WO2020031697A1 - Thermal spray system, thermal spray method and method for producing lithium secondary battery - Google Patents
Thermal spray system, thermal spray method and method for producing lithium secondary battery Download PDFInfo
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- WO2020031697A1 WO2020031697A1 PCT/JP2019/029011 JP2019029011W WO2020031697A1 WO 2020031697 A1 WO2020031697 A1 WO 2020031697A1 JP 2019029011 W JP2019029011 W JP 2019029011W WO 2020031697 A1 WO2020031697 A1 WO 2020031697A1
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- chamber
- lithium
- coating
- thermal spray
- thermal spraying
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C28/00—Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C4/00—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge
- C23C4/12—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge characterised by the method of spraying
- C23C4/123—Spraying molten metal
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C4/00—Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge
- C23C4/18—After-treatment
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
- C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
- C23C8/10—Oxidising
- C23C8/16—Oxidising using oxygen-containing compounds, e.g. water, carbon dioxide
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the following disclosure relates to a thermal spraying system, a thermal spraying method, and a method for manufacturing a lithium secondary battery.
- Patent Document 1 As a method of mass-producing electrochemical cells, an apparatus for film formation of an electrochemical cell including a process chamber configured to form a material on a substrate wound between two reels has been proposed ( Patent Document 1).
- an electrode manufacturing apparatus has been proposed in which an electrode material on an electrode sheet is doped with lithium ions to manufacture an electrode for a lithium ion capacitor (Patent Document 2).
- a lithium-containing powder is melted and sprayed onto an electrode material of an electrode sheet carried into a processing chamber to form a lithium thin film in an inert gas atmosphere.
- spontaneous ignition of lithium or the like is prevented by using an inert gas that does not react with lithium.
- JP 2014-224322 A Japanese Patent No. 6084841
- the present disclosure provides a technique capable of winding a substrate on which a coating is formed without deteriorating the quality of the coating formed by thermal spraying.
- the thermal spraying system includes a thermal spraying unit, a surface treatment unit, and a winding unit.
- the thermal spray portion is configured to form a coating on the first surface of the substrate by thermal spraying the powder material.
- the surface treatment is configured to stabilize the surface of the coating.
- the winding unit is configured to wind the substrate after stabilization of the surface of the coating.
- the substrate on which the coating is formed can be wound without deteriorating the quality of the coating formed by thermal spraying.
- FIG. 1 is a schematic sectional view illustrating an example of the configuration of the thermal spraying system according to the first embodiment.
- FIG. 2 is a schematic perspective view showing an example of the configuration of the thermal spraying system according to the first embodiment.
- FIG. 3 is a flowchart illustrating an example of the flow of the thermal spraying process in the thermal spraying system according to the first embodiment.
- FIG. 4A is a diagram for describing an example of a coating formed by a thermal spray processing unit of the thermal spray system according to the first embodiment.
- FIG. 4B is a diagram illustrating an example of a stabilization layer formed by the surface treatment unit of the thermal spraying system according to the first embodiment.
- FIG. 5 is a table showing experimental results regarding surface treatment conditions according to the first embodiment.
- FIG. 6A is a diagram illustrating a configuration example 1 of the thermal spraying system according to the second embodiment.
- FIG. 6B is a diagram illustrating a configuration example 2 of the thermal spraying system according to the second embodiment.
- FIG. 6C is a diagram illustrating a configuration example 3 of the thermal spraying system according to the second embodiment.
- FIG. 7 is a diagram for explaining a cooling mechanism included in the thermal spraying system according to the third embodiment.
- lithium ions move from the positive electrode to the negative electrode during charging, and lithium ions move from the negative electrode to the positive electrode during discharging.
- a part of lithium ions may react with a metal material (eg, carbon) of the negative electrode and not move to the positive electrode in some cases. In this case, the lithium ions remaining on the negative electrode do not function as a capacity, and the battery capacity cannot be used sufficiently effectively.
- the pre-lithiation technique for improving the capacity efficiency by doping a lithium-based material into a negative electrode or a positive electrode in advance has been studied.
- the prerepetition technique is to improve the charge / discharge efficiency by previously filling the negative electrode or the positive electrode with lithium ions consumed in the early stage of charge / discharge or having lost ion conductivity.
- the thermal spraying system 100 according to the first embodiment described below can be used for pre-repetition, that is, for manufacturing an electrode of a lithium ion secondary battery or the like.
- the thermal spray system 100 according to the first embodiment is configured such that a thermal spray coating can be formed on the substrate W while unwinding and winding the roll-shaped substrate W. Further, the thermal spraying system 100 according to the first embodiment is configured to stabilize the surface of the thermal spray coating formed on the substrate W before winding the substrate W. For this reason, even when the thermal spray coating is made of a highly adhesive material, it is necessary to prevent the thermal spray coating from sticking to the surface of the substrate wound on the thermal spray coating when the substrate W is wound. Can be. Further, the thermal spraying system 100 according to the first embodiment has a differential exhaust mechanism for preventing the material of the thermal spray coating from scattering. Therefore, even when a highly reactive material such as lithium is used, scattering and leakage of the material can be prevented.
- the substrate W to be processed in the thermal spraying system is, for example, an electrode sheet, and an electrode material is formed on the electrode sheet.
- the electrode material is, for example, a carbon material such as activated carbon and graphite.
- the electrode material is formed to have a width of, for example, about 1 to 100 centimeters (cm).
- the substrate W can be transported in a state wound in a roll.
- the substrate W may be a single-sided coated product or a double-sided coated product.
- the surface on one side of the sheet-shaped substrate W is also referred to as a first surface
- the surface on the opposite side to the first surface is also referred to as a second surface.
- the base material W becomes, for example, a negative electrode of a lithium ion secondary battery.
- the negative electrode is formed of, for example, a Si-based material, a SiO-based material, or a mixture of carbon and a Si-based or SiO-based material.
- FIG. 1 is a schematic cross-sectional view showing an example of the configuration of the thermal spraying system 100 according to the first embodiment.
- FIG. 2 is a schematic perspective view illustrating an example of the configuration of the thermal spraying system 100 according to the first embodiment.
- the thermal spraying system 100 shown in FIGS. 1 and 2 includes an unloading-side storage chamber (hereinafter, also referred to as a loader chamber) 1, a thermal spray processing chamber 3, a surface processing chamber 5, and a winding-side storage chamber (hereinafter, an unloader chamber). 7).
- the loader chamber 1, the thermal spray processing chamber 3, the surface processing chamber 5, and the unloader chamber 7 are examples of a first chamber, a second chamber, a third chamber, and a fourth chamber, respectively.
- a first differential exhaust chamber 2 is provided between the loader chamber 1 and the thermal spray processing chamber 3.
- a second differential exhaust chamber 4 is provided between the thermal spray processing chamber 3 and the surface processing chamber 5.
- a third differential exhaust chamber 6 is provided between the surface treatment chamber 5 and the unloader chamber 7.
- a slit S1 is provided between the loader chamber 1 and the first differential exhaust chamber 2 to allow the internal space of the loader chamber 1 and the internal space of the first differential exhaust chamber 2 to communicate with each other.
- a slit S2 is provided between the first differential evacuation chamber 2 and the thermal spray processing chamber 3 for communicating the internal space of the first differential evacuation chamber 2 with the internal space of the thermal spray processing chamber.
- a slit S3 is provided between the thermal spray processing chamber 3 and the second differential exhaust chamber 4 to allow the internal space of the thermal spray processing chamber 3 to communicate with the internal space of the second differential exhaust chamber 4.
- a slit S4 is provided between the differential exhaust chamber 4 and the surface treatment chamber 5 to allow the internal space of the differential exhaust chamber 4 and the internal space of the surface treatment chamber 5 to communicate with each other.
- a slit S5 is provided between the surface processing chamber 5 and the third differential exhaust chamber 6 to allow the internal space of the surface processing chamber 5 to communicate with the internal space of the third differential exhaust chamber 6.
- a slit S6 for communicating the internal space of the third differential exhaust chamber 6 with the internal space of the unloader chamber 7.
- the slits S1 to S6 are formed to transport the substrate W between the respective chambers. Therefore, the slits S1 to S6 are formed on the transport path of the base material W.
- the substrate W is transported from the loader chamber 1 to the unloader chamber 7 through the slits S1 to S6.
- the slits S1 to S6 are formed in a size and shape such that the electrode material or the thermal spray coating formed on the base material W does not contact the walls of the respective chambers where the slits S1 to S6 are formed.
- Each of the slits S1 to S6 has substantially the same size and shape. Further, the slits S1 to S6 are arranged at positions that do not hinder the conveyance of the substrate W. In FIG.
- the transport path of the substrate W is illustrated in a substantially linear shape, but the transport path of the substrate W is not necessarily linear.
- a guide roller may be provided for transporting the substrate W to control the transport path of the substrate W (see FIG. 2).
- the slits S1 to S6 can be arranged at positions corresponding to the transport path of the base material W.
- the loader chamber 1 houses the unwinding section 11 on which the substrate W to be processed is set.
- the unwinding unit 11 is, for example, a roller around which the substrate W to be processed is wound.
- the roller is, for example, a cylindrical unwinding shaft.
- the substrate W wound in a roll around the roller is set.
- the unwinding section 11 can be configured so that the base material W is supported by inserting the center of the roll-shaped base material W into the unwinding shaft.
