制负极界面锂枝晶的形成;并且,在锂润湿材料的诱导下,锂离子在向负极迁移时能够快速进入功能层内部,进一步降低了锂离子在负极界面停留的几率,从而通过进一步抑制界面锂枝晶的生长而维护了负极界面的完整性,不仅避免了界面锂枝晶生长刺破隔膜引起的安全隐患,更是有效杜绝了由于锂枝晶的生长,甚至“死锂”的形成引起的电化学装置循环性能的劣化。The functional layer of the negative electrode piece of the present application includes a dielectric layer and a conductive layer attached with a lithium wetting material, wherein the dielectric layer can reduce the electron concentration on the surface of the functional layer and prevent lithium ions from forming dendrites at a large electron concentration; Moreover, the dielectric layer can prevent electrons from being transported to the surface of the functional layer, forcing lithium ions into the functional layer for deposition, thereby reducing the amount of lithium ion deposition at the negative electrode interface and inhibiting the formation of lithium dendrites at the negative electrode interface; and, in the induction of lithium wetting materials In this way, lithium ions can quickly enter the functional layer when migrating to the negative electrode, which further reduces the probability of lithium ions staying at the negative electrode interface, thereby maintaining the integrity of the negative electrode interface by further inhibiting the growth of interfacial lithium dendrites, not only avoiding the The potential safety hazard caused by the growth of interfacial lithium dendrites piercing the separator can effectively prevent the deterioration of the cycle performance of electrochemical devices caused by the growth of lithium dendrites and even the formation of "dead lithium".
此外,本申请负极极片功能层的结构相当于导电层和介电层层叠而成的骨架,因此功能层内部具有一定的空间。当锂离子进入功能层的内部后,即使锂离子被还原生长为锂枝晶,功能层的骨架结构也能够为锂枝晶提供一定的生长空间,在一定程度上降低了锂枝晶的体积对负极极片的挤压和膨胀损毁,维护了电化学装置的循环性能和安全性能。值得一提的是,导电层还具有一定的“自纠错功能”。具体地,即使锂枝晶在功能层内部快速生长,当其生长接触到导电层,由于导电层本身的等电位性,可以使得锂枝晶顶部集中的电场分布得到分散趋于均匀化,从而遏制枝晶的进一步生长,实现枝晶“自纠错”,通过进一步抑制负极极片的体积膨胀而实现了电化学装置循环性能和安全性能的有效改善。In addition, the structure of the functional layer of the negative electrode pole piece of the present application corresponds to a skeleton formed by stacking a conductive layer and a dielectric layer, so the functional layer has a certain space inside. When lithium ions enter the interior of the functional layer, even if the lithium ions are reduced to grow into lithium dendrites, the skeleton structure of the functional layer can provide a certain growth space for lithium dendrites, which reduces the volume of lithium dendrites to a certain extent. The extrusion and expansion damage of the negative pole piece maintains the cycle performance and safety performance of the electrochemical device. It is worth mentioning that the conductive layer also has a certain "self-correcting function". Specifically, even if lithium dendrites grow rapidly inside the functional layer, when the growth contacts the conductive layer, due to the equipotentiality of the conductive layer itself, the electric field distribution concentrated on the top of the lithium dendrites can be dispersed and tend to be uniform, thereby preventing The further growth of dendrites realizes the "self-correction" of dendrites, and effectively improves the cycle performance and safety performance of electrochemical devices by further suppressing the volume expansion of the negative electrode.
因此,本申请的负极极片通过包括锂润湿材料的导电层和介电层形成的功能层,不仅降低了功能层中锂枝晶的形成,还抑制了界面锂枝晶的生长,更是有效改善了负极极片在长期应用过程中发生的体积膨胀,因此有利于电化学装置循环性能和安全性能的优化。Therefore, in the negative electrode plate of the present application, the functional layer formed by the conductive layer and the dielectric layer including the lithium-wetting material not only reduces the formation of lithium dendrites in the functional layer, but also inhibits the growth of lithium dendrites at the interface, which is more The volume expansion of the negative electrode plate during long-term application is effectively improved, so it is beneficial to the optimization of the cycle performance and safety performance of the electrochemical device.
此外,由于本申请的负极极片能够有效避免锂枝晶的形成,降低锂在循环过程中的损耗,因此电化学装置还能够具有良好的库伦效率。In addition, since the negative electrode sheet of the present application can effectively avoid the formation of lithium dendrites and reduce the loss of lithium during cycling, the electrochemical device can also have good Coulomb efficiency.
本申请对导电层的材质不作严格限制,只要能够实现对电子的有效传导即可。在具体实施过程中,导电层可以为导体材料,例如铜、镍、铬、钛、钨、锆、铝及其合金等金属材料;导电层的材质也可以为半导体材料,例如实心碳球、中空碳球、多孔碳、单层碳纳米管、多层碳纳米管、纯碳纤维、掺杂碳纤维(包括氧化物、硫化物、碳化物、氮化物、金属单质、官能团等掺杂的碳纤维)、石墨烯笼、掺杂石墨烯及掺杂石墨烯衍生物等碳基材料。本申请可以选择,但并不限定于上述材料。The present application does not impose strict restrictions on the material of the conductive layer, as long as it can effectively conduct electrons. In the specific implementation process, the conductive layer can be a conductor material, such as copper, nickel, chromium, titanium, tungsten, zirconium, aluminum and its alloys and other metal materials; the material of the conductive layer can also be a semiconductor material, such as solid carbon spheres, hollow Carbon spheres, porous carbon, single-walled carbon nanotubes, multi-layered carbon nanotubes, pure carbon fibers, doped carbon fibers (including carbon fibers doped with oxides, sulfides, carbides, nitrides, metal elements, functional groups, etc.), graphite Carbon-based materials such as graphene cages, doped graphene and doped graphene derivatives. This application can choose, but is not limited to the above-mentioned materials.
本申请对介电层的材质不作严格限制,只要能够阻断电子传导即可。在具体实施过程中,介电层可以采用高分子材料,例如,聚偏二氟乙烯、聚酰亚胺、聚酰胺、聚丙烯腈、聚乙二醇、聚苯醚、聚碳酸亚丙酯、聚甲基丙烯酸甲酯、聚对苯二甲酸乙二醇酯、聚环氧乙烷、聚偏二氟乙烯-六氟丙烯、聚偏二氟乙烯-三氟氯乙烯、聚偏氟乙烯-六氟丙烯、聚偏氟乙烯中的至少一种;介电层也可以是无机材料,例如硅酸钠及其衍生物、氧化铝及其衍生物、氧化硅及其衍生物中的至少一种。本申请可以选择,但并不限定于上述材料。The application does not impose strict restrictions on the material of the dielectric layer, as long as it can block electron conduction. In the specific implementation process, the dielectric layer can be made of polymer materials, such as polyvinylidene fluoride, polyimide, polyamide, polyacrylonitrile, polyethylene glycol, polyphenylene ether, polypropylene carbonate, Polymethyl methacrylate, polyethylene terephthalate, polyethylene oxide, polyvinylidene fluoride-hexafluoropropylene, polyvinylidene fluoride-chlorotrifluoroethylene, polyvinylidene fluoride-hexafluoropropylene At least one of fluoropropylene and polyvinylidene fluoride; the dielectric layer can also be an inorganic material, such as at least one of sodium silicate and its derivatives, aluminum oxide and its derivatives, silicon oxide and its derivatives. This application can choose, but is not limited to the above-mentioned materials.
本申请对锂润湿材料不作严格限制,只要能够与锂具有良好的亲和性即可。锂润湿材料可以为金属单质,例如,银、铝、金、钡、钙、铟、铂、硅、锡、锌、钴、稼;锂润湿材料也可以是氮化物如氮化钼,硫化物如硫化钼,硫化锡。此外,本申请还可以通过对导电层进行改性,使得导电层中包括羟基(-OH)、酯基(-COOR)、羧基(-COOH)、氨基(-NH 2)、磺基(-SO 3H)等亲锂的官能团来使得导电层中包括锂润湿材料。 This application does not impose strict restrictions on the lithium wetting material, as long as it can have good affinity with lithium. The lithium wetting material can be a metal element, for example, silver, aluminum, gold, barium, calcium, indium, platinum, silicon, tin, zinc, cobalt, gallium; the lithium wetting material can also be a nitride such as molybdenum nitride, sulfide Such as molybdenum sulfide, tin sulfide. In addition, the present application can also modify the conductive layer so that the conductive layer includes hydroxyl (-OH), ester (-COOR), carboxyl (-COOH), amino (-NH 2 ), sulfo (-SO) 3 H) and other lithiophilic functional groups to make the conductive layer include lithium wetting materials.
本申请对获得导电层的方式不作严格限制,作为一种可选的实施方式,本申请可以采用静 电纺丝与热处理相结合的方式获得到导电层。详细而言,使用能够生成导电物质的前驱体与溶剂配制成纺丝液,通过静电纺丝装置进行静电纺丝得到纤维膜,而后对纤维膜在惰性气氛中进行热处理,可以获得导电层。The present application does not strictly limit the manner of obtaining the conductive layer. As an optional embodiment, the present application can obtain the conductive layer by a combination of electrospinning and heat treatment. Specifically, a spinning solution is prepared by using a precursor capable of generating conductive substances and a solvent, electrospinning is performed by an electrospinning device to obtain a fiber film, and then the fiber film is heat-treated in an inert atmosphere to obtain a conductive layer.
作为另一种可行的实施方式,还可以配制包含导电物质以及粘接剂的导电浆料,然后选择一合适基板,将导电浆料涂布在基板上,获得导电层。As another feasible embodiment, it is also possible to formulate a conductive paste containing a conductive substance and an adhesive, and then select a suitable substrate, and coat the conductive paste on the substrate to obtain a conductive layer.
本申请对获得介电层的方式不作严格限制,介电层也可采用静电纺丝或者涂布的方式获得,本申请在此不再赘述。This application does not strictly limit the method of obtaining the dielectric layer, and the dielectric layer can also be obtained by means of electrospinning or coating, which will not be repeated in this application.
本申请对在导电层中包括锂润湿材料的方式不作严格限制,作为一种可实施的方式,本申请可以采用在上述静电纺丝和热处理相结合制备导电层的过程中,在纺丝液中加入锂润湿材料的前驱体进行静电纺丝,得到包括锂润湿材料前驱体的纤维膜,而后对纤维膜进行热处理时,锂润湿材料前驱体转化为锂润湿材料,从而使得导电层中包括锂润湿材料。作为另一种可实施的方式,可以在涂布制备导电层的过程中,在导电浆料中加入一定量的锂润湿材料,从而使得获得的导电层中包括锂润湿材料。The present application does not impose strict restrictions on the manner of including the lithium wetting material in the conductive layer. As an implementable manner, the present application may adopt the method of preparing the conductive layer by combining the above-mentioned electrospinning and heat treatment. Electrospinning is carried out by adding a precursor of a lithium-wetting material to electrospinning to obtain a fiber membrane including a lithium-wetting material precursor, and then when the fiber membrane is heat-treated, the lithium-wetting material precursor is converted into a lithium-wetting material, thereby making conductive The layer includes a lithium wetting material. As another implementable manner, a certain amount of lithium wetting material may be added to the conductive paste during the process of coating and preparing the conductive layer, so that the obtained conductive layer includes the lithium wetting material.
