阅读说明：本技术 金属锂带的表面保护方法、其产品和应用以及设备 (Method for protecting the surface of a lithium metal strip, product and use thereof and device ) 是由 孔德钰 郇庆娜 孙兆勇 陈强 牟瀚波 于 2021-06-25 设计创作，主要内容包括：本发明提供了一种金属锂带的表面保护方法、其产品和应用以及设备,所述方法在喷淋装置中用具有特定组成的喷淋溶液对以特定走带速率的金属锂带的表面进行喷淋,然后在干燥装置中对喷淋后的金属锂带进行干燥,从而获得具有表面保护层的金属锂带。利用本发明的方法,表面保护处理后的金属锂带在大气和电池中均具有优异的化学稳定性,特别是具有锂离子选择性的表面保护层可显著减少金属锂表面的副反应,延长金属锂负极的循环寿命。该表面保护方法为工业化流程,整个过程不产生三废(废水、废气、废渣)污染。(The invention provides a surface protection method of a lithium metal strip, a product, application and equipment thereof. By utilizing the method, the metal lithium belt after surface protection treatment has excellent chemical stability in the atmosphere and in the battery, particularly, the surface protection layer with lithium ion selectivity can obviously reduce the side reaction on the surface of the metal lithium and prolong the cycle life of the metal lithium cathode. The surface protection method is an industrialized process, and the whole process does not produce three-waste (waste water, waste gas and waste residue) pollution.)

1. A surface protection method for a lithium metal strip, the method comprising spraying a surface of the lithium metal strip with a spray solution in a spraying device, and then drying the sprayed lithium metal strip in a drying device, thereby obtaining a lithium metal strip having a surface protection layer, wherein:

the lithium metal strip passes through the spraying device at a belt speed of 5cm/s to 20cm/s, and

the spray solution is a mixed solution containing an organic solute and an inorganic solute in an inert organic solvent, wherein the organic solute is selected from perfluorinated C_1-10An alkylsulfonic acid polymer and at least one of the group consisting of modified polymers thereof, the inorganic solute being at least one selected from the group consisting of an inorganic acid, a metal salt of an oxoacid ion, a metal nitride, a metal fluoride, a metal chloride and a metal sulfide, and the concentration of the organic solute in the spray solution being 0.01 to 1mol/L andthe concentration of the inorganic solute is 0.04mol/L to 1 mol/L.

2. The method of claim 1, further comprising subjecting the lithium metal strip to a surface pre-treatment selected from at least one of purging, cutting, leveling, surface polishing, and degreasing prior to entering the spray device; and optionally rolling the metallic lithium ribbon with the surface protection layer after drying.

3. The surface protection method for metallic lithium tape according to claim 1, wherein the inert organic solvent is one or more selected from the group consisting of C4-C10 alkane, tetrahydrofuran, liquid paraffin, benzene, toluene, p-xylene, naphthalene, and C4-C10 cycloalkane.

4. The method of claim 1, wherein the perfluorinated C is_1-10Alkyl sulfonic acid polymers or perfluorinated C_1-10The modified polymer of the alkyl sulfonate polymer is a modified polymer obtained by modifying with one or more selected from the group consisting of PVDF, PEO, PVDF-HFP, PVA, PTFE, PE, PFR, PS, PSSA, PPO and polysilane.

5. The surface protection method for lithium metal tape according to claim 1, wherein the drying is performed at a temperature of 50 ℃ to 180 ℃.

6. A lithium metal strip with a surface protection layer obtained by the surface protection method for a lithium metal strip according to any one of claims 1 to 5, preferably the thickness of the lithium metal strip is 1 to 100 micrometers and the thickness of the surface protection layer is 1 to 20 micrometers.

7. Use of a lithium metal ribbon according to claim 6 for battery systems, wherein the lithium metal ribbon with a surface protection layer is used as a lithium metal negative electrode.

8. The use according to claim 7, wherein the battery system is one or more of a lithium ion battery, a lithium sulfur battery, a lithium oxygen battery, a quasi-solid state battery, and an all-solid state battery.