- the loader chamber 1 is connected to the intake / exhaust section 13 through the intake / exhaust port 12 so that the inside can be maintained at a predetermined atmosphere and pressure.
- the specific configuration of the intake / exhaust section 13 is not particularly limited as long as the inside of the loader chamber 1 can be maintained at a predetermined atmosphere and pressure.
- the intake / exhaust section 13 includes, for example, a gas supply source, a flow controller (for example, a mass flow controller) for adjusting a gas flow rate, an opening / closing valve, and the like.
- the intake / exhaust section 13 is configured to maintain the inside of the loader chamber 1 in an inert gas atmosphere, for example.
- the intake / exhaust section 13 is configured to maintain the inside of the loader chamber 1 in an argon gas atmosphere.
- the thermal spray processing chamber 3 accommodates the thermal spray section 31.
- the thermal spray portion 31 is configured to form a coating on the first surface of the base material W by, for example, thermal spraying of a powder material.
- the thermal spray unit 31 is, for example, a thermal spray gun configured to form a thermal spray coating by plasma thermal spraying.
- the thermal spray section 31 has a supply section for supplying the thermal spray material and various gases (for example, a carrier gas and a purge gas), and a mechanism for generating plasma and melting the thermal spray material by the heat of the plasma.
- the thermal spray unit 31 also has an injection port for injecting the thermal spray jet toward the base material W.
- the injection port of the thermal spray section 31 is disposed inside the thermal spray processing chamber 3 so as to face the transport path of the base material W.
- the injection port is disposed in the room facing the transport path of the base material W, a part or all of the supply unit of the thermal spraying unit 31 and the mechanism for melting the thermal spray material are disposed outside the thermal spray processing chamber 3. May be done.
- the thermal spray processing chamber 3 also has an exhaust port 32.
- the exhaust port 32 is connected to a vacuum pump 33.
- the air in the thermal spray processing chamber 3 is evacuated by the vacuum pump 33 through the exhaust port 32, and the pressure in the thermal spray processing chamber 3 is reduced.
- the surface treatment chamber 5 includes a surface treatment unit 50.
- the surface treatment unit 50 is configured to stabilize the surface of the coating film formed on the first surface of the base material W in the thermal spray processing chamber 3. That is, the surface treatment unit 50 is configured to perform a surface treatment.
- the surface treatment unit 50 includes a gas supply unit 51 and a gas discharge unit 52.
- the gas supply unit 51 supplies a gas for stabilizing the surface of the coating into the surface treatment chamber 5.
- the gas supply unit 51 supplies oxygen (O 2 ), carbon dioxide (CO 2 ), water (H 2 O) and inert gas to the surface treatment chamber 5 at a predetermined partial pressure.
- the gas supply unit 51 need not always supply O 2 , CO 2 , H 2 O, and an inert gas.
- the gas supply unit 51 may supply only one of O 2 and CO 2 .
- the partial pressure of the gas supplied by the gas supply unit 51 is, for example, as follows. O 2 gas: 0 to 760 Torr CO 2 gas: 0 to 760 Torr H 2 O: 0 to 760 Torr Ar gas: 0 to 760 Torr However, the partial pressure of each gas is adjusted according to the thickness of the film on the substrate W.
- the gas exhaust unit 52 exhausts the gas in the surface treatment chamber 5.
- the specific configurations of the gas supply unit 51 and the gas exhaust unit 52 are not particularly limited.
- the surface treatment chamber 5 also has an exhaust port 53.
- the exhaust port 53 is connected to a vacuum pump 54.
- the air in the surface treatment chamber 5 is evacuated by the vacuum pump 54 through the exhaust port 53, and the pressure in the surface treatment chamber 5 is reduced.
- the inside of the surface treatment chamber 5 is controlled to a pressure lower than the atmospheric pressure.
- the unloader chamber 7 houses the winding section 71.
- the winding unit 71 is configured to wind the substrate W after the surface of the coating film formed on the first surface of the substrate W is stabilized.
- the winding unit 71 is, for example, a roller around which the substrate W to be processed is wound.
- the roller is, for example, a cylindrical winding shaft.
- the substrate W that has passed through the thermal spray processing chamber 3 and the surface processing chamber 5 is wound around a roller (the winding section 71).
- the unloader chamber 7 is connected to an intake / exhaust section 73 through an intake / exhaust port 72 so that the inside can be maintained at a predetermined atmosphere and pressure.
- the specific configuration of the intake / exhaust section 73 is not particularly limited as long as the interior of the unloader chamber 7 can be maintained at a predetermined atmosphere and pressure.
- the intake / exhaust section 73 has, for example, a gas supply source, a flow controller (for example, a mass flow controller) for adjusting the flow rate of gas, and an opening / closing valve.
- the intake / exhaust section 73 is configured, for example, to maintain the inside of the unloader chamber 7 in an inert gas atmosphere.
- the suction / exhaust section 73 is configured to maintain the inside of the unloader chamber 7 in an argon gas atmosphere.
- the first differential exhaust chamber 2 functions as a differential exhaust mechanism between the loader chamber 1 and the thermal spray processing chamber 3.
- the first differential exhaust chamber 2 is provided between the loader chamber 1 and the thermal spray processing chamber 3, and is maintained in a higher pressure atmosphere than the thermal spray processing chamber 3.
- the first differential exhaust chamber 2 is connected to a gas supply unit 22 via, for example, an intake port 21. Further, the first differential exhaust chamber 2 is connected to an exhaust unit 24 via, for example, an exhaust port 23.
- the gas supply unit 22 supplies a predetermined gas to the first differential exhaust chamber 2 via the intake port 21. Further, the exhaust unit 24 exhausts the inside of the first differential exhaust chamber 2 through the exhaust port 23.
- the first differential exhaust chamber 2 includes the gas supply unit 22 and the exhaust unit 24, the internal atmosphere of the loader chamber 1 and the internal atmosphere of the thermal spray processing chamber 3 are prevented from flowing. I do.
- the first differential exhaust chamber 2 functions as a separation layer between the loader chamber 1 and the thermal spray processing chamber 3 as it were.
- the first differential exhaust chamber 2 prevents the powder material scattered by thermal spraying in the thermal spray processing chamber 3 from leaking into the loader chamber 1.
- the first differential exhaust chamber 2 only needs to be able to prevent the flow of the internal atmosphere of the loader chamber 1 and the thermal spray processing chamber 3 by differential exhaust and to prevent leakage of the thermal spray material.
- the configuration of the unit 24 and the like is not particularly limited.
- the second differential exhaust chamber 4 functions as a differential exhaust mechanism between the thermal spray processing chamber 3 and the surface processing chamber 5.
- the second differential exhaust chamber 4 is provided between the thermal spray processing chamber 3 and the surface processing chamber 5, and is maintained in a higher pressure atmosphere than the thermal spray processing chamber 3.
- the second differential exhaust chamber 4 is connected to a gas supply unit 42 via, for example, an intake port 41. Further, the second differential exhaust chamber 4 is connected to an exhaust unit 44 via, for example, an exhaust port 43.
- the gas supply unit 42 supplies a predetermined gas to the second differential exhaust chamber 4 via the intake port 41. Further, the exhaust unit 44 exhausts the inside of the second differential exhaust chamber 4 through the exhaust port 43.
- the second differential exhaust chamber 4 includes the gas supply unit 42 and the exhaust unit 44, the internal atmosphere of the thermal spray processing chamber 3 and the internal atmosphere of the surface processing chamber 5 can be circulated. To prevent.
- the second differential exhaust chamber 4 functions as a so-called separation layer between the thermal spray processing chamber 3 and the surface processing chamber 5. Further, the second differential exhaust chamber 4 prevents the powder material scattered by thermal spraying in the thermal spray processing chamber 3 from leaking to the surface processing chamber 5.
- the second differential evacuation chamber 4 only needs to be capable of preventing the flow of the internal atmosphere of the thermal spray processing chamber 3 and the surface processing chamber 5 by differential exhaust and preventing leakage of the thermal spray material.
- the configuration of the exhaust unit 44 and the like is not particularly limited.
- the third differential exhaust chamber 6 functions as a differential exhaust mechanism between the surface treatment chamber 5 and the unloader chamber 7.
- the third differential exhaust chamber 6 is provided between the surface processing chamber 5 and the unloader chamber 7 and is maintained in a higher pressure atmosphere than the surface processing chamber 5.
- the third differential exhaust chamber 6 is connected to a gas supply unit 62 via, for example, an intake port 61. Further, the third differential exhaust chamber 6 is connected to an exhaust unit 64 via, for example, an exhaust port 63.
- the gas supply unit 62 supplies a predetermined gas to the third differential exhaust chamber 6 via the intake port 61. Further, the exhaust part 64 exhausts the inside of the third differential exhaust chamber 6 through the exhaust port 63.
- the third differential exhaust chamber 6 includes the gas supply unit 62 and the exhaust unit 64, the internal atmosphere of the surface treatment chamber 5 and the internal atmosphere of the unloader chamber 7 are prevented from flowing. .
- the third differential exhaust chamber 6 functions as a separation layer between the surface treatment chamber 5 and the unloader chamber 7, so to speak.
- the third differential exhaust chamber 6 only needs to be able to prevent the flow of the internal atmosphere of the surface treatment chamber 5 and the unloader chamber 7 by differential exhaust, and the configurations of the gas supply unit 62 and the exhaust unit 64 are particularly limited. Not done.