本申请对层叠导电层和介电层以获得功能层的方式不作严格限制,作为一种可选的实施方式,本申请可以通过热压的方式使得M个导电层与N个介电层层叠设置获得功能层。作为另一种可选的方式,本申请还可以通过涂布的方式获得导电层与介电层层叠设置的功能层,具体为,选择一合适基板,将形成M个导电层和N个介电层的浆料在基板表面依次层叠涂布。The present application does not strictly limit the method of stacking conductive layers and dielectric layers to obtain functional layers. As an optional embodiment, the present application can stack M conductive layers and N dielectric layers by means of hot pressing. Get functional layers. As another optional method, the present application can also obtain a functional layer in which a conductive layer and a dielectric layer are stacked by coating. Specifically, a suitable substrate is selected to form M conductive layers and N dielectric layers. The layered pastes are sequentially layered and applied on the surface of the substrate.
在前述负极极片结构的基础上,本申请还进一步对导电层中的锂润湿材料的含量分布进行了限定,从而有利于进一步提升电化学装置的安全性能和循环寿命。在本申请的一些实施方式中,负极极片中锂润湿材料的含量在层叠方向上梯度分布。On the basis of the aforementioned negative pole piece structure, the present application further limits the content distribution of the lithium wetting material in the conductive layer, which is beneficial to further improve the safety performance and cycle life of the electrochemical device. In some embodiments of the present application, the content of the lithium wetting material in the negative pole piece is distributed in a gradient in the stacking direction.
本申请中,锂润湿材料的含量在层叠方向上梯度分布包括梯度递增和梯度递减,其中,梯度递增是指第j个导电层中的锂润湿材料的含量小于第(j+1)个导电层中的锂润湿材料的含量,梯度递减是指第j个导电层中的锂润湿材料的含量大于第(j+1)个导电层中的锂润湿材料的含量,1≤j<M。本申请通过对锂润湿材料的含量分布进行控制,能够对锂离子在功能层内沉积的部位进行控制。能够理解,锂离子倾向于在锂润湿材料含量较大的部位沉积,因此,在具体实施的过程中,控制远离负极界面的导电层中的锂润湿材料含量大于靠近负极界面的导电层中的锂润湿材料含量,从而减少锂离子在靠近负极界面处的沉积,抑制负极界面锂枝晶的形成,维护负极界面的完整性,避免界面锂枝晶的形成刺破隔膜引起短路,因此能够进一步提升了电化学装置的安全性能。In this application, the gradient distribution of the content of the lithium wetting material in the stacking direction includes an increasing gradient and a decreasing gradient, wherein the increasing gradient means that the content of the lithium wetting material in the jth conductive layer is less than the (j+1)th The content of the lithium wetting material in the conductive layer, the gradient decreasing means that the content of the lithium wetting material in the jth conductive layer is greater than the content of the lithium wetting material in the (j+1)th conductive layer, 1≤j <M. In the present application, by controlling the content distribution of the lithium wetting material, the location where lithium ions are deposited in the functional layer can be controlled. It can be understood that lithium ions tend to be deposited in parts with a large content of lithium wetting material. Therefore, in the specific implementation process, the content of lithium wetting material in the conductive layer far from the negative electrode interface is controlled to be greater than that in the conductive layer close to the negative electrode interface. The content of lithium wetting material can reduce the deposition of lithium ions near the negative electrode interface, inhibit the formation of lithium dendrites at the negative electrode interface, maintain the integrity of the negative electrode interface, and avoid the formation of interfacial lithium dendrites piercing the diaphragm and causing short circuit. The safety performance of the electrochemical device is further improved.
在例如图1所示的功能层中,M=1,则锂润湿材料的含量在这一个导电层a内部沿层叠方向梯度分布。作为一种可以采用的方式,在上述静电纺丝与热处理相结合获得导电层a的过程中,纺丝时,在不同时间段向静电纺丝装置中加入锂润湿材料前驱体浓度呈梯度变化的纺丝液,可以使得在沿导电层a的厚度方向锂润湿材料的含量梯度分布,而后将导电层a与介电层b沿导电层a的厚度方向进行层叠获得功能层,从而导电层a内锂润湿材料的含量在层叠方向上梯度分布。For example, in the functional layer shown in FIG. 1 , where M=1, the content of the lithium wetting material is distributed in a gradient along the stacking direction inside the conductive layer a. As a possible way, in the process of obtaining the conductive layer a by combining the above-mentioned electrospinning and heat treatment, during spinning, the concentration of the precursor of the lithium wetting material added to the electrospinning device at different time periods changes in a gradient. The spinning solution can make the content of the lithium-wetting material gradient distributed along the thickness direction of the conductive layer a, and then stack the conductive layer a and the dielectric layer b along the thickness direction of the conductive layer a to obtain a functional layer, so that the conductive layer The content of Li-wetting material in a is distributed gradiently in the stacking direction.
当功能层中包括两个及以上导电层(M≥2)时,各个导电层的锂润湿材料的含量在层叠方向上梯度分布,并且每一个导电层中的锂润湿材料的含量均匀分布。When the functional layer includes two or more conductive layers (M≥2), the content of the lithium-wetting material in each conductive layer is distributed in a gradient in the stacking direction, and the content of the lithium-wetting material in each conductive layer is uniformly distributed .
例如在图2所示的功能层中,M=2,锂润湿材料的含量在导电层a1内均匀分布,锂润湿材料的含量导电层a2内均匀分布,且导电层a1内锂润湿材料的含量大于导电层a2内锂润湿 材料的含量,从而在负极极片中,锂润湿材料的含量在层叠方向上梯度分布。For example, in the functional layer shown in FIG. 2, M=2, the content of the lithium wetting material is uniformly distributed in the conductive layer a1, the content of the lithium wetting material is uniformly distributed in the conductive layer a2, and the lithium wetting material in the conductive layer a1 is uniformly distributed The content of the material is greater than the content of the lithium wetting material in the conductive layer a2, so that in the negative pole piece, the content of the lithium wetting material is distributed in a gradient in the stacking direction.
在功能层中包括两个及以上导电层时,在静电纺丝与热处理结合制备M个导电层的过程中,使得M个纺丝液中锂润湿材料前驱体的含量梯度变化,而后在层叠时,导电层按照纺丝液中锂润湿材料前驱体的含量递增或递减的顺序与介电层层叠。作为另一种可实施的方式,在涂布获得导电层的过程中,可以使得层叠方向上M个导电浆料中锂润湿材料的含量梯度变化,从而使得锂润湿材料的含量在层叠方向上梯度分布。When two or more conductive layers are included in the functional layer, in the process of preparing M conductive layers by combining electrospinning and heat treatment, the content of the lithium wetting material precursor in the M spinning solutions is changed in a gradient, and then in the lamination process During the process, the conductive layer is laminated with the dielectric layer in the order of increasing or decreasing content of the precursor of the lithium-wetting material in the spinning solution. As another implementable manner, in the process of coating to obtain the conductive layer, the content of the lithium-wetting material in the M conductive pastes in the stacking direction can be changed in a gradient, so that the content of the lithium-wetting material in the stacking direction is changed. upper gradient distribution.
当然,在功能层包括两个及以上导电层时,一个导电层内锂润湿材料的含量在沿层叠方向上也可以梯度分布,并且,考虑到对锂离子的诱导沉积,一个导电层内锂润湿材料的含量在层叠方向上梯度分布的趋势与不同导电层中锂润湿材料的含量在层叠方向上梯度分布的趋势相同,例如,同时梯度递增或同时梯度递减。Of course, when the functional layer includes two or more conductive layers, the content of the lithium-wetting material in one conductive layer can also be distributed in a gradient along the stacking direction, and, considering the induced deposition of lithium ions, the lithium-wetting material in one conductive layer The gradient distribution of the content of the wetting material in the stacking direction is the same as the gradient distribution of the content of the lithium wetting material in the different conductive layers in the stacking direction, for example, the gradient is increasing simultaneously or the gradient is decreasing simultaneously.
在本申请的一些实施方式中,锂润湿材料的质量可以为功能层质量的5%至95%,可选地,为30%至60%。In some embodiments of the present application, the mass of the lithium-wetting material may be 5% to 95% of the mass of the functional layer, alternatively, 30% to 60%.
一般地,功能层中锂润湿材料的质量越多,功能层亲锂性越好,从而更有利于诱导锂离子快速进入功能层内进行沉积。但是,一味提高锂润湿材料的质量不利于电化学装置质量能量密度的提高以及功能层的结构稳定性,因此可以将锂润湿材料的质量控制在功能层质量的30%至60%的范围,从而在不影响电化学装置质量能量密度的前提下,降低锂离子在负极界面的几率,抑制负极界面锂枝晶的形成,改善电化学装置的循环寿命和安全性能。此外,在锂润湿材料的选择方面,也可以通过选择一些亲锂效果好且密度较低的材料以进一步实现电化学装置的循环寿命、安全性能和质量能量密度的统一。Generally, the higher the quality of the lithium-wetting material in the functional layer, the better the lithophilicity of the functional layer, which is more conducive to inducing lithium ions to rapidly enter the functional layer for deposition. However, blindly improving the quality of the lithium-wetting material is not conducive to the improvement of the mass energy density of the electrochemical device and the structural stability of the functional layer. Therefore, the quality of the lithium-wetting material can be controlled in the range of 30% to 60% of the quality of the functional layer. Therefore, without affecting the mass energy density of the electrochemical device, the probability of lithium ions at the negative electrode interface is reduced, the formation of lithium dendrites at the negative electrode interface is suppressed, and the cycle life and safety performance of the electrochemical device are improved. In addition, in the selection of lithium-wetting materials, some materials with good lithiophilic effect and low density can also be selected to further realize the unity of cycle life, safety performance and mass energy density of electrochemical devices.
本申请的负极极片中还包括锂金属层或集流体。一般来说,锂金属层或集流体为薄片状,锂金属层或集流体中两个较大且相对的面即为功能表面。当本申请的负极极片包括锂金属层或集流体时,功能层设置在功能表面上。The negative electrode sheet of the present application also includes a lithium metal layer or a current collector. Generally speaking, the lithium metal layer or current collector is in the form of flakes, and the two larger and opposite faces of the lithium metal layer or current collector are the functional surfaces. When the negative electrode sheet of the present application includes a lithium metal layer or a current collector, the functional layer is provided on the functional surface.
本申请对功能层在功能表面的设置方式不作严格限制,例如,可以通过热压使得功能层设置在功能表面;也可以如前述,在通过涂布的方式获得功能层时,使用锂金属层或集流体作为基板。在一些实施方式中,功能层也可以直接放置在锂金属层或集流体的功能表面上,功能层与功能表面不形成实质性连接。可以理解,通过热压或涂布的方式能够在功能层与功能表面之间形成实质性连接,有利于进一步保持负极极片在充放电过程中的结构稳定性和导电网络的稳固。This application does not strictly limit the arrangement of the functional layer on the functional surface. For example, the functional layer can be arranged on the functional surface by hot pressing; or as mentioned above, when the functional layer is obtained by coating, a lithium metal layer or a lithium metal layer can be used. The current collector acts as a substrate. In some embodiments, the functional layer can also be placed directly on the functional surface of the lithium metal layer or current collector without forming a substantial connection between the functional layer and the functional surface. It can be understood that a substantial connection can be formed between the functional layer and the functional surface by means of hot pressing or coating, which is beneficial to further maintain the structural stability of the negative pole piece and the stability of the conductive network during the charging and discharging process.