9. An apparatus for carrying out the method for surface protection of lithium metal strips according to any one of claims 1 to 5, comprising a spraying device, a drying device and a conveying device for conveying the lithium metal strips and optionally a winding device, wherein:

the spray device is provided with an inlet and an outlet for a lithium metal strip, a spray head positioned at the upper part of the spray device for spraying the spray solution, and a solution recovery device positioned at the lower part of the spray device for recovering the spray solution, and

the drying device is provided with an inlet and an outlet for receiving the lithium metal strip from the spraying device and a solvent recovery device located at the upper part of the drying device for recovering the evaporated solvent.

10. The apparatus of claim 9, wherein the distance between the spray head and the lithium metal strip is 5-20 cm.

Technical Field

The invention provides a method for protecting the surface of a lithium metal strip, a product obtained by the method and application thereof, and a device for implementing the method.

Background

In the existing lithium battery structure, the most widely used negative electrode material of the lithium battery is graphite. However, with the increase of the requirement of people on the energy density of the battery, the graphite material is overwhelmed, and the metallic lithium negative electrode with high specific energy is an ideal material for replacing the graphite negative electrode. The lithium form in the metal lithium negative electrode comprises metal lithium powder and a metal lithium belt, wherein the metal lithium belt is most commonly used for manufacturing the metal lithium negative electrode because the process of manufacturing the negative electrode pole piece is simple and the matching performance of the metal lithium belt and the existing lithium ion battery production process is good. However, since metallic lithium has high reactivity and causes a large number of side reactions in the atmosphere and in the battery, it is required to protect the surface of the metallic lithium ribbon for large-scale application.

The most widely used protection methods at present include magnetron sputtering, vapor deposition, electrostatic spinning, dip coating, blade coating, dropping and the like. However, the methods of magnetron sputtering, vapor deposition and electrostatic spinning have low treatment efficiency and are not suitable for industrial preparation; the dip coating method has large requirements on the solution, and the concentration and the impurity content of the solution change along with the processing process, so that the precise control is not suitable; after the treatment of the blade coating and dropping method, the uniformity of the surface protective layer is poor.

In addition, to realize large-scale application of the lithium metal negative electrode, it is still necessary to solve the problem of dendritic growth of the lithium metal. When used as a negative electrode in a battery system, a large amount of lithium dendrites may be generated on the surface of the metallic lithium negative electrode due to the non-uniform deposition of lithium ions on the surface of the metallic lithium during cycling of the metallic lithium negative electrode. The presence of lithium dendrites not only consumes active lithium and electrolyte to cause a reduction in battery capacity, but also pierces the separator to cause an internal short circuit of the battery as the lithium dendrites grow, resulting in a safety accident.

Therefore, there is still a need in the art to develop new methods and devices for surface protection of lithium metal ribbons.

Disclosure of Invention

The object of the present invention is to provide a method for surface protection of lithium metal strips, the products obtained by this method and their applications, as well as a device for implementing said method.

To this end, in one aspect, the present invention provides a surface protection method for a lithium metal strip, the method comprising spraying a surface of the lithium metal strip with a spray solution in a spraying device, and then drying the sprayed lithium metal strip in a drying device, thereby obtaining a lithium metal strip having a surface protection layer, wherein:

the lithium metal strip passes through the spraying device at a belt speed of 5cm/s to 20cm/s, and

the spray solution is a mixed solution containing an organic solute and an inorganic solute in an inert organic solvent, wherein the organic solute is selected from perfluorinated C_1-10An alkylsulfonic acid polymer and at least one of the group consisting of modified polymers thereof, the inorganic solute being at least one selected from the group consisting of an inorganic acid, a metal salt of an oxoacid ion, a metal nitride, a metal fluoride, a metal chloride and a metal sulfide, and the concentration of the organic solute being 0.01 to 1mol/L and the concentration of the inorganic solute being 0.04 to 1mol/L in the spray solution.

In some preferred embodiments, the method further comprises subjecting the lithium metal strip to a surface pretreatment selected from at least one of purging, cutting, leveling, surface polishing, and degreasing prior to entering the spray device; and optionally rolling the metallic lithium ribbon with the surface protection layer after drying.

In some preferred embodiments, the inert organic solvent is one or more selected from the group consisting of C4-C10 alkanes, tetrahydrofuran, liquid paraffin, benzene, toluene, p-xylene, naphthalene, and C4-C10 cycloalkanes.