- the first differential exhaust chamber 2, the second differential exhaust chamber 4, and the third differential exhaust chamber 6 can be similarly configured.
- the atmosphere in each chamber is preferably an inert gas (eg, argon) atmosphere because the atmosphere does not react with the lithium powder and the surface after the surface treatment can be maintained in an inactive state.
- the thermal spraying system 100 further includes a control device 8.
- the control device 8 includes a control unit 81, an operation unit 82, and a storage unit 83.
- the control unit 81 controls the operation of each unit of the thermal spraying system 100.
- the operation unit 82 receives an input operation of a command for operating the thermal spraying system 100 by an operator, and the like.
- the operation unit 82 is, for example, a keyboard, a display, a touch panel, or the like.
- the storage unit 83 stores a program for controlling the operation of each unit of the thermal spray system 100.
- the control device 8 is, for example, a computer including a CPU (Central Processing Unit) and a memory.
- the storage unit 83 stores programs for controlling various processes executed in the thermal spraying system 100.
- the control unit 81 controls the operation of the thermal spraying system 100 by reading and executing the program stored in the storage unit 83.
- the control unit 81 may be configured to read and execute a program stored in the storage unit 83 to maintain the temperature and humidity in the room where the thermal spraying system 100 is disposed at predetermined values.
- Some thermal spray materials react to temperature and humidity, such as those that ignite when contacted with water. Therefore, the temperature and humidity in the room where the thermal spraying system 100 is arranged may be controlled by the control device 8 in accordance with the characteristics of the thermal spraying material to be used. Further, the flow rate of the gas supplied to and exhausted from each of the chambers 1 to 7 provided in the thermal spray system 100 and the timing of supply and exhaust may be controlled by the control device 8.
- Such a program is recorded on a computer-readable storage medium, and may be installed in the storage unit 83 from the storage medium.
- Examples of the storage medium readable by a computer include a hard disk (HD), a flexible disk (FD), a compact disk (CD), a magneto-optical disk (MO), and a memory card.
- FIG. 2 shows an example of a configuration of the thermal spraying system 100 according to the first embodiment.
- each of the first differential pumping chamber 2, the second differential pumping chamber 4, and the third differential pumping chamber 6 is connected to a vacuum pump on the ceiling side of the chamber, so that the inside of the chamber is internally connected. Pressure is controlled.
- the method for realizing the differential exhaust in each differential exhaust chamber is not particularly limited.
- the base material W is supported by a plurality of guide rollers.
- the guide rollers are arranged horizontally.
- the arrangement position of the guide roller is not limited to this, and the thermal spraying system 100 may be configured to arrange the guide roller in other chambers other than the surface treatment chamber 5 to guide the base material W. As such, the details of the thermal spray system 100 can vary.
- FIG. 3 is a flowchart illustrating an example of the flow of the thermal spraying process in the thermal spraying system 100 according to the first embodiment.
- the thermal spraying process starts under the control of the control device 8.
- the roll-shaped substrate W is carried into the loader room 1 and set on the unwinding section 11 (step S31).
- the atmosphere, temperature, humidity, and the like of each room of the thermal spraying system 100 are controlled.
- the base material W is unwound from the unwinding unit 11, passes through the first differential evacuation chamber 2 through the transport path, and is transported to the thermal spray processing chamber 3.
- the thermal spray section 31 sprays the molten powder material onto the surface of the base material W to form a coating (thermal spray processing, step S32).
- the substrate W on which the coating is formed exits the thermal spray processing chamber 3, passes through the second differential exhaust chamber 4, and enters the surface processing chamber 5.
- the surface treatment chamber 5 the surface of the coating film on the substrate W is stabilized, that is, inactivated, by O 2 , CO 2 , H 2 O and the inert gas supplied from the gas supply unit 51 (surface treatment). , Step S33).
- the base material W having a stabilized film surface exits from the surface treatment chamber 5, passes through the third differential exhaust chamber 6, is wound by the winding unit 71 in the unloader chamber 7, and becomes a roll again (step). S34). This is the flow of the thermal spraying process according to the first embodiment.
- FIG. 4A is a diagram for explaining an example of a coating formed by the thermal spray processing section 31 of the thermal spray system 100 according to the first embodiment.
- FIG. 4B is a diagram for describing an example of a stabilization layer formed by the surface treatment unit 50 of the thermal spraying system 100 according to the first embodiment.
- lithium metal is a material that easily adheres, after a lithium metal film is formed on the substrate W, the substrate W is rolled into a roll shape, and the portion where the surface of the lithium metal film contacts the substrate W In this case, the coating film and the substrate W adhere to each other, and it is difficult to extend the film into a sheet. Therefore, in order to prevent the lithium metal coating and the substrate W from sticking to each other, it is conceivable to execute a process for stabilizing the surface of the lithium metal coating. However, when used in prelithiation, it is preferred that the lithium metal coating be kept as active as possible. Therefore, it is desirable to stabilize only the surface of the lithium metal coating.
- FIG. 4A shows a state in which a layer of carbon C (or graphite) is formed as an electrode material on a base material W, and then carried into the thermal spraying system 100 to form a thermal spray coating L of lithium metal in the thermal spray processing chamber 3. .
- a carbon film C is formed on a base material W, and a film L of lithium metal is formed on the carbon film C held by a binder B.
- the substrate W is transported to the surface treatment chamber 5. Then, the atmosphere (O 2 , CO 2 , H 2 O, inert gas) in the surface treatment chamber 5 reacts with the coating surface, and a few nanometers (nm) of lithium oxide, lithium carbonate or a mixture thereof is formed on the coating surface. Is formed.
- the combination of gases supplied into the surface treatment chamber 5 is, for example, H 2 O and an inert gas, or CO 2 , H 2 O and an inert gas, or O 2 , H 2 O and an inert gas, Or, CO 2 , O 2 , H 2 O and an inert gas.
- the formed film functions as a stabilizing layer. Therefore, even after the base layer W is wound into a roll after the stabilization layer is formed, the surface of the lithium coating is prevented from sticking to the base layer W.
- FIG. 5 is a table showing experimental results regarding surface treatment conditions according to the first embodiment.
- the transport speed of the substrate W was 1 to 20 m / min
- the width of the lithium coating was 5 to 50 cm
- the width of the current collector foil was 5 to 50 cm.
- the partial pressure of water is at a level at which the surface of the lithium coating is stabilized, and is preferably as low as possible.
- the thickness of the surface of the coating to be stabilized is preferably, for example, 0.1% or more of the thickness of the lithium coating.
- the differential exhaust chambers (2, 4, 6) are provided between the loader chamber 1, the thermal spray processing chamber 3, the surface processing chamber 5, and the unloader chamber 7, respectively.
- the present invention is not limited to this, and the differential exhaust chamber may be provided only between specific chambers.
- the thermal spraying system 100 can be configured so that the differential exhaust chamber is not provided next to the loader chamber 1 and the unloader chamber 7. In this case, the thermal spraying system 100 appropriately controls the pressure difference and the flow of air in the room to prevent mixing of the atmosphere between the rooms.
- the thermal spray processing chamber 3 In the thermal spray processing chamber 3, highly reactive powder material such as lithium is handled, and in the surface processing chamber 5, H 2 O is supplied into the chamber. There is. For this reason, the differential exhaust chamber may be always provided between the thermal spray processing chamber 3 and the surface processing chamber 5.
- each chamber is configured so that the internal pressure and atmosphere of each chamber can be adjusted separately.
- a common exhaust device vacuum pump or the like
- the thermal spraying system includes a thermal spraying unit, a surface treatment unit, and a winding unit.
- the thermal spray portion is configured to form a coating on the first surface of the substrate by thermal spraying the powder material.
- the surface treatment is configured to stabilize the surface of the coating.
- the winding unit is configured to wind the substrate after stabilization of the surface of the coating. For this reason, even if the coating formed by thermal spraying has high tackiness, the surface can be stabilized and the winding can be performed without fear of sticking. For this reason, the base material on which the coating has been formed can be wound up without deteriorating the quality of the coating formed by thermal spraying.
- the thermal spraying unit sprays a lithium powder material to form a lithium coating on the first surface of the base material.
- the surface treatment unit stabilizes the surface of the lithium coating by changing the surface of the lithium coating to lithium oxide, lithium carbonate, or a mixture of lithium oxide and lithium carbonate. For this reason, a thermal spray system can be used for pre-lithiation.
- the surface treatment unit treats the surface of the lithium coating with H 2 O and an inert gas, or CO 2 , O 2 , H 2 O and an inert gas, or O 2, H 2 O, and the inert gas or,, CO 2, O 2, stabilized by exposure to H 2 O and an inert gas.
- the partial pressure of H 2 O for exposing the surface of the lithium coating is set to 0.01 Torr or more.
- the thermal spray system can stabilize the surface of the lithium coating a few nanometers and keep the rest active. For this reason, the thermal spraying system can effectively realize the pre-repetition.
- the thermal spraying system includes a first chamber, a second chamber, a third chamber, and a fourth chamber.
- the base material before thermal spraying is arranged in a wound state.
- the second chamber is provided with a thermal spray section.
- a surface treatment unit is provided in the third chamber.