在具体的实施过程中,可以根据负极极片的用途而对负极极片是否包括锂金属层或集流体进行选择。例如,当本申请的负极极片用于扣式电池时,可以选择不使用锂金属层或集流体,以功能层直接作为电池的负极,从而能够使得扣式电池的质量更轻,扣式电池的质量能量密度进一步提高。当本申请的负极极片用于卷绕型电池时,负极极片包括锂金属层或集流体以便于设置极耳。本申请中,集流体可以采用但不限于铜箔。In a specific implementation process, whether the negative electrode plate includes a lithium metal layer or a current collector can be selected according to the purpose of the negative electrode plate. For example, when the negative pole piece of the present application is used in a button battery, it is possible to choose not to use a lithium metal layer or a current collector, and use the functional layer directly as the negative electrode of the battery, so that the button battery can be lighter in weight. The mass energy density is further improved. When the negative pole piece of the present application is used in a wound type battery, the negative pole piece includes a lithium metal layer or a current collector to facilitate the arrangement of the tabs. In this application, the current collector can be made of but not limited to copper foil.
为了进一步提高功能层对锂离子沉积的诱导效果和电子传输的阻断效果,作为一种优选的实施方式,当负极极片包括锂金属层或集流体时,功能层设置在锂金属层的功能表面或集流体的功能表面且锂金属层的延伸方向或集流体的延伸方向与层叠方向垂直;In order to further improve the inductive effect of the functional layer on lithium ion deposition and the blocking effect of electron transport, as a preferred embodiment, when the negative pole piece includes a lithium metal layer or a current collector, the functional layer is arranged on the lithium metal layer. The surface or the functional surface of the current collector and the extension direction of the lithium metal layer or the extension direction of the current collector is perpendicular to the stacking direction;
锂润湿材料的含量在远离所述锂金属层或集流体的方向上梯度递减。The content of the lithium wetting material is gradually decreasing in the direction away from the lithium metal layer or current collector.
图3为本申请一实施例中负极极片的结构示意图,如图3所示,该负极极片包括锂金属层或集流体d、功能层e,功能层e设置在锂金属层或集流体d的一功能表面。其中,功能层e 包括导电层a、介电层b和锂润湿材料c、M=1、N=1,层叠方向与锂金属层的延伸方向或集流体的延伸方向与层叠方向垂直,图中箭头方向为层叠方向,锂润湿材料的含量在远离锂金属层或集流体d的方向上梯度递减。FIG. 3 is a schematic structural diagram of a negative pole piece in an embodiment of the application. As shown in FIG. 3 , the negative pole piece includes a lithium metal layer or current collector d and a functional layer e, and the functional layer e is disposed on the lithium metal layer or current collector A functional surface of d. Among them, the functional layer e includes a conductive layer a, a dielectric layer b and a lithium wetting material c, M=1, N=1, and the stacking direction is perpendicular to the extension direction of the lithium metal layer or the extension direction of the current collector and the stacking direction. The direction of the middle arrow is the stacking direction, and the content of the lithium-wetting material gradually decreases in the direction away from the lithium metal layer or the current collector d.
本申请的负极极片按照上述方式实施时,介电层的延伸方向与锂金属层或集流体的延伸方向平行,介电层阻断电子传递的面积大,因此,介电层能够更有效降低功能层内的电子浓度从而有效阻止锂离子与电子结合,抑制功能层内锂枝晶的形成;并且介电层能够更有效降低功能层表面的电子浓度,迫使锂离子进入功能层内部进行沉积,降低负极界面锂枝晶的形成;因此能够改善电化学装置的循环寿命和安全性能。此外,锂润湿材料的含量在远离锂金属层或集流体的区域低,在靠近锂金属层或集流体的区域高,因此,锂离子更倾向于沉积在靠近锂金属层或集流体的区域,从而降低靠近负极界面区域锂枝晶的形成,防止锂枝晶刺破隔膜引起安全风险,进而提高电化学装置的安全性能。When the negative electrode sheet of the present application is implemented in the above manner, the extending direction of the dielectric layer is parallel to the extending direction of the lithium metal layer or the current collector, and the area of the dielectric layer for blocking electron transfer is large, so the dielectric layer can more effectively reduce the The electron concentration in the functional layer can effectively prevent the combination of lithium ions and electrons, and inhibit the formation of lithium dendrites in the functional layer; and the dielectric layer can more effectively reduce the electron concentration on the surface of the functional layer, forcing lithium ions into the functional layer for deposition. The formation of lithium dendrites at the anode interface is reduced; thus, the cycle life and safety performance of electrochemical devices can be improved. In addition, the content of Li-wetting material is low in the region away from the Li metal layer or current collector and high in the region close to the Li metal layer or current collector, therefore, lithium ions are more inclined to deposit in the region close to the Li metal layer or current collector , thereby reducing the formation of lithium dendrites near the negative electrode interface area, preventing lithium dendrites from piercing the separator and causing safety risks, thereby improving the safety performance of the electrochemical device.
发明人在研究过程中发现,功能层在沿层叠方向上的厚度对电化学装置的电性能会有一定的影响,功能层在沿层叠方向上的厚度过大,电化学装置的能量密度会下降,而厚度过小,功能层对电化学装置循环寿命和安全性能的改善有限。当功能层的厚度在50μm至100μm之间时,电化学装置不仅能够具有较好的能量密度,而且循环寿命和安全性能优良。During the research process, the inventor found that the thickness of the functional layer along the stacking direction will have a certain influence on the electrical properties of the electrochemical device. If the thickness of the functional layer along the stacking direction is too large, the energy density of the electrochemical device will decrease. , while the thickness is too small, the improvement of the functional layer on the cycle life and safety performance of the electrochemical device is limited. When the thickness of the functional layer is between 50 μm and 100 μm, the electrochemical device can not only have good energy density, but also have excellent cycle life and safety performance.
此外,在功能层厚度一定的情况下,合理控制导电层和介电层的层数,有利于进一步改善电化学装置的循环寿命和安全性能。具体地,随着导电层和介电层的层数在一定范围内增加,电化学装置的循环寿命和安全性能都先呈现递增趋势,后基本保持不变,因此出于经济性的考虑,一般导电层的层数M=4至6,和/或,介电层的层数N=4至6。In addition, under the condition of a certain thickness of the functional layer, rational control of the number of conductive layers and dielectric layers is beneficial to further improve the cycle life and safety performance of electrochemical devices. Specifically, as the number of conductive layers and dielectric layers increases within a certain range, the cycle life and safety performance of electrochemical devices first show an increasing trend, and then remain basically unchanged. Therefore, for economic considerations, generally The number of layers of the conductive layer M=4 to 6, and/or the number of layers of the dielectric layer N=4 to 6.
除了上述层叠方向与锂金属层或集流体延伸方向垂直的方式以外,层叠方向与锂金属层的延伸方向或集流体的延伸方向还可以平行或呈任意锐角。In addition to the above-mentioned manner in which the stacking direction is perpendicular to the extending direction of the lithium metal layer or the current collector, the stacking direction and the extending direction of the lithium metal layer or the extending direction of the current collector may be parallel or at any acute angle.
图4为本申请另一实施例中负极极片的结构示意图,如图4所示,该负极极片包括锂金属层或集流体d、功能层e,功能层e设置在锂金属层或集流体d的一功能表面。其中,功能层e包括导电层a1、导电层a2、介电层b1、介电层b2和锂润湿材料c;图4中M=2,N=2,层叠方向与锂金属层的延伸方向或集流体的延伸方向平行,图中箭头方向为层叠方向。FIG. 4 is a schematic structural diagram of a negative electrode pole piece in another embodiment of the present application. As shown in FIG. 4 , the negative electrode pole piece includes a lithium metal layer or a current collector d and a functional layer e, and the functional layer e is disposed on the lithium metal layer or the current collector. A functional surface of fluid d. The functional layer e includes a conductive layer a1, a conductive layer a2, a dielectric layer b1, a dielectric layer b2 and a lithium wetting material c; M=2, N=2 in FIG. 4, the stacking direction and the extending direction of the lithium metal layer Or the extension direction of the current collector is parallel, and the direction of the arrow in the figure is the lamination direction.
图5为本申请又一实施例中负极极片的结构示意图,如图5所示,该负极极片包括锂金属层或集流体d、功能层e,功能层e设置在锂金属层或集流体d的一功能表面。其中,功能层e包括导电层a1、导电层a2、介电层b1、介电层b2和锂润湿材料c;M=2,N=2,层叠方向与锂金属层的延伸方向或集流体的延伸方向成锐角,图中箭头方向为层叠方向。FIG. 5 is a schematic structural diagram of a negative electrode pole piece in another embodiment of the application. As shown in FIG. 5 , the negative electrode pole piece includes a lithium metal layer or a current collector d and a functional layer e, and the functional layer e is disposed on the lithium metal layer or the collector. A functional surface of fluid d. The functional layer e includes a conductive layer a1, a conductive layer a2, a dielectric layer b1, a dielectric layer b2 and a lithium wetting material c; M=2, N=2, the stacking direction and the extending direction of the lithium metal layer or the current collector The direction of extension is an acute angle, and the direction of the arrow in the figure is the stacking direction.
发明人在研究过程中发现,相比图4和图5所示的实施方式,采用图3所示的实施方式能够更有利于功能层发挥抑制界面锂枝晶形成的能力,从而能够使得电化学装置的循环寿命和安全性能更优。During the research process, the inventors found that, compared with the embodiments shown in FIGS. 4 and 5 , the embodiment shown in FIG. 3 can be more conducive to the functional layer’s ability to inhibit the formation of lithium dendrites at the interface, so that the electrochemical performance can be improved. The cycle life and safety performance of the device are better.
需要补充说明的是,不论层叠方向与锂金属层或集流体延伸方向垂直、平行或呈任意锐角,功能层设置在锂金属层或集流体的功能表面均包括功能层设置在锂金属层或集流体的一个功能表面和两个功能表面两种情形。在具体实施过程中,在锂金属层或集流体的一个功能表面设置一个功能层,还是两个功能表面设置两个功能层,以及不同功能表面设置的功能层的层叠方向与锂金属层或集流体延伸方向的关系可根据对负极极片的需求自行选择。It should be added that no matter the stacking direction is perpendicular, parallel or any acute angle to the extending direction of the lithium metal layer or current collector, the functional layer disposed on the functional surface of the lithium metal layer or current collector includes the functional layer disposed on the lithium metal layer or current collector. One functional surface and two functional surfaces of the fluid. In the specific implementation process, one functional layer is provided on one functional surface of the lithium metal layer or current collector, or two functional layers are provided on two functional surfaces, and the stacking direction of the functional layers provided on different functional surfaces is related to the lithium metal layer or the current collector. The relationship of the fluid extension direction can be selected according to the needs of the negative pole piece.