In some preferred embodiments, the perfluorinated C_1-10The modified polymer of the alkyl sulfonic acid polymer is modified by one or more selected from PVDF, PEO PVDF-HFP, PVA, PTFE, PE, PFR, PS, PSSA, PPO and polysilane through grafting, blending, blocking and/or polymerizationA compound (I) is provided.

In some preferred embodiments, the drying is carried out at a temperature of from 50 ℃ to 180 ℃.

In another aspect, the present invention provides a lithium metal strip having a surface protective layer obtained by the above surface protection method for a lithium metal strip, preferably, the lithium metal strip has a thickness of 1 to 100 micrometers and the surface protective layer has a thickness of 1 to 20 micrometers.

In some preferred embodiments, the lithium metal tape with a surface protection layer is used as a lithium metal negative electrode in a battery system.

In some preferred embodiments, the battery system is one or more of a lithium ion battery, a lithium sulfur battery, a lithium oxygen battery, a quasi-solid state battery, and an all-solid state battery.

In another aspect, the present invention provides an apparatus for implementing the above surface protection method for a lithium metal strip, the apparatus comprising a spraying device, a drying device, and a conveying device for conveying the lithium metal strip, and optionally a winding device, wherein:

the spray device is provided with an inlet and an outlet for a lithium metal strip, a spray head positioned at the upper part of the spray device for spraying the spray solution, and a solution recovery device positioned at the lower part of the spray device for recovering the spray solution, and

the drying device is provided with an inlet and an outlet for receiving the lithium metal strip from the spraying device and a solvent recovery device located at the upper part of the drying device for recovering the evaporated solvent.

In some preferred embodiments, the distance between the spray head and the lithium metal strip is 5-20 cm.

The present invention can form a uniform surface protection layer on a lithium metal strip by using a spray solution having a specific composition (i.e., a mixed solution having a specific organic solute and an inorganic solute) in combination with a specific tape speed and a specific spray solution concentration. The surface protection layer has organic-inorganic synergistic effects, wherein an inorganic phase provides mechanical strength for the metal lithium band to prevent the growth of lithium dendrites, and simultaneously an organic phase provides elastic deformation capacity and repair capacity for the metal lithium band, so that the integrity of the surface protection layer is maintained in a circulation process when the surface protection layer is applied to a battery, the side reaction of the metal lithium band serving as a metal lithium cathode and electrolyte can be obviously reduced, and the circulation life of the metal lithium cathode is prolonged.

In addition, through the combination of a specific tape transport rate and a specific spray solution concentration, the spray amount on the lithium metal tape can be accurately controlled, so that a surface protection layer with a required thickness can be obtained as required.

In addition, the spraying width can be further controlled by adjusting the distance between a spray head or a nozzle of the spraying device and the metal lithium strip, and the application range of the method is widened.

In addition, the method can realize industrial continuous production and has high treatment efficiency.

Drawings

Fig. 1 shows a schematic flow diagram of a surface protection method according to the present invention, wherein 1 denotes a lithium metal strip, 2 denotes a spray device, 3 denotes a drying device, a lithium metal strip transport system (including an unwinding roll 41, height-adjustable press rolls 42, 43, a back-up roll 44, a winding roll 45), 5 denotes a spray head, and 6 denotes a sprayed spray solution.

Fig. 2 shows graphs of cycle voltage and cycle time for applying metallic lithium tapes obtained according to example 1, comparative example 1 and comparative example 4 of the present invention as lithium negative electrodes to batteries, respectively.

Detailed Description

The present inventors have conducted intensive and extensive studies to overcome one or more or even all of the drawbacks of the prior surface protection methods of metallic lithium while inhibiting the growth of lithium dendrites, and have unexpectedly discovered a new method for surface protection of metallic lithium tapes.

In view of the above, the surface protection method for the lithium metal strip provided by the invention includes spraying the surface of the lithium metal strip with a spraying solution in a spraying device, and then drying the sprayed lithium metal strip in a drying device, thereby obtaining the lithium metal strip with the surface protection layer.