- the fourth chamber is provided with a winding unit. The substrate is transported from the first chamber to the fourth chamber through slits formed in each of the first, second, third, and fourth chambers. For this reason, the thermal spraying system can perform the thermal spraying process and the surface treatment in separate rooms, and can easily control the processing conditions of each process.
- the thermal spraying system according to the first embodiment further includes a first working exhaust chamber provided between the first chamber and the second chamber and maintained at a higher pressure atmosphere than the second chamber. For this reason, the thermal spray system can prevent the powder material used for the processing in the second chamber from leaking into the first chamber.
- the thermal spraying system according to the first embodiment further includes a second working exhaust chamber provided between the second chamber and the third chamber and maintained at a higher pressure atmosphere than the second chamber. For this reason, the thermal spray system can prevent the powder material and the like used for the processing in the second chamber from leaking into the third chamber. Further, when the lithium powder is used for the processing in the second chamber, the thermal spraying system can prevent the fire from coming into contact with the water used for the processing in the third chamber.
- the thermal spray system according to the first embodiment further includes a third working exhaust chamber provided between the third chamber and the fourth chamber and maintained in a higher-pressure atmosphere than the third chamber.
- the thermal spraying system can execute processing by individually controlling the state of each chamber. Further, the thermal spray system can prevent the internal atmospheres of the respective chambers from being mixed.
- the thermal spraying system according to the first embodiment executes the thermal spraying process and the surface treatment in separate rooms. For this reason, lithium carbonate and lithium oxide are not generated excessively, and the absolute amount of active lithium metal that contributes to the improvement of the efficiency of the lithium secondary battery does not decrease.
- the gas supplied for stabilizing the surface does not remain in the room and does not reduce the absolute amount of active lithium metal. Further, the gas supplied for stabilizing the surface does not need to be exhausted for the thermal spraying process, so that a decrease in throughput can be suppressed.
- the thermal spraying system 100 forms a coating by thermal spraying on the first surface of the base material W.
- the present invention is not limited thereto, and the thermal spraying system 100 may be configured to form a coating by thermal spraying on the first and second surfaces of the base material W.
- 6A, 6B, and 6C are diagrams illustrating Configuration Examples 1 to 3 of the thermal spraying system according to the second embodiment.
- each unit includes a loader chamber 1A, a first differential exhaust chamber 2A, a first thermal spray processing chamber 3A, a second differential exhaust chamber 4A, and a first surface processing chamber 5A. And a second thermal processing chamber 6A, a second surface processing chamber 7A, and a fourth differential exhaust chamber 8A.
- the configuration and function of each unit are the same as in the first embodiment.
- the thermal spraying system 100A shown in FIG. 6A after the first surface of the substrate W is processed in the first thermal spray processing chamber 3A and the first surface processing chamber 5A, the second surface of the substrate W is processed. Is processed in the second thermal processing chamber 6A and the second surface processing chamber 7A.
- the thermal spraying system 100A of FIG. 6A has two thermal processing chambers (first thermal processing chamber 3A, second thermal processing chamber 6A) and two surface processing chambers (first surface processing chamber 5A, second thermal processing chamber 5A). Surface treatment chamber 7A).
- the first thermal spray processing chamber 3A and the second thermal spray processing chamber 6A are arranged in a two-story structure. Further, in the thermal spraying system 100A of FIG.
- a loader chamber 1A in which a loader chamber and an unloader chamber are integrated into one is provided.
- the transport direction of the substrate W is reversed in the first surface treatment chamber 5A, and the substrate W is transported such that the second surface faces upward.
- the second differential evacuation chamber 4A is configured so that both the base material W carried into the first surface treatment chamber 5A and the base material W carried out from the first surface treatment chamber 5A are used. pass.
- the present invention is not limited thereto, and the differential exhaust chamber through which the base material W carried into the first surface treatment chamber 5A passes, and the differential exhaust chamber through which the base material W carried out from the first surface treatment chamber 5A passes.
- the chamber may be provided separately.
- the thermal spray system 100B shown in FIG. 6B includes a loader chamber 1B, a first differential exhaust chamber 2B, a thermal spray processing chamber 3B, a second differential exhaust chamber 4B, a surface processing chamber 5B, and an unloader chamber 6B. , Is provided.
- the thermal spray system 100B shown in FIG. 6B is configured to process both the first surface and the second surface of the substrate W simultaneously.
- the base material W conveyed from the loader chamber 1B passes between the spray parts 31B arranged so as to sandwich the conveyance path of the base material W from two directions in the thermal spray processing chamber 3B. At this time, a film is formed on both the first surface and the second surface of the base material W.
- the differential exhaust chamber is not disposed at the subsequent stage of the surface treatment chamber 5B, but the differential exhaust chamber may be modified to be disposed.
- a guide roller is provided in the surface treatment chamber 5B to control the transport direction of the base material W.
- the position of the guide roller may be changed so that the substrate W comes into contact with the guide roller after the surface of the coating is stabilized in the surface treatment chamber 5B.
- the thermal spraying system 100C shown in FIG. 6C includes a loader chamber 1C, a first differential exhaust chamber 2C, a first thermal spray processing chamber 3C, a second differential exhaust chamber 4C, and a first surface processing chamber 5C. Further, the thermal spray system 100C includes a third differential exhaust chamber 6C, a second thermal spray processing chamber 7C, a fourth differential exhaust chamber 8C, a second surface processing chamber 9C, and an unloader chamber 10C.
- the components included in the thermal spraying system 100C of FIG. 6C are substantially the same as those of the thermal spraying system 100A shown in FIG. 6A, except that a part having a two-story structure is reduced. Note that, also in the example of FIG. 6C, a differential exhaust chamber may be disposed downstream of the second surface treatment chamber 9C.
- the thermal spray system according to the embodiment can be arranged in buildings having various structures by devising the arrangement of each room.
- the thermal spray system according to the above embodiment may further include a cooling mechanism for suppressing damage to the base material W due to heat during thermal spraying.
- a thermal spraying system 100D including the cooling mechanism 34 will be described.
- FIG. 7 is a diagram for explaining a cooling mechanism 34 provided in a thermal spraying system 100D according to the third embodiment.
- the thermal spraying system 100D according to the first embodiment is the same as the thermal spraying system 100 according to the first embodiment except that the thermal spraying system 100D according to the third embodiment includes a cooling mechanism 34 that suppresses the influence of heat generated by thermal spraying in the thermal spraying processing chamber 3D. It has a similar configuration. Therefore, the same components as those in the first embodiment are denoted by the same reference numerals, and detailed description and / or illustration is omitted.
- the cooling mechanism 34 shown in FIG. 7 includes a cooling roller 35, a guide roller 36, and a refrigerant supply unit 37.
- the cooling roller 35 is disposed below the injection port of the thermal spray section 31 in the thermal spray processing chamber 3D and on the transport path of the base material W.
- the cooling roller 35 has a refrigerant passage 35A through which the refrigerant flows.
- the cooling roller 35 has a width and a diameter capable of transporting the base material W unwound from the loader chamber 1. Further, the diameter of the cooling roller 35 is formed to a size that satisfies the cooling conditions described later.
- the guide roller 36 is disposed on the transport path of the base material W in the thermal spray processing chamber 3D.
- the guide roller 36 is disposed closer to the loader chamber 1 than the cooling roller 35 on the transport path of the base material W.
- the guide roller 36 increases the transport distance of the substrate W on the cooling roller 35 by changing the transport direction of the substrate W before the substrate W reaches the cooling roller 35.
- the guide roller 36 is arranged at a position closer to the second differential exhaust chamber 4 than the cooling roller 35. Even if the guide roller 36 is not provided, the guide roller 36 may not be provided if the transport distance of the base material W on the cooling roller 35 can satisfy the cooling condition described later. Further, the relative positional relationship between the guide roller 36 and the cooling roller 35 is not particularly limited.
- FIG. 7 illustrates one guide roller 36, but the number of guide rollers 36 is not particularly limited. An arbitrary number of guide rollers 36 can be arranged to adjust the transport distance of the base material W on the cooling roller 35.
- the refrigerant supply unit 37 supplies the refrigerant to the refrigerant passage 35A of the cooling roller 35.
- the specific configuration of the refrigerant supply unit 37 is not particularly limited.
- the type of the refrigerant supplied by the refrigerant supply unit 37 is not particularly limited, and may be, for example, tap water adjusted to a predetermined temperature.
- the base material W unwound from the unwinding section 11 in the loader chamber 1 passes through the first working exhaust chamber 2 and enters the thermal spray processing chamber 3D.
- the base material W is first wound upward from below the guide roller 36.
- the transport direction from the loader chamber 1 to the unloader chamber 7 is the forward direction
- the transport direction of the substrate W wound around the guide roller 36 is opposite to the forward direction.
- the base material W is wound upward from below the cooling roller 35 disposed above the guide roller 36, and the transport direction becomes the forward direction again.
- the base material W passes from the thermal spray processing chamber 3D, passes through the second differential exhaust chamber 4, the surface treatment chamber 5, and the third working exhaust chamber 6, and is taken up by the take-up portion 71 in the unloader chamber 7.
- the molten powder material is jetted onto the base material W by the thermal spraying part 31 disposed above the cooling roller 35 to form a film. At this time, the surface of the substrate W is heated by the molten powder material.
- the coolant flows through the cooling roller 35 during the thermal spraying process, whereby the temperature rise of the base material W on the cooling roller 35 is suppressed.