在本申请中,M个导电层与N个介电层的层叠顺序对功能层的性能产生一定的影响。作为一种优选的实施方式,本申请的M个导电层和N个介电层交错层叠设置。In this application, the stacking sequence of the M conductive layers and the N dielectric layers has a certain influence on the performance of the functional layer. As a preferred embodiment, the M conductive layers and the N dielectric layers of the present application are alternately stacked.
与i(2≤i≤M)个导电层层叠后再与k(2≤k≤N)个介电层层叠的方式相比,导电层和介电层交错层叠设置能够使得功能层中产生的锂枝晶更容易接触到导电层,从而更有利于导电层对锂枝晶进行“自纠错”进而抑制锂枝晶的进一步生长,降低锂枝晶戳破隔膜造成短路的风险,以及锂枝晶造成的能量密度损失,改善电化学装置安全性能和循环寿命。Compared with the way in which i (2≤i≤M) conductive layers are stacked and then k (2≤k≤N) dielectric layers are stacked, the cross-stacking arrangement of conductive layers and dielectric layers can make the generation of noise generated in the functional layer. Lithium dendrites are easier to contact the conductive layer, which is more conducive to the "self-correction" of lithium dendrites by the conductive layer, thereby inhibiting the further growth of lithium dendrites, reducing the risk of lithium dendrites puncturing the separator and causing short circuits, and lithium dendrites. The energy density loss caused by crystals can be improved, and the safety performance and cycle life of electrochemical devices can be improved.
在一种优选的实施方式中,功能层的第一边缘层和/或第二边缘层为介电层。In a preferred embodiment, the first edge layer and/or the second edge layer of the functional layer is a dielectric layer.
本申请中,功能层的第一边缘层和/或第二边缘层分别是指功能层在层叠方向上的第一层和/或最后一层。In this application, the first edge layer and/or the second edge layer of the functional layer respectively refers to the first layer and/or the last layer of the functional layer in the stacking direction.
能够理解,当M=1时,不论导电层和介电层如何层叠,功能层的第一边缘层和/或第二边缘层必定为介电层。当M≥2时,本申请中功能层的第一边缘层和/或第二边缘层为介电层。It can be understood that when M=1, no matter how the conductive layer and the dielectric layer are stacked, the first edge layer and/or the second edge layer of the functional layer must be a dielectric layer. When M≧2, the first edge layer and/or the second edge layer of the functional layer in the present application is a dielectric layer.
由于锂润湿材料分布在导电层内,因此,当第一边缘层和/或第二边缘层为介电层时,锂离子更倾向于沉积在功能层内部,因此,负极界面的锂沉积量减少,负极界面锂枝晶的形成受到抑制,从而电化学装置的循环寿命和安全性能够得到进一步提高。Since the lithium wetting material is distributed in the conductive layer, when the first edge layer and/or the second edge layer is a dielectric layer, lithium ions are more likely to be deposited inside the functional layer, so the amount of lithium deposition at the negative electrode interface In this way, the formation of lithium dendrites at the negative electrode interface is suppressed, so that the cycle life and safety of the electrochemical device can be further improved.
发明人在研究过程中发现,导电层的电导率为10 -7S/cm至10 6S/cm,和/或,介电层的电导率小于10 -8S/cm时,电化学装置具有更加优异的能量密度、循环寿命和安全性能。 During the research, the inventors found that when the conductivity of the conductive layer is 10 -7 S/cm to 10 6 S/cm, and/or, when the conductivity of the dielectric layer is less than 10 -8 S/cm, the electrochemical device has Better energy density, cycle life and safety performance.
本申请通过导电层的电导率和/或介电层的电导率的控制可以优化功能层中的电流密度,更有利于锂离子沉积在功能层内部,抑制锂枝晶的形成。当导电层的电导率和/或介电层的电导率在上述范围内时,功能层中的电流密度既不会过高,从而加大功能层中锂枝晶的生成风险,也不会过低,而使得大量的锂无法在功能层内完成得电子沉积,使得电化学装置的容量降低;因此,能够实现电化学装置安全性能、循环性能和容量的有机统一。The present application can optimize the current density in the functional layer by controlling the conductivity of the conductive layer and/or the conductivity of the dielectric layer, which is more conducive to the deposition of lithium ions inside the functional layer and inhibits the formation of lithium dendrites. When the conductivity of the conductive layer and/or the conductivity of the dielectric layer is within the above range, the current density in the functional layer will neither be too high, thereby increasing the risk of lithium dendrite formation in the functional layer, nor will the current density in the functional layer be too high. Therefore, the organic unity of safety performance, cycle performance and capacity of electrochemical devices can be realized.
当导电层的材质选择导体材料时,导电层的电导率在10 -3S/cm至10 6S/cm;当导电层的材质选择半导体材料时,导电层的电导率在10 -7至10 3。在具体的实施过程中,可以通过导电层材料或介电层材料的选择、在导电层和/或介电层的制备过程中选择合适的参数、在导电层和/或介电层的制备过程中加入一定量的导电剂或绝缘材料等等方法调整导电层和/或介电层的电导率,使得导电层和/或介电层的电导率在上述范围。 When the material of the conductive layer is a conductor material, the conductivity of the conductive layer is 10 -3 S/cm to 10 6 S/cm; when the material of the conductive layer is a semiconductor material, the conductivity of the conductive layer is 10 -7 to 10 3 . In the specific implementation process, the selection of conductive layer materials or dielectric layer materials, the selection of appropriate parameters in the preparation process of the conductive layer and/or the dielectric layer, the selection of the conductive layer and/or the dielectric layer preparation process The conductivity of the conductive layer and/or the dielectric layer is adjusted by adding a certain amount of conductive agent or insulating material, etc., so that the conductivity of the conductive layer and/or the dielectric layer is within the above range.
功能层的孔隙率对锂金属在功能层中的沉积有一定的影响,发明人在研究过程中发现,功能层的孔隙率为5%至90%,进一步可选为50%至90%。The porosity of the functional layer has a certain influence on the deposition of lithium metal in the functional layer. The inventor found in the research process that the porosity of the functional layer is 5% to 90%, and can be further selected to be 50% to 90%.
能够理解,功能层的孔隙率越大,越有利于锂离子在功能层内的穿梭,诱导锂离子更快速进入功能层内部进行沉积,而且功能层能够具有更大的比表面积为锂离子的沉积提供更多位点。然而,功能层大的孔隙率往往意味着功能层具有较大的体积,不利于电化学装置体积能量密度的提高。因此,将功能层的孔隙率控制在50%至90%的范围,从而可以在不影响电化学装置体积能量密度的前提下,诱导锂离子进入功能层内部并实现沉积,抑制界面锂枝晶的形成,改善电化学装置的循环寿命和安全性能。It can be understood that the larger the porosity of the functional layer, the more favorable it is for the shuttle of lithium ions in the functional layer, inducing lithium ions to enter the functional layer more quickly for deposition, and the functional layer can have a larger specific surface area for the deposition of lithium ions. Provide more sites. However, the large porosity of the functional layer often means that the functional layer has a large volume, which is not conducive to the improvement of the volumetric energy density of electrochemical devices. Therefore, the porosity of the functional layer is controlled in the range of 50% to 90%, so that lithium ions can be induced to enter the functional layer and deposited without affecting the volume energy density of the electrochemical device, and the interfacial lithium dendrite can be suppressed. formed to improve the cycle life and safety performance of electrochemical devices.
在具体实施过程中,可以选择具有合适孔隙率的导电层和介电层材料、导电层与介电层的厚度、配合适宜的导电层与介电层的制备工艺(如,静电纺丝的温度、纺丝液浓度)、以及导电层与介电层的层叠工艺(如,热压的压力和温度)使得功能层的孔隙率在50%至90%。In the specific implementation process, the materials of the conductive layer and the dielectric layer with suitable porosity, the thickness of the conductive layer and the dielectric layer, and the appropriate preparation process of the conductive layer and the dielectric layer (for example, the temperature of electrospinning) can be selected. , spinning solution concentration), and the lamination process (eg, pressure and temperature of hot pressing) of the conductive layer and the dielectric layer make the porosity of the functional layer between 50% and 90%.
功能层良好的机械强度能够实现功能层充放电循环中结构的稳定性,避免功能层在循环过程中发生破碎,使得功能层能够持续发挥效用,保证负极极片稳定的构造。在具体实施过程中,功能层的机械强度可以通过选择合适强度的导电层和介电层材料,结合导电层与介电层的制备工艺、导电层与介电层的层叠工艺等方式调整。The good mechanical strength of the functional layer can realize the stability of the structure of the functional layer during the charge-discharge cycle, prevent the functional layer from being broken during the cycle, so that the functional layer can continue to function, and ensure the stable structure of the negative pole piece. In the specific implementation process, the mechanical strength of the functional layer can be adjusted by selecting the materials of the conductive layer and the dielectric layer with appropriate strength, combining the preparation process of the conductive layer and the dielectric layer, and the stacking process of the conductive layer and the dielectric layer.
在上述负极极片的基础上,本申请的负极极片的功能层还包括锂金属,锂金属在功能层中的含量为0.25mg/cm 2至25mg/cm 2,即,每平方厘米功能层的面积包括0.25mg至25mg锂金属。功能层的面积指功能层最靠近集流体功能表面的表面的面积。 On the basis of the above negative pole piece, the functional layer of the negative pole piece of the present application further includes lithium metal, and the content of lithium metal in the functional layer is 0.25 mg/cm 2 to 25 mg/cm 2 , that is, per square centimeter of the functional layer The area includes 0.25mg to 25mg lithium metal. The area of the functional layer refers to the area of the surface of the functional layer closest to the functional surface of the current collector.
通过在功能层中包括一定含量的锂金属,可以补充放电循环中损失的锂,更进一步提高包括该负极极片的电化学装置的循环寿命。By including a certain content of lithium metal in the functional layer, the lithium lost in the discharge cycle can be supplemented, and the cycle life of the electrochemical device including the negative electrode plate can be further improved.
在具体实施过程中,可以通过熔融法、物理气相沉积法、电化学法等方式使得功能层中包括上述含量的锂金属。In a specific implementation process, the functional layer may include the above-mentioned content of lithium metal by means of a melting method, a physical vapor deposition method, an electrochemical method, or the like.
本申请第二方面还提供一种电化学装置,该电化学装置包括上述的负极极片。能够理解,电化学装置中,除负极极片外,一般还包括正极极片、电解液(电解质)、隔膜等。A second aspect of the present application further provides an electrochemical device, the electrochemical device comprising the above-mentioned negative electrode plate. It can be understood that an electrochemical device generally includes a positive electrode, an electrolyte (electrolyte), a separator, and the like in addition to the negative electrode.
本申请对电化学装置不作严格限制,例如,该电化学装置可以卷绕电池、叠片电池、固态电池等等。在具体实施过程中,可以根据需求使用本申请的负极极片、配合合适的正极极片、电解液(电解质)、隔膜等构造合适的电化学装置。The present application does not impose strict limitations on the electrochemical device, for example, the electrochemical device may be a wound battery, a laminated battery, a solid-state battery, and the like. In the specific implementation process, a suitable electrochemical device can be constructed by using the negative electrode plate of the present application, matched with a suitable positive electrode plate, electrolyte (electrolyte), separator, etc., as required.