In the present invention, the spray solution used is a mixed solution containing both an organic solute and an inorganic solute in an inert organic solvent. In the present invention, in the spray solution, the concentration of the organic solute is 0.01mol/100ml to 1mol/100ml, and the concentration of the inorganic solute is 0.04mol/ml to 1 mol/ml. Meanwhile, the metal lithium belt is sprayed by a spraying device at a belt speed of 5cm/s to 20 cm/s.

The present inventors have found that by using a mixed solution of an organic solute and an inorganic solute having the above-mentioned specific concentrations in combination with the above-mentioned specific transport rate, a uniform surface protection layer can be formed on a metallic lithium ribbon by the method of the present invention. Moreover, such a surface protective layer has an organic-inorganic synergistic effect. Without being bound by any theory, it is believed that the inorganic phase formed by the inorganic solute therein is capable of providing mechanical strength to the metallic lithium band while preventing the growth of lithium dendrites; meanwhile, the organic phase formed by the organic solute can provide elastic deformation capacity and repair capacity for the metal lithium strip, so that the integrity of the surface protection layer can be maintained in the battery cycling process. Further, by the synergistic effect of the inorganic phase and the organic phase, not only the side reaction of the metal lithium band as the metal lithium negative electrode with the electrolyte can be significantly reduced, but also the cycle life of the metal lithium negative electrode can be extended. On the contrary, the present inventors have also found that, on the one hand, when the spray solution used does not contain the above-mentioned organic solute or inorganic solute, the above-mentioned synergistic effect cannot be obtained; on the other hand, when the transport rate of the lithium metal strip and/or the concentration of the spray solution (including the concentrations of both organic and inorganic solutes) are not within the above-mentioned ranges, either a uniform surface protective layer cannot be formed, or the formed protective layer cannot inhibit the growth of lithium dendrites, and/or the integrity of the protective layer cannot be maintained during battery cycling, and accordingly the desired synergy cannot be achieved.

In the method of the present invention, preferably, the method further comprises subjecting the lithium metal strip to a surface pretreatment selected from at least one of purging, cutting, leveling, surface polishing, and degreasing before entering the spraying device. As known to those skilled in the art, such a pretreatment enables a better formation of a uniform surface layer, and accordingly the above-described synergistic effect can be further enhanced.

In the method of the present invention, it is preferable that the method further comprises rolling the metallic lithium strip having the surface protective layer after drying, so as to be stored for later use.

In the present invention, the spraying device used may be a spraying device known in the art with a nozzle or a spray head capable of spraying a solution. Preferably, the spraying device used in the method of the present invention is provided with an inlet for the strip of lithium metal to be sprayed, an outlet for the strip of lithium metal after being sprayed, a spray head for spraying (or spraying) the spray solution located at an upper portion of the spraying device, and a solution recovery device located at a lower portion of the spraying device for recovering the spray solution. By using the spraying device, the pollution of three wastes (waste water, waste gas and waste residue) can be avoided, and the recovered spraying solution can be reused.

In the present invention, the spray solution for spraying may be supplied from an external storage device such as a tank to the spray nozzle or the head, and the pumping, spraying operation may be performed at normal temperature and pressure or with the aid of a booster pump. Preferably, nozzles or nozzle orifices are used having a diameter or gap size in the range of 100 microns to 2 millimeters; the booster pump used may provide pressures in the range of 0.01MPa to 1 MPa. More preferably, the sprayed solution is subjected to screen filtration before entering the spray head or nozzle, further preferably, the number of screens used is 200 to 1000 mesh, even more preferably 400 to 600 mesh.

In the present invention, the drying device used may be a drying device known in the art, which may be heated with its own heat source or by means of an external heat source. Preferably, the drying device used in the method of the present invention is provided with an inlet for receiving the lithium metal strip from the spray device, an outlet for the dried lithium metal strip, and a solvent recovery device, such as a vapor condensing device and a recovery tank, for recovering the evaporated solvent, located at an upper portion of the drying device. Similarly, such a drying apparatus can further ensure that no three-waste (waste water, waste gas, waste residue) pollution is generated, and the recovered solvent can be reused.

In the present invention, preferably, the drying may be carried out at a temperature of 50 ℃ to 180 ℃ depending mainly on the kind of the inert solvent used and the boiling point thereof.