- the present inventors conducted experiments to examine cooling conditions for suppressing a temperature rise of the base material W in the thermal spraying system 100D, and obtained the following knowledge.
- Example 1 Effect of refrigerant flow rate on cooling performance
- the flow rate of the refrigerant was changed while the transport speed of the base material W was fixed, and the influence of the change in the flow rate of the refrigerant was examined.
- the transport speed and the flow rate were set as follows.
- -Transfer speed of the substrate W 0.1 m / min
- Flow rate of the refrigerant 2 L / min, 5 L / min, 10 L / min
- the temperature of the substrate W starts the thermal spraying process. It was found that it was stabilized in about 20 to 30 minutes after that, and then stabilized.
- the temperature of the base material W was stabilized at a temperature lower by about 5 ° C. to 7 ° C. than in the case of 2 L / min. From this, it was found that the larger the flow rate of the refrigerant, the more stable the temperature of the base material W at a low temperature, but the more stable the temperature of the base material W regardless of the flow rate of the refrigerant.
- Experiment 2 Influence of substrate transfer speed on cooling performance
- the effect of the transport speed of the substrate W on the cooling performance was measured.
- Experiment 2 was performed under the following conditions. -Transport speed of the substrate W: 1 m / min, 3 m / min, 5 m / min, 10 m / min, 20 m / min-Flow rate of refrigerant: 2 L / min, 5 L / min, 10 L / min.
- the substrate W was heated by the heater while transporting the substrate W. Five minutes after the start of heating, the temperature of the substrate W was measured.
- the diameter of the cooling roller 35, the contact distance (transport distance) between the cooling roller 35 and the substrate W, the flow rate of the refrigerant, What is necessary is just to set the conveyance speed of the base material W in advance as a cooling condition.
- the set cooling conditions are satisfied, the temperature of the base material W does not increase even if the thermal spraying process is continued for a long time.
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Abstract
Description
以下の開示は、溶射システム、溶射方法およびリチウム二次電池の製造方法に関する。 The following disclosure relates to a thermal spraying system, a thermal spraying method, and a method for manufacturing a lithium secondary battery.
電気化学電池の大量製造方法として、2つのリールの間で巻き取られる基板上に材料を成膜するように構成されたプロセスチャンバを含む電気化学電池の成膜用の装置が提案されている(特許文献1)。 As a method of mass-producing electrochemical cells, an apparatus for film formation of an electrochemical cell including a process chamber configured to form a material on a substrate wound between two reels has been proposed ( Patent Document 1).
また、電極シート上の電極材料にリチウムイオンをドーピングしてリチウムイオンキャパシタ用電極を製造する電極製造装置が提案されている(特許文献2)。当該装置では、処理室内に搬入される電極シートの電極材料上に、リチウム含有粉末を溶融させながら吹き付けて、不活性ガス雰囲気中でリチウムの薄膜を成膜する。この技術では、リチウムと反応しない不活性ガスを用いることで、リチウムの自然発火などを防いでいる。 Also, an electrode manufacturing apparatus has been proposed in which an electrode material on an electrode sheet is doped with lithium ions to manufacture an electrode for a lithium ion capacitor (Patent Document 2). In this apparatus, a lithium-containing powder is melted and sprayed onto an electrode material of an electrode sheet carried into a processing chamber to form a lithium thin film in an inert gas atmosphere. In this technology, spontaneous ignition of lithium or the like is prevented by using an inert gas that does not react with lithium.
本開示は、溶射により形成された被膜の品質を落とすことなく、被膜が形成された基材を巻き取ることができる技術を提供する。 The present disclosure provides a technique capable of winding a substrate on which a coating is formed without deteriorating the quality of the coating formed by thermal spraying.
開示する実施形態において、溶射システムは、溶射部と、表面処理部と、巻き取り部と、を備える。溶射部は、粉末材料の溶射により、基材の第1の表面上に被膜を形成するよう構成される。表面処理部は、被膜の表面を安定化させるよう構成される。巻き取り部は、被膜の表面の安定化の後、基材を巻き取るよう構成される。 に お い て In the disclosed embodiment, the thermal spraying system includes a thermal spraying unit, a surface treatment unit, and a winding unit. The thermal spray portion is configured to form a coating on the first surface of the substrate by thermal spraying the powder material. The surface treatment is configured to stabilize the surface of the coating. The winding unit is configured to wind the substrate after stabilization of the surface of the coating.
開示する実施態様によれば、溶射により形成された被膜の品質を落とすことなく、被膜が形成された基材を巻き取ることができるという効果を奏する。 According to the disclosed embodiment, there is an effect that the substrate on which the coating is formed can be wound without deteriorating the quality of the coating formed by thermal spraying.
以下、添付図面を参照して、本願の開示する溶射システム、溶射方法およびリチウム二次電池の製造方法の実施形態を詳細に説明する。なお、以下に示す各実施形態により本開示が限定されるものではない。また、図面は模式的なものであり、各要素の寸法の関係、各要素の比率などは、現実と異なる場合があることに留意する必要がある。さらに、図面の相互間においても、互いの寸法の関係や比率が異なる部分が含まれている場合がある。また、各実施形態は、処理内容を矛盾させない範囲で適宜組み合わせることが可能である。 Hereinafter, embodiments of a thermal spraying system, a thermal spraying method, and a method of manufacturing a lithium secondary battery disclosed in the present application will be described in detail with reference to the accompanying drawings. The present disclosure is not limited by the embodiments described below. In addition, it is necessary to keep in mind that the drawings are schematic, and the dimensional relationship of each element, the ratio of each element, and the like may be different from reality. Further, the drawings may include portions having different dimensional relationships and ratios. In addition, the embodiments can be appropriately combined within a range that does not contradict processing contents.
<プレリチエーション>
第1の実施形態について説明する前に、まず、プレリチエーションについて説明する。
<Preritiation>
Before describing the first embodiment, first, prerelation will be described.
リチウム二次電池は、充電時にリチウムイオンが正極から負極に移動し、放電時にリチウムイオンが負極から正極に移動する。しかし、放電時にリチウムイオンの一部が負極の金属材料(たとえばカーボン)と反応して正極に移動しない場合がある。この場合、負極に残ったリチウムイオンは容量として機能せず、電池容量が十分有効に活用できなくなる。 (4) In a lithium secondary battery, lithium ions move from the positive electrode to the negative electrode during charging, and lithium ions move from the negative electrode to the positive electrode during discharging. However, at the time of discharge, a part of lithium ions may react with a metal material (eg, carbon) of the negative electrode and not move to the positive electrode in some cases. In this case, the lithium ions remaining on the negative electrode do not function as a capacity, and the battery capacity cannot be used sufficiently effectively.
そこで、リチウム系材料を予め負極または正極にドーピングしておき容量効率を改善するプレリチエーション(pre-lithiation)技術が研究されている。プレリチエーション技術とは、充放電初期に消費された、もしくはイオン電導性を失ったリチウムイオンを事前に負極または正極に充填しておくことで充放電効率を改善させるものである。 Therefore, a pre-lithiation technique for improving the capacity efficiency by doping a lithium-based material into a negative electrode or a positive electrode in advance has been studied. The prerepetition technique is to improve the charge / discharge efficiency by previously filling the negative electrode or the positive electrode with lithium ions consumed in the early stage of charge / discharge or having lost ion conductivity.
以下に説明する第1の実施形態に係る溶射システム100は、プレリチエ―ションのため、すなわちリチウムイオン二次電池などの電極を製造するために用いることができる。
溶 The
<第1の実施形態>
第1の実施形態に係る溶射システム100は、ロール状の基材Wを巻き出して巻き取りながら、基材W上に溶射被膜を形成できるように構成される。また、第1の実施形態に係る溶射システム100は、基材Wを巻き取る前に、基材W上に形成された溶射被膜の表面を安定化させるように構成される。このため、溶射被膜が粘着性の高い材料からなる場合であっても、基材Wの巻き取り時に溶射被膜と溶射被膜の上に巻き回された基材表面とが固着することを防止することができる。また、第1の実施形態に係る溶射システム100は、溶射被膜の材料の飛散を防止するための差動排気機構を有する。このため、リチウムなどの反応性の高い材料を使用する場合でも材料の飛散や漏洩を防止することができる。
<First embodiment>
The
溶射システムにおける処理対象である基材Wはたとえば、電極シートであり、電極シート上には電極材料が形成されている。電極材料はたとえば、活性炭、グラファイトなどの炭素材料である。電極材料はたとえば、1~100センチメートル(cm)程度の幅に形成される。基材Wはロール状に巻き回した状態で搬送することができる。基材Wは片面塗布品であっても両面塗布品であってもよい。なお、以下の説明中、シート状の基材Wの一方側の表面を第1の表面、第1の表面と反対側の表面を第2の表面とも呼ぶ。基材Wはたとえば、リチウムイオン二次電池の負極となる。負極はたとえば、Si系材料、SiO系材料、または、炭素とSi系若しくはSiO系の材料との混合物で形成される。 基材 The substrate W to be processed in the thermal spraying system is, for example, an electrode sheet, and an electrode material is formed on the electrode sheet. The electrode material is, for example, a carbon material such as activated carbon and graphite. The electrode material is formed to have a width of, for example, about 1 to 100 centimeters (cm). The substrate W can be transported in a state wound in a roll. The substrate W may be a single-sided coated product or a double-sided coated product. In the following description, the surface on one side of the sheet-shaped substrate W is also referred to as a first surface, and the surface on the opposite side to the first surface is also referred to as a second surface. The base material W becomes, for example, a negative electrode of a lithium ion secondary battery. The negative electrode is formed of, for example, a Si-based material, a SiO-based material, or a mixture of carbon and a Si-based or SiO-based material.