在本申请的一些实施例中,负极极片可以只有功能层,此时,可以使得功能层的延伸方向与正极极片的延伸方向平行,从而实现电化学装置的负极极片与正极极片相对,并与隔膜、电解液(质)配合,获得循环寿命与安全性能优异的电化学装置。In some embodiments of the present application, the negative pole piece may only have a functional layer. In this case, the extending direction of the functional layer may be parallel to the extending direction of the positive pole piece, so that the negative pole piece and the positive pole piece of the electrochemical device are opposite to each other. , and cooperate with the diaphragm and electrolyte (quality) to obtain an electrochemical device with excellent cycle life and safety performance.
在本申请的另一些实施例中,负极极片包括功能层和集流体,功能层设置在集流体的功能表面,此时,通过使得集流体的延伸方向与正极极片的延伸方向平行,并与隔膜、电解液(质)配合,获得循环寿命和安全性能优异的电化学装置。In other embodiments of the present application, the negative pole piece includes a functional layer and a current collector, and the functional layer is arranged on the functional surface of the current collector. Cooperate with diaphragm and electrolyte (quality) to obtain electrochemical devices with excellent cycle life and safety performance.
本申请的电化学装置,其负极极片包括的功能层能够有效降低负极极片在充放电循环中的体积膨胀以及锂枝晶的形成,从而使得电化学装置具有优异的循环寿命和安全性能。In the electrochemical device of the present application, the functional layer included in the negative electrode plate can effectively reduce the volume expansion of the negative electrode plate and the formation of lithium dendrites during charge-discharge cycles, so that the electrochemical device has excellent cycle life and safety performance.
本申请第三方面还提供一种电子装置,该装置包括上述的电化学装置。电化学装置可以作为该电子装置的驱动源或能量存储单元。本申请中的电子装置可以但不限于是移动设备(如,智能手表、手机、笔记本电脑等)、电动车辆(如电动自行车、混合动力电动车、助力自行车等)等。A third aspect of the present application further provides an electronic device, which includes the above electrochemical device. An electrochemical device can be used as a driving source or an energy storage unit for the electronic device. The electronic devices in this application can be, but are not limited to, mobile devices (eg, smart watches, mobile phones, notebook computers, etc.), electric vehicles (eg, electric bicycles, hybrid electric vehicles, power-assisted bicycles, etc.), and the like.
本申请的电子装置,由于包括前述电化学装置,因此具有优异的续航能力,使用寿命以及安全性能,用户体验感良好。Since the electronic device of the present application includes the aforementioned electrochemical device, it has excellent endurance, service life and safety performance, and has a good user experience.
下面结合实施例,进一步阐述本申请。应理解,这些实施例仅用于说明本申请而不用于限制本申请的范围。在下述实施例中,除非另有说明,所用到的原料均可商购获得。The present application will be further described below with reference to the embodiments. It should be understood that these examples are only used to illustrate the present application and not to limit the scope of the present application. In the following examples, the raw materials used were all commercially available unless otherwise stated.
实施例1-17的扣式电池均按照下述方法进行制备。The button cells of Examples 1-17 were all prepared according to the following methods.
(1)负极极片的制备(1) Preparation of negative pole piece
A:导电层的制备:将0.8质量份的聚丙烯腈溶于10质量份的N,N-二甲基甲酰胺而后加入四氯化锡,获得包含一定浓度的四氯化锡的纺丝液;将纺丝液注入静电纺丝装置进行静电纺丝得到聚丙烯腈纤维膜,在纺丝过程中,设置静电纺丝装置的工作状态控制聚丙烯腈纤维膜的厚度;之后,将聚丙烯腈纤维膜置于马弗炉,在空气气氛中以1℃每分钟的升温速率将马弗炉升温至230℃后保持2小时,对聚丙烯腈纤维膜进行预氧化,将完成预氧化的聚丙烯腈纤维膜在管式炉中氩气气氛下,以5℃每分钟的升温速率升温至800℃保持4小时,得到的碳纤维膜中分布有二氧化锡(锂润湿材料),得到导电层;A: Preparation of conductive layer: 0.8 parts by mass of polyacrylonitrile was dissolved in 10 parts by mass of N,N-dimethylformamide and then tin tetrachloride was added to obtain a spinning solution containing a certain concentration of tin tetrachloride ; The spinning solution is injected into the electrospinning device for electrospinning to obtain a polyacrylonitrile fiber film. During the spinning process, the working state of the electrospinning device is set to control the thickness of the polyacrylonitrile fiber film; The fiber membrane was placed in a muffle furnace, and the muffle furnace was heated to 230 °C at a heating rate of 1 °C per minute in an air atmosphere, and then kept for 2 hours. The polyacrylonitrile fiber membrane was pre-oxidized, and the pre-oxidized polypropylene was The nitrile fiber film is heated to 800°C at a heating rate of 5°C per minute under an argon atmosphere in a tube furnace for 4 hours, and tin dioxide (lithium wetting material) is distributed in the obtained carbon fiber film to obtain a conductive layer;
向静电纺丝装置中注入纺丝液的过程中,当纺丝液中四氯化锡浓度不发生变化时(即对四氯化锡的浓度不调整时),可以得到沿聚丙烯腈纤维膜厚度方向四氯化锡的含量均匀分布的聚丙烯腈纤维膜;In the process of injecting the spinning solution into the electrospinning device, when the concentration of tin tetrachloride in the spinning solution does not change (that is, when the concentration of tin tetrachloride is not adjusted), a polyacrylonitrile fiber membrane can be obtained along the A polyacrylonitrile fiber film with a uniform distribution of tin tetrachloride content in the thickness direction;
向静电纺丝装置中注入纺丝液的过程中,在不同时间段调整纺丝液中的四氯化锡的浓度使四氯化锡浓度呈现梯度变化,可以得到沿聚丙烯腈纤维膜厚度方向四氯化锡的含量梯度分布的聚丙烯腈纤维膜;During the process of injecting the spinning solution into the electrospinning device, the concentration of tin tetrachloride in the spinning solution was adjusted at different time periods so that the concentration of tin tetrachloride showed a gradient change, which could be obtained along the thickness direction of the polyacrylonitrile fiber film. The polyacrylonitrile fiber membrane with the content gradient distribution of tin tetrachloride;
B:介电层的制备:将0.8质量份的聚偏氟乙烯溶于10质量份的N,N-二甲基加酰胺得到纺丝液,将纺丝液注入静电纺丝装置进行静电纺丝得到聚偏氟乙烯纤维膜,设置静电纺丝装置的工作状态,控制聚偏氟乙烯纤维膜的厚度;将聚偏氟乙烯纤维膜置于真空干燥箱中在80℃下保持12小时,得到介电层;B: Preparation of dielectric layer: 0.8 parts by mass of polyvinylidene fluoride was dissolved in 10 parts by mass of N,N-dimethyl amide to obtain a spinning solution, and the spinning solution was injected into an electrospinning device for electrospinning The polyvinylidene fluoride fiber membrane was obtained, the working state of the electrospinning device was set, and the thickness of the polyvinylidene fluoride fiber membrane was controlled; electric layer;
C:功能层的制备:将M个导电层与N个介电层冲切成直径18mm的圆片,采用热压方式,将M个导电层与N个介电层交错层叠,得到功能层,利用电化学方法,在功能层中预补锂,使得锂金属在功能层中的含量为4.1mg/cm 2C: Preparation of functional layers: The M conductive layers and the N dielectric layers are punched into a disc with a diameter of 18 mm, and the M conductive layers and the N dielectric layers are alternately stacked by means of hot pressing to obtain the functional layer. Using an electrochemical method, lithium is pre-supplemented in the functional layer, so that the content of lithium metal in the functional layer is 4.1 mg/cm 2 ;
D:采用热压的方式将步骤C得到的功能层设置在负极集流体铜箔的一功能表面,得到负极极片;D: the functional layer obtained in step C is arranged on a functional surface of the negative electrode current collector copper foil by means of hot pressing to obtain a negative electrode pole piece;
其中,导电层与介电层的层叠方向与铜箔集流体的延伸方向垂直。Wherein, the stacking direction of the conductive layer and the dielectric layer is perpendicular to the extending direction of the copper foil current collector.
(2)正极极片的制备(2) Preparation of positive electrode sheet
将正极活性材料磷酸铁锂、导电炭黑、聚偏二氟乙烯按照质量比97.5:1.0:1.5混合后加入N-甲基吡咯烷酮中,调配成为固含量为0.75的正极浆料,并搅拌均匀,将正极浆料均匀涂覆在集流体铝箔一功能表面上,90℃下烘干铝箔,得到正极极片,将正极极片冲切成直径14mm的薄片;The positive electrode active material lithium iron phosphate, conductive carbon black, and polyvinylidene fluoride are mixed in a mass ratio of 97.5:1.0:1.5 and added to N-methylpyrrolidone to prepare a positive electrode slurry with a solid content of 0.75, and stir evenly. The positive electrode slurry is uniformly coated on the functional surface of the current collector aluminum foil, the aluminum foil is dried at 90°C to obtain a positive electrode piece, and the positive electrode piece is punched into a sheet with a diameter of 14 mm;
其中,正极极片上正极活性材料的负载量为1mg/cm 2The loading amount of the positive electrode active material on the positive electrode sheet is 1 mg/cm 2 .
(3)电解液的制备(3) Preparation of electrolyte
在干燥氩气气氛中,首先将二氧环戊烷、二甲醚按照1:1的体积比混合得到混合液,然后在混合液中加入双三氟甲磺酰亚胺锂并混合均匀,得到双三氟甲磺酰亚胺锂浓度为1M的电解液。In a dry argon atmosphere, firstly, dioxolane and dimethyl ether were mixed in a volume ratio of 1:1 to obtain a mixed solution, and then lithium bistrifluoromethanesulfonimide was added to the mixed solution and mixed uniformly to obtain The electrolyte solution with lithium bistrifluoromethanesulfonimide concentration of 1M.
(4)扣式电池组装(4) Button battery assembly
选择CR2032电池壳,电池壳直径为20mm,高度为3.2mm,片厚为0.25mm;将上述负极极片、正极极片、以及隔膜按照本领域常用扣式电池组装方式完成组装,组装后进行侧封-顶封-注液-封装,最终得到扣式电池;Choose CR2032 battery case, the diameter of the battery case is 20mm, the height is 3.2mm, and the thickness is 0.25mm; the above-mentioned negative pole piece, positive pole piece, and separator are assembled according to the button battery assembly method commonly used in the field, and the side is assembled after assembly. Sealing - top sealing - liquid injection - packaging, and finally a button battery is obtained;
其中,隔膜为厚度为15μm的聚乙烯膜。The separator is a polyethylene film with a thickness of 15 μm.
实施例18Example 18
本实施例扣式电池的制备与实施例1制备步骤基本相同,唯一不同处在于,本实施例在(1)制备负极极片的步骤C中获得功能层后不进行预补锂。The preparation of the button battery in this example is basically the same as that in Example 1. The only difference is that this example does not pre-supplement lithium after obtaining the functional layer in step C of (1) preparing the negative pole piece.