In the present invention, there is no particular requirement for the inert organic solvent as long as it does not react with the metallic lithium ribbon. From the viewpoint of easy spraying and solubility to the aforementioned organic and inorganic solutes, preferably, the inert organic solvent used may be one or more selected from the group consisting of C4-C10 alkane, tetrahydrofuran, liquid paraffin, benzene, toluene, p-xylene, naphthalene, C4-C10 cycloalkane, and the like.

In the present invention, the organic solute used is selected from perfluorinated C_1-10At least one of the group consisting of alkyl sulfonic acid polymers and modified polymers thereof. Examples include, but are not limited to, perfluoro 1-butanesulfonic acid polymer, perfluoro hexanesulfonic acid polymer, perfluoro 1-butanesulfonic acid polymer, and the like.

In the present invention, preferably, perfluorinated C is used_1-10The alkylsulfonic acid polymer being a non-conductive polymer and being perfluorinated C_1-10The modified polymer of the alkylsulfonic acid polymer is a modified polymer obtained by modifying one or more selected from the group consisting of polyvinylidene fluoride (PVDF), polyethylene oxide (PEO), polyvinylidene fluoride-hexafluoropropylene (PVDF-HFP), polyvinyl alcohol (PVA), Polytetrafluoroethylene (PTFE), Polyethylene (PE), phenol resin (PFR), Polystyrene (PS), sulfonated Polystyrene (PSSA), polypropylene oxide (PPO), and polysilane. Such modification may be accomplished, for example, by grafting, blending, blocking, and/or polymerization, as is well known to those skilled in the art. Further, as such a polymer of an organic solute or a modified polymer thereof, it can be prepared by a conventional method, and also commercially available from, for example, Asahi chemical company, Dow company or Merck group, more specifically, such an organic polymer can be, for example, under the trade name "Nafion" polymer (which is a series of commercial polymers having different compositions).

In the present invention, the inorganic solute used is at least one selected from the group consisting of inorganic acids, metal salts containing an oxyacid ion, metal nitrides, metal fluorides, metal chlorides, and metal sulfides. Examples of the inorganic acid include phosphoric acid, phosphorous acid, polyphosphoric acid, hydrofluoric acid, nitric acid, nitrous acid, oxalic acid, and hydrochloric acid; as the metal salt containing an oxygen acid ion, for example, metal salts of the aforementioned inorganic acids with alkali metals or alkaline earth metals, such as zinc sulfate and the like; as the metal nitride, for example, aluminum nitride, potassium nitride, or the like; examples of the metal fluoride or metal chloride include magnesium fluoride, copper fluoride, zinc chloride, and copper chloride; as the metal sulfide, for example, lithium sulfide, copper sulfide, or the like can be used. As known to those skilled in the art, such inorganic solvents applicants have found that when such inorganic solutes are dissolved or dispersed in an inert organic solvent at a specific concentration with the aforementioned organic solutes, a desired uniform surface protection layer can be formed on the metallic lithium ribbon without causing damage or corrosive effects to the surface of the metallic lithium ribbon in combination with an appropriate take-off rate.

The present invention also provides a lithium metal strip having a surface protective layer obtained by the above surface protection method for a lithium metal strip. Preferably, the metallic lithium ribbon is a super-wave lithium ribbon having a thickness of 1-100 microns. More preferably, the surface protection layer formed on the lithium metal strip may have a thickness of 1 to 20 μm. The thickness of the protective layer is less than 1 micron, the requirement on the performance of equipment is extremely high, and the organic phase and the inorganic phase of the prepared surface protective layer are easily separated, so that the organic and inorganic synergistic effect is lost; when the thickness of the surface protection layer is larger than 20 micrometers, the power performance of the prepared pole piece is also influenced by a longer transmission path, and the overall energy density of the metal lithium negative electrode is reduced due to the larger thickness of the surface protection layer. Therefore, the optimal surface protective layer thickness is 1-20 microns.

The metallic lithium ribbon with a surface protection layer obtained by the method of the present invention can be used as a metallic lithium negative electrode in a battery system. Preferably, the battery system that can be applied is one or more of a lithium ion battery, a lithium sulfur battery, a lithium oxygen battery, a quasi-solid state battery, and an all-solid state battery.