図1は、第1の実施形態に係る溶射システム100の構成の一例を示す概略断面図である。また、図2は、第1の実施形態に係る溶射システム100の構成の一例を示す概略斜視図である。
FIG. 1 is a schematic cross-sectional view showing an example of the configuration of the
図1および図2に示す溶射システム100は、巻出し側の収容室(以下ローダ室とも呼ぶ)1と、溶射処理室3と、表面処理室5と、巻き取り側の収容室(以下アンローダ室とも呼ぶ)7と、を備える。ローダ室1、溶射処理室3、表面処理室5およびアンローダ室7は各々、第1室、第2室、第3室および第4室の一例である。ローダ室1と溶射処理室3との間には第1の差動排気室2が設けられる。また、溶射処理室3と表面処理室5との間には第2の差動排気室4が設けられる。また、表面処理室5とアンローダ室7との間には第3の差動排気室6が設けられる。
The
ローダ室1と、第1の差動排気室2との間には、ローダ室1の内部空間と第1の差動排気室2の内部空間とを連通させるスリットS1が設けられる。第1の差動排気室2と溶射処理室3との間には、第1の差動排気室2の内部空間と溶射処理室の内部空間とを連通させるスリットS2が設けられる。溶射処理室3と第2の差動排気室4との間には、溶射処理室3の内部空間と第2の差動排気室4の内部空間とを連通させるスリットS3が設けられる。差動排気室4と表面処理室5との間には、差動排気室4の内部空間と表面処理室5の内部空間とを連通させるスリットS4が設けられる。表面処理室5と第3の差動排気室6との間には、表面処理室5の内部空間と第3の差動排気室6の内部空間とを連通させるスリットS5が設けられる。第3の差動排気室6とアンローダ室7との間には、第3の差動排気室6の内部空間とアンローダ室7の内部空間とを連通させるスリットS6が設けられる。
ス リ ッ ト A slit S1 is provided between the
スリットS1乃至スリットS6は、各室間で基材Wを搬送するために形成される。このため、スリットS1乃至スリットS6は基材Wの搬送経路上に形成される。基材Wは、スリットS1乃至スリットS6を通過して、ローダ室1からアンローダ室7に搬送される。スリットS1乃至スリットS6は、基材W上に形成される電極材料や溶射被膜が、スリットS1乃至スリットS6が形成される各室の壁に接触しない大きさおよび形状に構成される。スリットS1乃至S6は各々、略同一の大きさおよび形状に構成される。また、スリットS1乃至S6は基材Wの搬送を妨げない位置に配置される。図1においては基材Wの搬送経路を略直線状に図示しているが、基材Wの搬送経路は必ずしも直線状でなくてもよい。たとえば、基材Wの搬送のためにガイドローラを設けて基材Wの搬送経路を制御することができる(図2参照)。この場合、スリットS1乃至S6は、基材Wの搬送経路にあわせた位置に配置することができる。
The slits S1 to S6 are formed to transport the substrate W between the respective chambers. Therefore, the slits S1 to S6 are formed on the transport path of the base material W. The substrate W is transported from the
ローダ室1は、処理対象である基材Wがセットされる巻出し部11を収容する。巻出し部11はたとえば、処理対象である基材Wが巻き回されるローラである。ローラはたとえば、円柱状の巻出し軸である。ローラの周りにロール状に巻き回された基材Wがセットされる。巻出し部11は、ロール状の基材Wの中心を巻出し軸に差し込むことで基材Wが支持されるように構成することができる。
The
ローダ室1は、内部を所定の雰囲気および圧力に維持できるよう、吸排気口12を介して吸排気部13と接続される。吸排気部13は、ローダ室1の内部を所定の雰囲気および圧力に維持することができれば、具体的な構成は特に限定されない。吸排気部13はたとえば、ガス供給源、ガスの流量を調整する流量調整器(たとえばマスフローコントローラ)、開閉バルブ等を有する。吸排気部13はたとえば、ローダ室1内を不活性ガス雰囲気に維持するよう構成される。たとえば、吸排気部13はローダ室1内をアルゴンガス雰囲気に維持するよう構成される。
(4) The
溶射処理室3は、溶射部31を収容する。溶射部31はたとえば、粉末材料の溶射により、基材Wの第1の表面上に被膜を形成するよう構成される。溶射部31はたとえば、プラズマ溶射により溶射被膜を形成するよう構成される溶射ガンである。溶射部31は、溶射材料と各種ガス(たとえばキャリアガスおよびパージガス)を供給する供給部と、プラズマを生成してプラズマの熱により溶射材料を溶融する機構と、を有する。溶射部31はまた、溶射噴流を基材Wに向けて噴射する噴射口を有する。溶射部31の噴射口は、溶射処理室3の内部に、基材Wの搬送経路に対向するよう配置される。また、噴射口が基材Wの搬送経路に対向して室内に配置されている限り、溶射部31の供給部および溶射材料を溶融する機構の一部または全部は溶射処理室3の外部に配置されてもよい。
The thermal
溶射処理室3はまた、排気口32を有する。排気口32は真空ポンプ33に接続される。排気口32を介して溶射処理室3内の空気が真空ポンプ33によって真空排気され、溶射処理室3内が減圧される。
The thermal
表面処理室5は、表面処理部50を備える。表面処理部50は、溶射処理室3において基材Wの第1の表面上に形成された被膜の表面を安定化させるよう構成される。すなわち、表面処理部50は、表面処理を実行するよう構成される。表面処理部50は、ガス供給部51と、ガス排出部52と、を備える。
The
ガス供給部51は、表面処理室5内に被膜の表面を安定化させるためのガスを供給する。たとえば、プレリチエ―ションの場合には、ガス供給部51は、表面処理室5内に酸素(O2)、二酸化炭素(CO2)、水(H2O)および不活性ガスを所定の分圧で供給する。なお、ガス供給部51は常にO2、CO2、H2Oおよび不活性ガスを供給しなくてもよい。たとえば、ガス供給部51は、O2およびCO2のいずれか一方のみを供給してもよい。
The
ガス供給部51が供給するガスの分圧は例えば以下の通りである。
O2ガス:0~760Torr
CO2ガス:0~760Torr
H2O:0~760Torr
Arガス:0~760Torr
ただし、基材W上の被膜の膜厚に応じて、各ガスの分圧が調整される。
The partial pressure of the gas supplied by the
O 2 gas: 0 to 760 Torr
CO 2 gas: 0 to 760 Torr
H 2 O: 0 to 760 Torr
Ar gas: 0 to 760 Torr
However, the partial pressure of each gas is adjusted according to the thickness of the film on the substrate W.