实施例19Example 19
本实施例扣式电池的制备与实施例1制备步骤基本相同,唯一不同处在于,本实施例在(1)制备负极极片的步骤D中采用热压的方式将步骤C得到的功能层设置在负极集流体铜箔的一 功能表面得到负极极片时,介电层与导电层的层叠方向与集流体的延伸方向平行。The preparation of the button battery in this example is basically the same as that in Example 1. The only difference is that in this example, in the step D of (1) preparing the negative pole piece, the functional layer obtained in the step C is formed by hot pressing. When a negative electrode pole piece is obtained on a functional surface of the negative electrode current collector copper foil, the stacking direction of the dielectric layer and the conductive layer is parallel to the extending direction of the current collector.
实施例20Example 20
本实施例扣式电池的制备与实施例1制备步骤基本相同,唯一不同处在于,本实施例在(1)负极极片的制备步骤D中,在将功能层设置在负极集流体铜箔前,使用1.5T的辊机对功能层进行辊压,辊压速度为1m/min。The preparation steps of the button battery in this example are basically the same as those in Example 1. The only difference is that in (1) the preparation step D of the negative pole piece in this example, the functional layer is arranged before the negative electrode current collector copper foil. , using a 1.5T roller machine to roll the functional layer, and the rolling speed is 1m/min.
对比例1Comparative Example 1
本对比例的扣式电池的制备过程如下:The preparation process of the button battery of this comparative example is as follows:
(1)负极极片的制备(1) Preparation of negative pole piece
将0.8质量份的聚丙烯腈溶于10质量份的溶剂得到纺丝液,将纺丝液注入静电纺丝装置进行静电纺丝得到聚丙烯腈纤维膜,设置静电纺丝装置的工作状态,使得聚丙烯腈纤维膜的厚度为60μm;之后,将聚丙烯腈纤维膜置于马弗炉,在空气气氛中以1℃每分钟的升温速率将马弗炉升温至230℃后保持2小时,对聚丙烯腈纤维膜进行预氧化,而后将完成预氧化的聚丙烯腈纤维膜在管式炉中氩气气氛下以5℃每分钟的升温速率升温至800℃保持4小时,得到碳纤维膜,将碳纤维膜冲切为直径18mm的薄片,得到导电层,将导电层通过热压设置在负极集流体铜箔的一功能表面,利用电化学方法,在功能层中预补锂,使得锂金属在功能层中的含量为4.1mg/cm 2,得到负极极片; Dissolve 0.8 parts by mass of polyacrylonitrile in 10 parts by mass of a solvent to obtain a spinning solution, inject the spinning solution into an electrospinning device for electrospinning to obtain a polyacrylonitrile fiber film, and set the working state of the electrospinning device so that The thickness of the polyacrylonitrile fiber film was 60 μm; after that, the polyacrylonitrile fiber film was placed in a muffle furnace, and the muffle furnace was heated to 230 °C at a heating rate of 1 °C per minute in an air atmosphere and kept for 2 hours. The polyacrylonitrile fiber film is pre-oxidized, and then the pre-oxidized polyacrylonitrile fiber film is heated to 800° C. at a heating rate of 5° C. per minute under an argon atmosphere in a tube furnace for 4 hours to obtain a carbon fiber film. The carbon fiber film is punched into thin sheets with a diameter of 18 mm to obtain a conductive layer, which is placed on a functional surface of the negative electrode current collector copper foil by hot pressing, and lithium is pre-supplemented in the functional layer by an electrochemical method, so that lithium metal is functional. The content in the layer is 4.1 mg/cm 2 to obtain a negative pole piece;
本对比例中正极极片的制备、电解液的制备、扣式组装的过程与实施例1一致。In this comparative example, the preparation of the positive pole piece, the preparation of the electrolyte, and the process of button-type assembly are the same as those in Example 1.
对比例2Comparative Example 2
本对比例中扣式电池的制备过程如下:The preparation process of the button battery in this comparative example is as follows:
(1)负极极片的制备(1) Preparation of negative pole piece
将0.8质量份的聚偏氟乙烯溶于10质量份的溶剂得到纺丝液,将纺丝液注入静电纺丝装置进行静电纺丝得到聚偏氟乙烯纤维膜,设置静电纺丝装置的工作状态,使得聚偏氟乙烯纤维膜的厚度为60μm;将聚偏氟乙烯纤维膜置于真空干燥箱中在80℃下保持12小时,而后将聚偏氟乙烯纤维膜冲切成直径为18mm的薄片,得到介电层,将介电层通过热压设置在负极集流体铜箔的一功能表面,得到负极极片;Dissolve 0.8 parts by mass of polyvinylidene fluoride in 10 parts by mass of a solvent to obtain a spinning solution, inject the spinning solution into an electrospinning device for electrospinning to obtain a polyvinylidene fluoride fiber film, and set the working state of the electrospinning device , so that the thickness of the polyvinylidene fluoride fiber film is 60 μm; the polyvinylidene fluoride fiber film is placed in a vacuum drying oven at 80 ° C for 12 hours, and then the polyvinylidene fluoride fiber film is punched into pieces with a diameter of 18mm. , obtain a dielectric layer, and set the dielectric layer on a functional surface of the negative electrode current collector copper foil by hot pressing to obtain a negative electrode pole piece;
本对比例中正极极片的制备、电解液的制备、扣式电池组装的过程与实施例1一致。In this comparative example, the preparation of the positive pole piece, the preparation of the electrolyte, and the assembly of the button battery are the same as those in Example 1.
对比例3Comparative Example 3
本对比例中扣式电池的制备过程如下:The preparation process of the button battery in this comparative example is as follows:
(1)负极极片的制备(1) Preparation of negative pole piece
将0.8质量份的聚丙烯腈溶于10质量份的N,N-二甲基加酰胺溶剂,而后加入四氯化锡,使得纺丝液中四氯化锡的浓度为0.4M;将纺丝液注入静电纺丝装置进行静电纺丝得到聚丙烯腈纤维膜,设置静电纺丝装置的工作状态,使得聚丙烯腈纤维膜的厚度为60μm;之后,将聚丙烯腈纤维膜置于马弗炉,在空气气氛中以1℃每分钟的升温速率将马弗炉升温至230℃后保持2小时,对聚丙烯腈纤维膜进行预氧化,将完成预氧化的聚丙烯腈纤维膜在管式炉中氩气气氛下,以5℃每分钟的升温速率升温至800℃保持4小时,得到的碳纤维膜中在沿碳纤维膜厚 度方向上均匀分布二氧化锡,将碳纤维膜冲切为直径18mm的薄片,得到导电层,将导电层通过热压设置在负极集流体铜箔的一功能表面,得到负极极片;Dissolve 0.8 parts by mass of polyacrylonitrile in 10 parts by mass of N,N-dimethyl amide solvent, and then add tin tetrachloride, so that the concentration of tin tetrachloride in the spinning solution is 0.4M; The liquid was injected into the electrospinning device for electrospinning to obtain a polyacrylonitrile fiber membrane, and the working state of the electrospinning device was set so that the thickness of the polyacrylonitrile fiber membrane was 60 μm; after that, the polyacrylonitrile fiber membrane was placed in a muffle furnace , in the air atmosphere at a heating rate of 1 ℃ per minute, the muffle furnace is heated to 230 ℃ and kept for 2 hours, the polyacrylonitrile fiber film is pre-oxidized, and the pre-oxidized polyacrylonitrile fiber film is placed in the tube furnace. In a medium argon atmosphere, the temperature was raised to 800°C at a heating rate of 5°C per minute and held for 4 hours. In the obtained carbon fiber film, tin dioxide was uniformly distributed along the thickness direction of the carbon fiber film, and the carbon fiber film was punched into pieces with a diameter of 18 mm. , obtain a conductive layer, and set the conductive layer on a functional surface of the negative electrode current collector copper foil by hot pressing to obtain a negative electrode pole piece;
本对比例中正极极片的制备、电解液的制备、扣式电池组装的过程与实施例1一致。In this comparative example, the preparation of the positive pole piece, the preparation of the electrolyte, and the assembly of the button battery are the same as those in Example 1.
对比例4Comparative Example 4
本对比例采用直径为18mm的铜箔作为负极极片;In this comparative example, a copper foil with a diameter of 18mm was used as the negative pole piece;
本对比例中正极极片的制备、电解液的制备、扣式电池组装的过程与实施例1一致。In this comparative example, the preparation of the positive pole piece, the preparation of the electrolyte, and the assembly of the button battery are the same as those in Example 1.
具体各个实施例与对比例中,导电层层数(M)、介电层层数(N)、热压前导电层厚度、热压前介电层厚度、功能层在沿层叠方向的厚度、负极极片的组成、制备各导电层时不同纺丝时间段向静电纺丝装置中加入的纺丝液的四氯化锡的浓度、导电层中锂润湿材料在远离集流体方向上的含量分布等参数如表1所示。In the specific examples and comparative examples, the number of conductive layers (M), the number of dielectric layers (N), the thickness of the conductive layer before hot pressing, the thickness of the dielectric layer before hot pressing, the thickness of the functional layer along the stacking direction, The composition of the negative pole piece, the concentration of tin tetrachloride in the spinning solution added to the electrospinning device at different spinning time periods when preparing each conductive layer, and the content of the lithium wetting material in the conductive layer in the direction away from the current collector The distribution and other parameters are shown in Table 1.
表1Table 1
Figure PCTCN2021081366-appb-000001
Figure PCTCN2021081366-appb-000001
Figure PCTCN2021081366-appb-000002
Figure PCTCN2021081366-appb-000002
Figure PCTCN2021081366-appb-000003
Figure PCTCN2021081366-appb-000003
表1中功能层在层叠方向的厚度通过使用氩离子抛光CP法制备负极极片的样品后利用扫描电子显微镜观测获得。The thickness of the functional layer in the stacking direction in Table 1 was obtained by using the argon ion polishing CP method to prepare a sample of the negative pole piece and then observing it with a scanning electron microscope.
各实施例与对比例中导电层与介电层的电导率、功能层的孔隙率、锂润湿材料的质量基于功能层的质量如表2所示。The electrical conductivity of the conductive layer and the dielectric layer, the porosity of the functional layer, and the quality of the lithium-wetting material based on the quality of the functional layer in each Example and Comparative Example are shown in Table 2.
表2Table 2
Figure PCTCN2021081366-appb-000004
Figure PCTCN2021081366-appb-000004
Figure PCTCN2021081366-appb-000005
Figure PCTCN2021081366-appb-000005
Figure PCTCN2021081366-appb-000006
Figure PCTCN2021081366-appb-000006
表2中,相关参数的检测方法如下:In Table 2, the detection methods of relevant parameters are as follows:
1、电导率:1. Conductivity:
A.将四探针电阻率开启,并用标准电阻法校准仪器,确定仪器能够正常使用;A. Turn on the resistivity of the four probes, and calibrate the instrument with the standard resistance method to confirm that the instrument can be used normally;
B.根据样品厚度设定薄膜的厚度,选择探头形状为方形,根据样品厚度和材质不同选择电压档位和探针间距;B. Set the thickness of the film according to the thickness of the sample, select the shape of the probe as square, and select the voltage gear and probe spacing according to the thickness and material of the sample;
C.连接测试探头,通过上下微调节探头平台,使探针与样品接触,C. Connect the test probe, and make the probe contact with the sample by adjusting the probe platform up and down slightly.