The invention also provides equipment for implementing the surface protection method for the metallic lithium strip, which comprises a spraying device, a drying device and a conveying device for conveying the metallic lithium strip and an optional rolling device, wherein the spraying device is provided with an inlet and an outlet for the metallic lithium strip, a spray head positioned at the upper part of the spraying device for spraying the spraying solution and a solution recovery device positioned at the lower part of the spraying device for recovering the spraying solution, and the drying device is provided with an inlet and an outlet for receiving the metallic lithium strip from the spraying device and a solvent recovery device positioned at the upper part of the drying device for recovering the evaporated solvent. For those skilled in the art, such a device can be easily designed and assembled by themselves, or assembled after being purchased (e.g., commercially available from shenzhen xinjia automation technology limited, nonsin pioneer smart equipment limited, shenzhen kojizhida technology limited) for each sub-device.

In the invention, the distance between the spray head of the spraying device and the metal lithium belt is preferably 5-20 cm. By means of the distance setting, the spraying width of the spraying solution can be controlled more accurately according to needs, the atomizing effect of the nozzle is correspondingly improved, the surface of the metal lithium strip is ensured to be in uniform contact with the spraying solution, and the formation of a required uniform surface protection layer is facilitated.

More specifically, first, a lithium metal strip to be surface-protected enters a spraying device at a certain strip speed by means of a conveying system such as a conveyor belt (including but not limited to an unwinding roll, one or more height-adjustable pressure rolls, one or more support rolls, and a winding roll). In the spraying device, a spraying solution with a specific composition is sprayed or misted on the metal lithium strip through a nozzle or a spray head positioned at the upper part of the spraying device; and a solution recovery device for recovering the spray solution is arranged at the lower part of the spray device, so that the recovered spray solution can be reused or can be prepared again according to the needs and then be reused. The sprayed lithium metal strip is driven by the conveying system to come out of the spraying device and enter the drying device. Drying the lithium metal strip at a temperature in a drying device, wherein a solvent in the spray solution is evaporated, thereby forming a protective layer of a certain thickness on the surface of the lithium metal strip; meanwhile, the evaporated solvent is recovered via a solvent recovery device of the drying device, such as a condensing device (not shown). After drying, the metallic lithium strip with the surface protective layer comes out of the drying device, is cooled as required, and is rolled for storage and standby.

For a better understanding of the technical features, objects, and advantages of the present invention, reference will now be made to the following drawings and examples, in which the present invention is illustrated in further detail. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.

Equipment assembling: fig. 1 shows an exemplary flow diagram for carrying out the method for surface protection according to the invention. As shown in fig. 1, the lithium metal strip 1 is unwound from an unwinding roller 41 and then enters a spraying device 2.

The spraying device 2 consists of an integrated top cover two-fluid atomizer (pilot drying equipment limited company in Changzhou city), height-adjustable press rollers 42 and 43, a gas recovery device and a semi-closed shell. The integrated top cover two-fluid atomizer is fixed on the top of the spraying device 2, the pressure roller 42 and the pressure roller 43 are adjusted, the distance between the control nozzle or the spray head 5 and the vertex connecting surface of the pressure roller 42 and the pressure roller 43 is 5-20cm, and a plurality of air outlets on the wall of the spraying device are connected with an air recovery device (not shown) (Nantong Keyuan electrical equipment Co., Ltd.). Wherein the two-fluid atomizer is connected with the spray solution 6 and the atomizing gas (atmospheric air, compressed air or compressed argon). And metal lithium belt inlets and outlets are reserved on two sides of the semi-closed shell, and the metal lithium belts enter and leave the spraying device during spraying.

The lithium metal strip coming out of the spraying device 2 passes through the supporting roller 44 and enters the drying device 3.

The drying device is composed of an external temperature control system, a gas recovery device and a semi-closed shell. An external temperature control system is arranged outside the semi-closed shell, and a metal lithium belt inlet and a metal lithium belt outlet are reserved in the semi-closed shell. The external temperature control system can ensure that the internal temperature of the drying device is maintained at any temperature within the range of 50 ℃ to 180 ℃, and the temperature fluctuation is +/-5 ℃. The wall of the drying device is provided with a plurality of air outlets connected with the gas recovery device.