ガス排気部52は、表面処理室5内のガスを排気する。なお、ガス供給部51およびガス排気部52の具体的構成は特に限定されない。
The
表面処理室5はまた、排気口53を有する。排気口53は真空ポンプ54に接続される。排気口53を介して表面処理室5内の空気が真空ポンプ54によって真空排気され、表面処理室5内が減圧される。表面処理室5内は大気圧以下の圧力に制御される。
The
アンローダ室7は、巻き取り部71を収容する。巻き取り部71は、基材Wの第1の表面上に形成された被膜表面の安定化の後、基材Wを巻き取るよう構成される。巻き取り部71はたとえば、処理対象である基材Wが巻き回されるローラである。ローラはたとえば、円柱状の巻き取り軸である。ローラ(巻き取り部71)の周りに溶射処理室3および表面処理室5を通過した基材Wが巻き取られる。
The
アンローダ室7は、内部を所定の雰囲気および圧力に維持できるよう、吸排気口72を介して吸排気部73と接続される。吸排気部73は、アンローダ室7の内部を所定の雰囲気および圧力に維持することができれば、具体的な構成は特に限定されない。吸排気部73はたとえば、ガス供給源、ガスの流量を調整する流量調整器(たとえばマスフローコントローラ)、開閉バルブ等を有する。吸排気部73はたとえば、アンローダ室7内を不活性ガス雰囲気に維持するよう構成される。たとえば、吸排気部73はアンローダ室7内をアルゴンガス雰囲気に維持するよう構成される。
(4) The
第1の差動排気室2は、ローダ室1と溶射処理室3との間の差動排気機構として機能する。第1の差動排気室2は、ローダ室1と溶射処理室3との間に設けられ、溶射処理室3よりも高圧雰囲気に維持される。第1の差動排気室2は、たとえば吸気口21を介してガス供給部22と接続される。また、第1の差動排気室2は、たとえば排気口23を介して排気部24と接続される。ガス供給部22は吸気口21を介して第1の差動排気室2に所定のガスを供給する。また、排気部24は排気口23を介して第1の差動排気室2内を排気する。
The first
このように、第1の差動排気室2は、ガス供給部22と排気部24とを備えることにより、ローダ室1の内部雰囲気と、溶射処理室3の内部雰囲気とが流通することを防止する。第1の差動排気室2は、いわばローダ室1と溶射処理室3との間の分離層として機能する。また、第1の差動排気室2は、溶射処理室3内での溶射によって飛散する粉末材料がローダ室1に漏洩することを防止する。なお、第1の差動排気室2は差動排気によってローダ室1および溶射処理室3の内部雰囲気の流通を防止し、溶射材料の漏洩を防止することができればよく、ガス供給部22および排気部24等の構成は特に限定されない。
As described above, since the first
第2の差動排気室4は、溶射処理室3と表面処理室5との間の差動排気機構として機能する。第2の差動排気室4は、溶射処理室3と表面処理室5との間に設けられ、溶射処理室3よりも高圧雰囲気に維持される。第2の差動排気室4は、たとえば吸気口41を介してガス供給部42と接続される。また、第2の差動排気室4は、たとえば排気口43を介して排気部44と接続される。ガス供給部42は吸気口41を介して第2の差動排気室4に所定のガスを供給する。また、排気部44は排気口43を介して第2の差動排気室4内を排気する。
The second
このように、第2の差動排気室4は、ガス供給部42と排気部44とを備えることにより、溶射処理室3の内部雰囲気と、表面処理室5の内部雰囲気とが流通することを防止する。第2の差動排気室4は、いわば溶射処理室3と表面処理室5との間の分離層として機能する。また、第2の差動排気室4は、溶射処理室3内での溶射によって飛散する粉末材料が表面処理室5に漏洩することを防止する。なお、第2の差動排気室4は差動排気によって溶射処理室3および表面処理室5の内部雰囲気の流通を防止し、溶射材料の漏洩を防止することができればよく、ガス供給部42および排気部44等の構成は特に限定されない。
As described above, since the second
第3の差動排気室6は、表面処理室5とアンローダ室7との間の差動排気機構として機能する。第3の差動排気室6は、表面処理室5とアンローダ室7との間に設けられ、表面処理室5よりも高圧雰囲気に維持される。第3の差動排気室6は、たとえば吸気口61を介してガス供給部62と接続される。また、第3の差動排気室6は、たとえば排気口63を介して排気部64と接続される。ガス供給部62は吸気口61を介して第3の差動排気室6に所定のガスを供給する。また、排気部64は排気口63を介して第3の差動排気室6内を排気する。
The third
このように、第3の差動排気室6は、ガス供給部62と排気部64とを備えることにより、表面処理室5の内部雰囲気とアンローダ室7の内部雰囲気とが流通することを防止する。第3の差動排気室6は、いわば表面処理室5とアンローダ室7との間の分離層として機能する。なお、第3の差動排気室6は差動排気によって表面処理室5およびアンローダ室7の内部雰囲気の流通を防止することができればよく、ガス供給部62および排気部64等の構成は特に限定されない。
As described above, since the third
第1の差動排気室2、第2の差動排気室4および第3の差動排気室6は各々、同様に構成することができる。また、各室内の雰囲気は、リチウム粉末と反応せず、表面処理後の表面の不活性状態を維持できることから、不活性ガス(たとえばアルゴン)雰囲気とすることが好ましい。
The first
溶射システム100はさらに、制御装置8を備える。制御装置8は、制御部81、操作部82および記憶部83を有する。
The
制御部81は、溶射システム100の各部の動作を制御する。
The
操作部82は、オペレータによる、溶射システム100の操作のためのコマンドの入力操作等を受け付ける。操作部82はたとえばキーボード、ディスプレイ、タッチパネル等である。
The
記憶部83は、溶射システム100の各部の動作を制御するためのプログラムを記憶する。
The
制御装置8は、たとえば、CPU(Central Processing Unit)とメモリを備えるコンピュータである。記憶部83は、溶射システム100において実行される各種の処理を制御するプログラムが格納される。制御部81は、記憶部83に記憶されたプログラムを読み出して実行することによって溶射システム100の動作を制御する。また、制御部81はたとえば、記憶部83に記憶されたプログラムを読み出して実行することにより、溶射システム100が配置される室内の温度や湿度を所定値に維持するよう構成してもよい。溶射材料の中には水に接触すると発火するもの等、温度や湿度に反応するものがある。このため、溶射システム100が配置される室内の温度および湿度は、使用する溶射材料の特性に合わせて制御装置8により制御されるように構成してもよい。また、溶射システム100が備える各室1乃至7に供給され排気されるガスの流量や供給および排気のタイミングも制御装置8により制御されるように構成してもよい。
The
なお、かかるプログラムは、コンピュータによって読み取り可能な記憶媒体に記録されていたものであって、その記憶媒体から記憶部83にインストールされたものであってもよい。コンピュータによって読み取り可能な記憶媒体としては、たとえばハードディスク(HD)、フレキシブルディスク(FD)、コンパクトディスク(CD)、マグネトオプティカルディスク(MO)、メモリカードなどがある。
Note that such a program is recorded on a computer-readable storage medium, and may be installed in the
図2は、第1の実施形態に係る溶射システム100の構成の一例を示す。図2の例では、第1の差動排気室2、第2の差動排気室4および第3の差動排気室6の各々は、室の天井側において真空ポンプと接続されることで内部圧力が制御されている。このように、各差動排気室において差動排気を実現する方法は特に限定されない。また、基材Wは複数のガイドローラによって支持されている。図2の例ではガイドローラは水平方向に整列して配置されている。ただし、ガイドローラの配置位置はこれに限定されず、表面処理室5他の室にもガイドローラを配置して基材Wを案内するように溶射システム100を構成してもよい。このように、溶射システム100の細部は様々に変形することができる。
FIG. 2 shows an example of a configuration of the
<溶射システム100における処理の流れの一例>
図3は、第1の実施形態に係る溶射システム100における溶射処理の流れの一例を示すフローチャートである。
<Example of Process Flow in
FIG. 3 is a flowchart illustrating an example of the flow of the thermal spraying process in the
上記のように構成された溶射システム100では、制御装置8の制御下で、溶射処理が開始する。まず、ロール状の基材Wがローダ室1に搬入され、巻出し部11にセットされる(ステップS31)。次に、記憶部83に記憶されたプログラム等が実行されることで、溶射システム100の各室の雰囲気、温度、湿度等が制御される。そして、基材Wが巻出し部11から巻き出され、搬送経路を通って第1の差動排気室2を通過し溶射処理室3に搬送される。溶射処理室3において、溶射部31は溶融した粉末材料を基材Wの表面に噴射し、被膜を形成する(溶射処理、ステップS32)。被膜が形成された基材Wは溶射処理室3を出て第2の差動排気室4を通過し表面処理室5に入る。表面処理室5においては、ガス供給部51から供給されるO2,CO2,H2Oおよび不活性ガスにより、基材W上の被膜の表面が安定化すなわち不活性化される(表面処理、ステップS33)。被膜表面が安定化された基材Wは表面処理室5から出て第3の差動排気室6を通過し、アンローダ室7において巻き取り部71に巻き取られて再びロール状となる(ステップS34)。これが第1の実施形態に係る溶射処理の流れである。
In the
<表面処理>
次に図4Aおよび図4Bを参照して表面処理室5における表面処理についてさらに説明する。図4Aは、第1の実施形態に係る溶射システム100の溶射処理部31により形成される被膜の一例について説明するための図である。図4Bは、第1の実施形態に係る溶射システム100の表面処理部50により形成される安定化層の一例について説明するための図である。
<Surface treatment>
Next, the surface treatment in the
ここでは、プレリチエ―ションのため、溶射材料として粉末状のリチウム金属材料を用いるものとする。リチウム金属は粘着しやすい材料であるため、基材W上にリチウム金属の被膜を形成した後、基材Wを丸めてロール状にするとリチウム金属の被膜の表面と基材Wとが接触した部分において被膜と基材Wとが固着し、シート状に延ばすことが困難になる。そこで、リチウム金属の被膜と基材Wとの固着を防止するために、リチウム金属の被膜の表面を安定化させる処理を実行することが考えられる。しかし、プレリチエ―ションに使用する場合、リチウム金属の被膜はできるだけ活性の状態で保持することが好ましい。したがって、リチウム金属の被膜の表面のみを安定化させることが望ましい。 Here, it is assumed that a powdery lithium metal material is used as a thermal spraying material for prelithiation. Since lithium metal is a material that easily adheres, after a lithium metal film is formed on the substrate W, the substrate W is rolled into a roll shape, and the portion where the surface of the lithium metal film contacts the substrate W In this case, the coating film and the substrate W adhere to each other, and it is difficult to extend the film into a sheet. Therefore, in order to prevent the lithium metal coating and the substrate W from sticking to each other, it is conceivable to execute a process for stabilizing the surface of the lithium metal coating. However, when used in prelithiation, it is preferred that the lithium metal coating be kept as active as possible. Therefore, it is desirable to stabilize only the surface of the lithium metal coating.