D.待四探针电阻仪显示的电阻数据稳定后读取电导率数据即为样品的电导率;D. After the resistance data displayed by the four-probe resistance meter is stable, the conductivity data is read as the conductivity of the sample;
2、功能层的孔隙率:2. The porosity of the functional layer:
根据国标法GB/T 21650.1-2008,利用压汞法测试功能层的孔隙率;According to the national standard method GB/T 21650.1-2008, the porosity of the functional layer is tested by mercury intrusion method;
3、锂润湿材料的含量:3. Content of lithium wetting material:
根据国标法GB/T 27761-2011,利用热重分析仪测试材料中二氧化锡的含量。According to the national standard method GB/T 27761-2011, the content of tin dioxide in the material was tested by thermogravimetric analyzer.
试验例Test example
对上述各实施例及对比例的负极极片、叠片扣式电池进行如下参数检测。The following parameters were tested for the negative pole pieces and laminated button batteries of the above embodiments and comparative examples.
1、负极极片组成:1. The composition of the negative pole piece:
使用扫描电子显微镜对实施例8获得的负极极片进行微观形貌的观察,结果见图6;The microscopic morphology of the negative pole piece obtained in Example 8 was observed using a scanning electron microscope, and the results are shown in Figure 6;
从图6可知:It can be seen from Figure 6 that:
图6中包括铜箔101,锂金属层201,介电层301、导电层401、介电层501、导电层601,因此,本申请的功能层由介电层与导电层层叠而成,具有三维结构;6 includes copper foil 101, lithium metal layer 201, dielectric layer 301, conductive layer 401, dielectric layer 501, and conductive layer 601. Therefore, the functional layer of the present application is formed by stacking a dielectric layer and a conductive layer, and has three-dimensional structure;
2、锂在负极极片中沉积状态:2. Lithium deposition state in the negative pole piece:
将实施例11和对比例1获得的负极极片以0.2C的倍率恒流充电至3.7V,然后恒压充电至0.025C,静置5min,以0.5C恒流放电至2.55V;循环10次之后,静置5min,用0.1C的倍率恒流充电至3.7V满充状态;采用氩离子抛光CP法制备负极极片的样品,而后使用扫描电镜对样品进行观察,结果分别见图7和图8;The negative pole pieces obtained in Example 11 and Comparative Example 1 were charged to 3.7V with a constant current of 0.2C, then charged to 0.025C with a constant voltage, left for 5 minutes, and discharged to 2.55V with a constant current of 0.5C; cycle 10 times After that, let it stand for 5 minutes, and charge it with a constant current of 0.1C to a full charge state of 3.7V; the sample of the negative electrode piece was prepared by the argon ion polishing CP method, and then the sample was observed by scanning electron microscope. The results are shown in Figures 7 and 7, respectively. 8;
从图7和图8的比较可知:From the comparison of Figure 7 and Figure 8, it can be seen that:
图7的负极极片中,锂在功能层内的沉积的非常致密,沉积量很大;而图8负极极片中锂离子沉积的非常松散,沉积量也更少;图7和图8的对比说明,本申请的负极极片能够有效诱导锂沉积在功能层内部,并且锂沉积的十分致密;而且,从图7中可以看出,锂不易沉积在靠近负极界面的区域,因此,负极界面锂枝晶的形成受到抑制;因此能够说明,当层叠方向与集流体延伸方向垂直,锂润湿材料在层叠方向上梯度递减时,负极极片能够诱导锂离子沉积在靠近集流体的区域,降低锂离子沉积负极界面的几率,抑制负极界面锂枝晶的形成;从而包括该负极极片的电化学装置能够表现出更好的循环寿命和安全性能;表3中,实施例11与对比例1扣式电池的循环圈数和体积膨胀率的结果比较也能够证实这一点;In the negative pole piece of Fig. 7, the deposition of lithium in the functional layer is very dense, and the deposition amount is large; while in the negative pole piece of Fig. 8, the deposition of lithium ions is very loose, and the deposition amount is also less; The comparison shows that the negative electrode plate of the present application can effectively induce lithium deposition inside the functional layer, and the lithium deposition is very dense; moreover, as can be seen from Figure 7, lithium is not easily deposited in the area close to the negative electrode interface, therefore, the negative electrode interface The formation of lithium dendrites is suppressed; therefore, it can be shown that when the stacking direction is perpendicular to the extension direction of the current collector, and the gradient of the lithium-wetting material decreases in the stacking direction, the negative electrode plate can induce the deposition of lithium ions in the region close to the current collector, reducing the The probability of lithium ions depositing on the negative electrode interface suppresses the formation of lithium dendrites on the negative electrode interface; thus the electrochemical device including the negative electrode pole piece can show better cycle life and safety performance; In Table 3, Example 11 and Comparative Example 1 This can also be confirmed by the comparison of the cycle number and volume expansion rate of the coin cell battery;
3、循环性能:3. Cycle performance:
在20℃下,利用蓝电电化学工作站,以0.2C的倍率恒流充电至3.7V,然后恒压充电至0.025C,静置5min,而后以0.5C恒流放电至2.55V;静置5min,此为一个循环,循环性能为放电容量衰减到首圈放电容量的80%时循环次数,结果见表3;At 20°C, using a blue-electric electrochemical workstation, charge to 3.7V at a rate of 0.2C with constant current, then charge with constant voltage to 0.025C, let stand for 5 minutes, and then discharge to 2.55V with a constant current of 0.5C; let stand for 5 minutes , this is one cycle, and the cycle performance is the number of cycles when the discharge capacity decays to 80% of the discharge capacity of the first cycle. The results are shown in Table 3;
4、体积膨胀率:4. Volume expansion rate:
20℃下,利用蓝电电化学工作站,以0.2C的倍率恒流充电至3.7V,然后恒压充电至0.025C,静置5min,以0.5C恒流放电至2.55V;静置5min,此为一个循环,当电池的放电容量衰减到首圈放电容量的80%时,停止测试,将电池拆解,取出负极极片后,浸泡在碳酸二甲酯溶液中,采用氩离子抛光CP法制备负极极片的样品,使用扫描电子显微镜观察负极极片的截面(垂直于集流体功能表面),获得负极极片的截面在循环后的厚度T,循环前负极极片的截面厚度为t,容量保持率=(T-t)/T,结果见表3;At 20°C, use a blue-electric electrochemical workstation to charge to 3.7V with a constant current of 0.2C, then charge to 0.025C with a constant voltage, let stand for 5 minutes, and discharge to 2.55V with a constant current of 0.5C; For one cycle, when the discharge capacity of the battery decayed to 80% of the discharge capacity of the first cycle, the test was stopped, the battery was disassembled, and the negative pole piece was taken out, soaked in dimethyl carbonate solution, and prepared by argon ion polishing CP method For the sample of the negative pole piece, use a scanning electron microscope to observe the cross section of the negative pole piece (perpendicular to the functional surface of the current collector), and obtain the thickness T of the cross section of the negative pole piece after the cycle. The thickness of the cross section of the negative pole piece before the cycle is t, the capacity Retention rate=(T-t)/T, the results are shown in Table 3;
5、库伦效率:5. Coulomb efficiency:
20℃下,利用蓝电电化学工作站,以0.2C的倍率恒流充电至3.7V,然后恒压充电至0.025C,静置5min,而后以0.5C恒流放电至2.55V,静置5min,此为一个循环,库伦效率为,当容量衰减至首圈放电容量的80%时,各圈放电容量与充电容量的比值的平均值,结果见表3。At 20°C, using a blue-electric electrochemical workstation, charged to 3.7V with a constant current rate of 0.2C, then charged to 0.025C with a constant voltage, let stand for 5 minutes, and then discharged to 2.55V with a constant current of 0.5C, let stand for 5 minutes, This is a cycle, and the Coulomb efficiency is the average value of the ratio of the discharge capacity to the charge capacity in each cycle when the capacity decays to 80% of the discharge capacity of the first cycle. The results are shown in Table 3.