The spraying device 2 and the drying device 3 can share one gas recovery device.

Spray solution preparation

Preparation example 1

At room temperature, a beaker was charged with 30g of perfluoro 1-butanesulfonic acid polymer (Nafion polymer available from Merck group) and 16.1g of zinc sulfate (Chinese medicine), mechanically stirred for 24 hours using an additional small mechanical stirring device (CJMS-1000 laboratory stirrer, Shanghai Chengtian electromechanical devices Co., Ltd.), and the above substances were uniformly dispersed in 1000ml of tetrahydrofuran solvent (alatin) to obtain a spray solution having an organic solute concentration of 0.1mol/L and an inorganic solute concentration of 0.1 mol/L.

Preparation example 2

By changing only the organic solute to perfluorohexanesulfonic acid polymer (another Nafion polymer available from Merck group) and the rest of the conditions as in preparation example 1, a spray solution with an organic solute concentration of 0.075mol/L and an inorganic solute concentration of 0.1mol/L was obtained.

Preparation example 3

The spraying solution with the organic solute concentration of 0.1mol/L and the inorganic solute concentration of 0.37mol/L is obtained by changing the inorganic solute to be aluminum nitride (Chinese traditional medicine) and other conditions to be the preparation example 1.

Preparation example 4

Only by changing the mass of the perfluoro 1-butanesulfonic acid polymer (Nafion polymer available from Merck group) to 150g and the other conditions as in preparation example 1, a spray solution having an organic solute concentration of 0.5mol/L and an inorganic solute concentration of 0.1mol/L was obtained.

Preparation example 5

Spray solution with organic solute concentration of 0.1mol/L and inorganic solute concentration of 0.1mol/L was obtained by changing only the solvent to p-xylene (alatin) and the other conditions as in preparation example 1.

Preparation example 6

Using a perfluorosulfonic acid-polytetrafluoroethylene copolymer (a Nafion-modified polymer available from Dow, USA) and the rest of the conditions as in preparation example 1, a spray solution having an organic solute concentration of 0.16mol/L and an inorganic solute concentration of 0.1mol/L was obtained.

Comparative preparation example 1

0.3g of perfluoro-1-butanesulfonic acid polymer (Nafion polymer purchased from merck group) and 16.1g of zinc sulfate (Chinese medicine) are respectively weighed according to the mass, and the materials are uniformly dispersed in 1000ml of tetrahydrofuran solvent (alatin) by mechanical stirring for 24 hours at room temperature to obtain a spraying solution with the concentration of organic solute of 0.001mol/L and the concentration of inorganic solute of 0.1 mol/L.

Comparative preparation example 2

30g of perfluoro-1-butanesulfonic acid polymer (Nafion polymer purchased from merck group) and 1.61g of zinc sulfate (Chinese medicine) are respectively weighed according to the mass, and the materials are uniformly dispersed in 1000ml of tetrahydrofuran solvent (avadin) by mechanical stirring for 24 hours at room temperature to obtain a spraying solution with the concentration of organic solute of 0.1mol/L and the concentration of inorganic solute of 0.01 mol/L.

Comparative preparation example 3

0.3g of perfluoro-1-butanesulfonic acid polymer (Nafion polymer purchased from merck group) and 1.36g of zinc sulfate (Chinese medicine) are respectively weighed according to the mass, and the materials are uniformly dispersed in 1000ml of tetrahydrofuran solvent (alatin) by mechanical stirring for 24 hours at room temperature to obtain a spraying solution with the concentration of organic solute of 0.001mol/L and the concentration of inorganic solute of 0.01 mol/L.

Example 1

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 micrometers is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of a spraying solution is as described in preparation example 1. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 10cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a rolling roller to obtain the metal lithium belt with the surface protection layer thickness of 6 microns.

Example 2

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 micrometers is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of a spraying solution is as described in preparation example 1. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 5cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a winding roller to obtain the metal lithium belt with the surface protection layer thickness of 18 microns.

Example 3

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 micrometers is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of a spraying solution is as described in preparation example 1. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 20cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a winding roller to obtain the metal lithium belt with the surface protective layer thickness of 1 micron.

Example 4

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 micrometers is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of a spraying solution is as described in preparation example 4. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 10cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a winding roller to obtain the metal lithium belt with the surface protective layer of 10 microns.

Example 5

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 micrometers is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of the spraying solution is as described in preparation example 5. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 10cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a rolling roller to obtain the metal lithium belt with the surface protection layer thickness of 6 microns.

Comparative example 1

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 microns is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of the spraying solution is as described in comparative preparation example 1. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 10cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a rolling roller to obtain the metal lithium belt with the surface protective layer thickness of 2 microns.

Comparative example 2

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 microns is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of the spraying solution is as described in comparative preparation example 2. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 10cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a winding roller to obtain the metal lithium belt with the surface protective layer of 3 microns.

Comparative example 3

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 microns is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of the spraying solution is as described in comparative preparation example 3. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 10cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a winding roller to obtain the metal lithium belt with the surface protective layer thickness of 1 micron.

Comparative example 4

According to the flow shown in fig. 1, a metal lithium belt with a thickness of 50 micrometers is unreeled, subjected to inert gas purging and corona pretreatment, and then enters a spraying device, and the preparation process of a spraying solution is as described in preparation example 1. The distance between the nozzle and the metal lithium belt is controlled to be 10cm, the belt travelling speed of the metal lithium belt is controlled to be 30cm/s, and the spraying amount is controlled to be 3 ml/s. And the sprayed metal lithium belt enters a drying device through a supporting roller. An external temperature control system was set to maintain the internal temperature of the drying apparatus at 55 ℃. And (4) drying the metal lithium belt, and then rolling the metal lithium belt by using a winding roller to obtain the metal lithium belt with the surface protective layer of 3 microns.

Application and Performance testing

The lithium metal tapes obtained in example 1, comparative example 1 and comparative example 4 were used to assemble button cells and to perform performance tests. The method comprises the following specific steps: the lithium metal tapes obtained in example 1, comparative example 1 and comparative example 4 were punched out into a 15mm diameter electrode sheet, and this electrode sheet was used as an electrode and a commercially available lithium sheet was used as a counter electrode. The battery was subjected to charge-discharge cycling under the following conditions: the electrolyte contains 1mol/L LiPF₆And a two-component mixed solvent EC: EMC 1:1 (volume ratio v/v), wherein the diaphragm is a polypropylene film, the test temperature is 25 ℃, and the cycle program is as follows: standing for 12 hours, charging for 1 hour at constant current, discharging for 1 hour at constant current, and circulating current of 1mA/cm²The circulation capacity is 1mAh/cm²。

The voltage and cycle time during the cycle were recorded and plotted, and the results are shown in fig. 2. It is to be noted with respect to this fig. 2 that the graph is a cycle curve for a symmetric cell, the cycle test for which is a means for characterizing the performance of the lithium metal anode after processing. Under the ideal condition, namely when the electrode surface appearance is unchanged, the charge-discharge cycle is carried out on the cycle curve by using a constant potential with 0V as a symmetrical line, but under the actual condition, the electrode appearance is changed, which causes the cycle potential to change, after the electrode of the battery is changed at the later stage of the cycle, the internal resistance of the battery is increased, the overpotential is enlarged, and the electrode is opened in a horn shape. As can be seen from fig. 2, under the same cycling conditions, the overpotential of the battery prepared using the metallic lithium negative electrode of example 1 was the smallest, after 500 hours of cycling, the overpotential of the electrode was less than 0.1V, whereas the overpotentials of the batteries prepared using the metallic lithium negative electrodes of comparative examples 1 and 4 increased faster, and after 450 cycles, the potentials of the batteries both exceeded 0.1V, and the overpotential of the battery prepared using the metallic lithium negative electrode of comparative example 4 was 0.4V, which indicates that the surface structure of the electrode had changed greatly and a large amount of lithium dendrites were generated on the surface. The experimental data show that the surface of the lithium metal negative electrode of the embodiment is effectively protected, and the electrode surface protective layer can effectively inhibit the generation of lithium dendrites and prolong the service life of the electrode in the battery cycle process.

The invention has been described in detail with reference to specific embodiments thereof, but the invention is not limited thereto. Any modification and improvement of the details within the spirit and principle of the invention should be considered within the scope of the invention. The full scope of the invention is given by the appended claims and any equivalents thereof.