表3table 3
类别category 循环性能(圈)Cycling performance (lap) 体积膨胀率(%)Volume expansion rate (%) 库伦效率Coulomb efficiency
实施例1Example 1 9090 8080 98.8%98.8%
实施例2Example 2 9393 8585 98.78%98.78%
实施例3Example 3 100100 7575 99.54%99.54%
实施例4Example 4 9090 8080 98.87%98.87%
实施例5Example 5 100100 8080 99.36%99.36%
实施例6Example 6 100100 8080 99.48%99.48%
实施例7Example 7 150150 6060 99.67%99.67%
实施例8Example 8 130130 8080 99.64%99.64%
实施例9Example 9 200200 3535 99.86%99.86%
实施例10Example 10 180180 4040 99.78%99.78%
实施例11Example 11 200200 3030 99.87%99.87%
实施例12Example 12 180180 3535 99.81%99.81%
实施例13Example 13 205205 2525 99.9%99.9%
实施例14Example 14 180180 3030 99.84%99.84%
实施例15Example 15 220220 2020 99.92%99.92%
实施例16Example 16 180180 5050 99.7%99.7%
实施例17Example 17 152152 4040 99.69%99.69%
实施例18Example 18 5050 3030 97%97%
实施例19Example 19 8080 9090 97.8%97.8%
实施例20Example 20 128128 9090 99.63%99.63%
对比例1Comparative Example 1 6060 300300 97.1%97.1%
对比例2Comparative Example 2 7070 100100 97.5%97.5%
对比例3Comparative Example 3 8080 180180 97.96%97.96%
对比例4Comparative Example 4 5050 500500 96%96%
从表3可知:It can be seen from Table 3 that:
1、实施例1至实施例17以及实施例19与各对比例相比,实施例的电池具有更大的循环圈数更小的体积膨胀率,说明电化学装置的负极极片满足本申请的技术方案时,电化学装置的循环性能和安全性能可以得到改善,原因在于:一方面,介电层能够降低功能层的电子浓度,防止锂离子在大电流密度下形成枝晶,从而抑制锂枝晶的形成;而且介电层还能够降低功能层表面的电子浓度,迫使锂离子进入功能层内部沉积,因此能够降低负极界面锂枝晶的形成;另一方面,锂润湿材料也能够诱导锂离子沉积在功能层内部,降低负极界面锂枝晶的形成;此外,导电层与介电层层叠构成的三维骨架能够降低功能层内形成的锂枝晶对负极极片的挤压和膨胀损毁,缓解负极极片在循环过程中的体积膨胀;虽然与进行预补锂的各对比例相比,实施例18的循环寿命较差,但是实施例18在没有进行预补锂的情况下,其库伦效率与对比例1和对比例2相比相差不大,因此说明本申请的功能层能够抑制锂枝晶的形成,进而降低了锂离子的消耗,从而有助于提升电化学装置的库伦效率;而对比例3由于与对比例1和对比例2相比包括锂润湿材料,锂润湿材料的存在能够进一步抑制锂枝晶的形成,进一步降低了锂离子的消耗, 因此对比例3的电化学装置的库伦效率有所提升;1. Compared with the comparative examples in Examples 1 to 17 and Example 19, the batteries of the examples have a larger number of cycles and a smaller volume expansion rate, indicating that the negative pole piece of the electrochemical device satisfies the requirements of the present application. In the technical solution, the cycle performance and safety performance of the electrochemical device can be improved because: on the one hand, the dielectric layer can reduce the electron concentration of the functional layer, prevent lithium ions from forming dendrites at high current density, thereby inhibiting lithium dendrites In addition, the dielectric layer can also reduce the electron concentration on the surface of the functional layer, forcing lithium ions to deposit inside the functional layer, thus reducing the formation of lithium dendrites at the negative interface; on the other hand, the lithium wetting material can also induce lithium The ions are deposited inside the functional layer to reduce the formation of lithium dendrites at the negative electrode interface; in addition, the three-dimensional skeleton formed by the stacking of the conductive layer and the dielectric layer can reduce the extrusion and expansion damage of the negative electrode pole pieces by the lithium dendrites formed in the functional layer. Alleviate the volume expansion of the negative pole piece during the cycle; although the cycle life of Example 18 is poor compared with the comparative examples with pre-supplementation of lithium, the coulomb of Example 18 without pre-supplementation of lithium Compared with Comparative Example 1 and Comparative Example 2, the efficiency is not much different, so it shows that the functional layer of the present application can inhibit the formation of lithium dendrites, thereby reducing the consumption of lithium ions, thereby helping to improve the Coulomb efficiency of the electrochemical device; Compared with Comparative Example 1 and Comparative Example 2, Comparative Example 3 includes a lithium wetting material, and the presence of the lithium wetting material can further inhibit the formation of lithium dendrites and further reduce the consumption of lithium ions. The Coulombic efficiency of chemical devices has been improved;
2、实施例1与3相比,实施例3的电池具有更大的循环圈数和更小的体积膨胀,锂润湿材料的含量在层叠方向上梯度递减时,对电化学装置的循环寿命和安全性能的改善效果更好,原因在于:锂润湿材料在靠近集流体的区域含量更高能够更有效诱导锂离子进入功能层内部沉积,抑制负极界面锂枝晶的形成,因此电化学装置具有更优的循环寿命和安全性能;实施例4和实施例6的比较也可以得出相同结论;2. Compared with Example 1 and 3, the battery of Example 3 has a larger number of cycles and a smaller volume expansion. When the content of the lithium wetting material is gradually decreased in the stacking direction, the cycle life of the electrochemical device is affected. The improvement of safety performance and safety performance is better, because the higher content of lithium wetting material in the region near the current collector can more effectively induce lithium ions to enter the functional layer to deposit, inhibit the formation of lithium dendrites at the negative electrode interface, so the electrochemical device It has better cycle life and safety performance; the same conclusion can also be drawn from the comparison of Example 4 and Example 6;
3、实施例9与实施例11相比,实施例11的电池表现出更小的体积膨胀率,电化学装置的安全性能更优异,原因在于:锂润湿材料分布在导电层,因此,功能层的第一边缘层和/或第二边缘层为介电层时,锂离子更倾向于在内部的导电层进行沉积,从而抑制负极界面锂枝的形成,提高电化学装置安全性能;3. Compared with Example 11, the battery of Example 9 shows a smaller volume expansion rate, and the safety performance of the electrochemical device is better. The reason is that the lithium wetting material is distributed in the conductive layer, so the functional When the first edge layer and/or the second edge layer of the layer is a dielectric layer, lithium ions are more inclined to be deposited in the inner conductive layer, thereby inhibiting the formation of lithium branches at the negative electrode interface and improving the safety performance of the electrochemical device;
4、实施例9和实施例10相比,实施例9的电池具有更优的循环寿命和安全性能,原因在于,当功能层最靠近负极界面的一层为介电层时,介电层能够有效抑制界面锂枝晶的形成;4. Compared with Example 9 and Example 10, the battery of Example 9 has better cycle life and safety performance. The reason is that when the layer of the functional layer closest to the negative electrode interface is a dielectric layer, the dielectric layer can Effectively inhibit the formation of interfacial lithium dendrites;
5、实施例18与实施例15相比,实施例18所得电池的循环圈数明显比实施例15大,这是因为在负极极片的功能层中包括锂金属时,锂金属能够补充循环过程中损耗的锂,因此,能够显著提升电化学装置的循环寿命;5. Compared with Example 15, the cycle number of the battery obtained in Example 18 is significantly larger than that in Example 15. This is because when lithium metal is included in the functional layer of the negative pole piece, lithium metal can supplement the cycle process. Therefore, the cycle life of electrochemical devices can be significantly improved;
6、实施例19与其余实施例相比,实施例19所得电池的循环圈数小、体积膨胀率大,体现出电池的循环性能和安全性能更差,这是因为,其余实施例中功能层的层叠方向与集流体的延展方向垂直,介电层能够更有效降低功能层的电子浓度和抑制负极界面锂枝晶的形成,从而对电化学装置的循环寿命和安全性能的改善更有效;6. Compared with the other examples, Example 19 shows that the battery obtained in Example 19 has a small number of cycles and a large volume expansion rate, which shows that the cycle performance and safety performance of the battery are worse. This is because the functional layer in the other examples is The stacking direction is perpendicular to the extension direction of the current collector, and the dielectric layer can more effectively reduce the electron concentration of the functional layer and inhibit the formation of lithium dendrites at the anode interface, thereby improving the cycle life and safety performance of the electrochemical device.
7、实施例16、实施例17与实施例13相比,实施例16和实施例17的循环性能和安全性能都比实施例13要差,原因在于:锂润湿材料含量过高(实施例17),功能层的结构稳定性降低,不利于电化学装置循环寿命和安全性能的改善,电化学装置的能量密度也会受影响;锂润湿含量过低(实施例16),对锂金属的诱导能力有限,电化学装置的循环寿命和安全性能改善有限,因此,控制锂润湿材料的质量为功能层质量的30%至60%时,更有利于提高电化学装置的循环寿命和安全性能;7. Compared with Example 13, Example 16 and Example 17 have worse cycle performance and safety performance than Example 13, because the content of lithium wetting material is too high (Example 13). 17), the structural stability of the functional layer is reduced, which is not conducive to the improvement of the cycle life and safety performance of the electrochemical device, and the energy density of the electrochemical device will also be affected; Therefore, when the quality of the lithium-wetting material is controlled to be 30% to 60% of the quality of the functional layer, it is more beneficial to improve the cycle life and safety of electrochemical devices. performance;
8、实施例20与实施例13相比,实施例20所得电化学装置的循环性能和安全性能都较差,其原因在于,功能层的孔隙率较低,锂无法顺畅进入功能层内部进行沉积,因此锂倾向于沉积在负极界面,容易形成界面锂枝晶,不利于电化学装置的循环性能和安全性能。8. Compared with Example 13, Example 20 has poor cycle performance and safety performance of the electrochemical device obtained in Example 20. The reason is that the porosity of the functional layer is low, and lithium cannot smoothly enter the functional layer for deposition. Therefore, lithium tends to be deposited on the negative electrode interface, and it is easy to form interfacial lithium dendrites, which is not conducive to the cycle performance and safety performance of electrochemical devices.
最后应说明的是:以上各实施例仅用以说明本申请的技术方案,而非对其限制;尽管参照前述各实施例对本申请进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本申请各实施例技术方案的范围。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present application, but not to limit them; although the present application has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: The technical solutions described in the foregoing embodiments can still be modified, or some or all of the technical features thereof can be equivalently replaced; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the technical solutions of the embodiments of the present application. scope.

Claims (11)

  1. 一种负极极片,其中,所述负极极片包括功能层;所述功能层包括层叠设置的M个导电层和N个介电层,所述导电层中包括锂润湿材料;A negative pole piece, wherein the negative pole piece comprises a functional layer; the functional layer comprises M conductive layers and N dielectric layers arranged in layers, and the conductive layers comprise a lithium wetting material;
    其中,M≥1,N≥1。Among them, M≥1, N≥1.
  2. 根据权利要求1所述的负极极片,其中,所述锂润湿材料的含量在层叠方向上梯度分布。The negative electrode sheet according to claim 1, wherein the content of the lithium wetting material is distributed in a gradient in the stacking direction.
  3. 根据权利要求1或2所述的负极极片,其中,所述负极极片还包括锂金属层或集流体,所述功能层设置在所述锂金属层的功能表面或集流体的功能表面且所述锂金属层的延伸方向或集流体的延伸方向与所述层叠方向垂直;The negative pole piece according to claim 1 or 2, wherein the negative pole piece further comprises a lithium metal layer or a current collector, the functional layer is provided on the functional surface of the lithium metal layer or the functional surface of the current collector and The extending direction of the lithium metal layer or the extending direction of the current collector is perpendicular to the stacking direction;
    所述锂润湿材料的含量在远离所述锂金属层或集流体的方向上梯度递减。The content of the lithium wetting material is gradually decreasing in a direction away from the lithium metal layer or current collector.
  4. 根据权利要求1-3任一项所述的负极极片,其中,所述M个导电层和N个介电层交错层叠设置。The negative pole piece according to any one of claims 1-3, wherein the M conductive layers and the N dielectric layers are alternately stacked.
  5. 根据权利要求1-4任一项所述的负极极片,其中,所述功能层的第一边缘层和/或第二边缘层为介电层。The negative pole piece according to any one of claims 1-4, wherein the first edge layer and/or the second edge layer of the functional layer is a dielectric layer.
  6. 根据权利要求1所述的负极极片,其中,所述导电层的电导率为10 -7至10 6S/cm,和/或, The negative pole piece according to claim 1, wherein the electrical conductivity of the conductive layer is 10 -7 to 10 6 S/cm, and/or,
    所述介电层的电导率小于10 -8S/cm。 The electrical conductivity of the dielectric layer is less than 10 -8 S/cm.
  7. 根据权利要求1-6任一项所述的负极极片,其中,所述功能层的孔隙率为5%至90%,可选为50%至90%。The negative pole piece according to any one of claims 1-6, wherein the porosity of the functional layer is 5% to 90%, optionally 50% to 90%.
  8. 根据权利要求1-7任一项所述的负极极片,其中,所述锂润湿材料的质量为所述功能层质量的5%至95%,可选为30%至60%。The negative pole piece according to any one of claims 1-7, wherein the mass of the lithium wetting material is 5% to 95% of the mass of the functional layer, and optionally 30% to 60%.
  9. 根据权利要求1-8任一项所述的负极极片,其中,所述功能层还包括锂金属,所述锂金属在所述功能层中的含量为0.25mg/cm 2至25mg/cm 2The negative pole piece according to any one of claims 1-8, wherein the functional layer further comprises lithium metal, and the content of the lithium metal in the functional layer is 0.25 mg/cm 2 to 25 mg/cm 2 .
  10. 一种电化学装置,其中,所述电化学装置包括权利要求1-9任一项所述的负极极片。An electrochemical device, wherein the electrochemical device comprises the negative electrode plate of any one of claims 1-9.
  11. 一种电子装置,其中,所述电子装置的驱动源或能量存储单元为权利要求10所述的电化学装置。An electronic device, wherein the driving source or energy storage unit of the electronic device is the electrochemical device of claim 10 .
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