図4Aは、基材Wの上に電極材料としてカーボンC(またはグラファイト)の層を形成した後、溶射システム100に搬入し、溶射処理室3においてリチウム金属の溶射被膜Lを形成した状態を示す。図4Aの状態では、基材Wの上に、カーボン膜Cが形成されバインダBによって保持された上にリチウム金属の被膜Lが形成されている。
FIG. 4A shows a state in which a layer of carbon C (or graphite) is formed as an electrode material on a base material W, and then carried into the
図4Aの被膜Lが形成された後、基材Wは表面処理室5に搬送される。そして、表面処理室5内の雰囲気(O2,CO2,H2O,不活性ガス)と被膜表面とが反応し、被膜表面に数ナノメートル(nm)の酸化リチウム、炭酸リチウムまたはその混合物の膜が形成される。表面処理室5内に供給されるガスの組み合わせは、たとえば、H2Oおよび不活性ガス、または、CO2、H2Oおよび不活性ガス、または、O2、H2Oおよび不活性ガス、または、CO2、O2、H2Oおよび不活性ガスである。形成された膜は安定化層として機能する。このため、安定化層が形成された後、基材Wをロール状に巻き回してもリチウム被膜の表面が基材Wに固着することが防止される。
After the film L of FIG. 4A is formed, the substrate W is transported to the
<処理条件等>
ところで、上述のように、表面処理の際にリチウム被膜全体を安定化させてしまうと、電極容量の有効活用ができなくなってしまう。そこで、本発明者らは、表面処理において用いる各ガスの分圧を変化させて実験を行った。図5は、第1の実施形態に係る表面処理の条件に関する実験結果を示す表である。なお、実験において、基材Wの搬送速度は1~20m/min、リチウム被膜の幅は5~50cm、集電箔の幅は5~50cmとした。
<Processing conditions etc.>
By the way, as described above, if the entire lithium coating is stabilized during the surface treatment, the electrode capacity cannot be effectively used. Therefore, the present inventors conducted experiments by changing the partial pressure of each gas used in the surface treatment. FIG. 5 is a table showing experimental results regarding surface treatment conditions according to the first embodiment. In the experiment, the transport speed of the substrate W was 1 to 20 m / min, the width of the lithium coating was 5 to 50 cm, and the width of the current collector foil was 5 to 50 cm.
また、実験においてリチウム被膜に生じた変化は、走査型電子顕微鏡(SEM)、X線光電分光法(XPS)により観察した。この結果、図5に示すように、水(H2O)の分圧が0.01未満の場合は、リチウム被膜には変化が見られなかった。これに対して、水の分圧が0.05以上、さらに0.45以上では、他のガスの処理条件に関わらずリチウム被膜の表面の安定化が認められた。このことから、プレリチエ―ションに適した表面処理の条件は、水の分圧が0.01以上、好ましくは0.05以上であると発明者らは結論付けた。なお、水の分圧が高すぎると、リチウム被膜全体が安定化されてしまうため、水の分圧は、リチウム被膜の表面が安定化するレベルであり、かつ、できるだけ低いことが好ましい。また、安定化する被膜表面の厚みは、たとえばリチウム被膜の膜厚の0.1%以上が好ましい。 In addition, changes occurring in the lithium coating in the experiment were observed by a scanning electron microscope (SEM) and an X-ray photoelectric spectroscopy (XPS). As a result, as shown in FIG. 5, when the partial pressure of water (H 2 O) was less than 0.01, no change was observed in the lithium coating. On the other hand, when the partial pressure of water was 0.05 or more, and further 0.45 or more, stabilization of the surface of the lithium coating was recognized regardless of other gas treatment conditions. From these facts, the inventors concluded that the surface treatment conditions suitable for prelithiation are such that the partial pressure of water is 0.01 or more, preferably 0.05 or more. If the partial pressure of water is too high, the entire lithium coating is stabilized. Therefore, the partial pressure of water is at a level at which the surface of the lithium coating is stabilized, and is preferably as low as possible. The thickness of the surface of the coating to be stabilized is preferably, for example, 0.1% or more of the thickness of the lithium coating.
<変形例>
なお、上記第1の実施形態においては、ローダ室1、溶射処理室3、表面処理室5およびアンローダ室7の各々の間に差動排気室(2,4,6)を設けるものとした。しかし、これに限らず、差動排気室は、特定の室間のみに設けるものとしてもよい。たとえば、差動排気室は、ローダ室1およびアンローダ室7の隣りには設けないように溶射システム100を構成することも可能である。この場合には、溶射システム100は、室内の圧力差や空気の流れを適切に制御して室間での雰囲気の混合を防止する。
<Modification>
In the first embodiment, the differential exhaust chambers (2, 4, 6) are provided between the
なお、溶射処理室3においてはリチウム等の反応性の高い粉末材料が扱われ、表面処理室5においてはH2Oを室内に供給するため、仮にリチウムが表面処理室5に侵入すると発火の恐れがある。このため、差動排気室は、溶射処理室3と表面処理室5の間には必ず設けるものとしてもよい。
In the thermal
なお、各室の排気機構については、各室の内部圧力および雰囲気を別々に調整することができるように構成する。ただし、ガスの混合による安全上の問題がなければ共通の排気装置(真空ポンプ等)を設けてもよい。 In addition, the exhaust mechanism of each chamber is configured so that the internal pressure and atmosphere of each chamber can be adjusted separately. However, a common exhaust device (vacuum pump or the like) may be provided if there is no safety problem due to gas mixing.
<第1の実施形態の効果>
上記の第1の実施形態に係る溶射システムは、溶射部と、表面処理部と、巻き取り部と、を備える。溶射部は、粉末材料の溶射により、基材の第1の表面上に被膜を形成するよう構成される。表面処理部は、被膜の表面を安定化させるよう構成される。巻き取り部は、被膜の表面の安定化の後、基材を巻き取るよう構成される。このため、溶射により形成された被膜が高い粘着性を有する場合であっても、表面を安定化させることで、固着の恐れなく巻き取りを行うことができる。このため、溶射により形成された被膜の品質を落とすことなく、被膜が形成された基材を巻き取ることができる。
<Effects of First Embodiment>
The thermal spraying system according to the first embodiment includes a thermal spraying unit, a surface treatment unit, and a winding unit. The thermal spray portion is configured to form a coating on the first surface of the substrate by thermal spraying the powder material. The surface treatment is configured to stabilize the surface of the coating. The winding unit is configured to wind the substrate after stabilization of the surface of the coating. For this reason, even if the coating formed by thermal spraying has high tackiness, the surface can be stabilized and the winding can be performed without fear of sticking. For this reason, the base material on which the coating has been formed can be wound up without deteriorating the quality of the coating formed by thermal spraying.
また、第1の実施形態に係る溶射システムにおいて、溶射部は、リチウム粉末材料を溶射して、基材の第1の表面上にリチウム被膜を形成する。そして、表面処理部は、前記リチウム被膜の表面を酸化リチウム、炭酸リチウムまたは酸化リチウムと炭酸リチウムの混合物に変化させることにより安定化させる。このため、プレリチエ―ションのために溶射システムを利用することができる。 In addition, in the thermal spraying system according to the first embodiment, the thermal spraying unit sprays a lithium powder material to form a lithium coating on the first surface of the base material. The surface treatment unit stabilizes the surface of the lithium coating by changing the surface of the lithium coating to lithium oxide, lithium carbonate, or a mixture of lithium oxide and lithium carbonate. For this reason, a thermal spray system can be used for pre-lithiation.
また、第1の実施形態に係る溶射システムにおいて、表面処理部は、リチウム被膜の表面を、H2Oおよび不活性ガス、または、CO2、O2、H2Oおよび不活性ガス、または、O2、H2Oおよび不活性ガス、または、CO2、O2、H2Oおよび不活性ガスに曝露することにより安定化させる。また、表面処理部は、リチウム被膜の表面を曝露させるH2Oの分圧を0.01Torr以上とする。このため、溶射システムは、リチウム被膜の表面数ナノメートルを安定化させて残りの部分を活性に維持することができる。このため、溶射システムはプレリチエ―ションを効果的に実現することができる。 Further, in the thermal spraying system according to the first embodiment, the surface treatment unit treats the surface of the lithium coating with H 2 O and an inert gas, or CO 2 , O 2 , H 2 O and an inert gas, or O 2, H 2 O, and the inert gas or,, CO 2, O 2, stabilized by exposure to H 2 O and an inert gas. In the surface treatment section, the partial pressure of H 2 O for exposing the surface of the lithium coating is set to 0.01 Torr or more. Thus, the thermal spray system can stabilize the surface of the lithium coating a few nanometers and keep the rest active. For this reason, the thermal spraying system can effectively realize the pre-repetition.
また、第1の実施形態に係る溶射システムは、第1室、第2室、第3室および第4室を備える。第1室には、溶射前の基材が巻き取られた状態で配置される。第2室には、溶射部が設けられる。第3室には、表面処理部が設けられる。第4室には、巻き取り部が設けられる。そして、基材は、第1室、第2室、第3室および第4室各々に形成されるスリットを通って第1室から前記第4室へ搬送される。このため、溶射システムは、溶射処理と表面処理とを別の室内で実行することができ、各処理の処理条件を容易に制御することができる。 溶 The thermal spraying system according to the first embodiment includes a first chamber, a second chamber, a third chamber, and a fourth chamber. In the first chamber, the base material before thermal spraying is arranged in a wound state. The second chamber is provided with a thermal spray section. A surface treatment unit is provided in the third chamber. The fourth chamber is provided with a winding unit. The substrate is transported from the first chamber to the fourth chamber through slits formed in each of the first, second, third, and fourth chambers. For this reason, the thermal spraying system can perform the thermal spraying process and the surface treatment in separate rooms, and can easily control the processing conditions of each process.
また、第1の実施形態に係る溶射システムは、第1室と第2室の間に設けられ、第2室よりも高圧雰囲気に維持される第1の作動排気室をさらに備える。このため、溶射システムは、第2室内の処理に用いられる粉末材料等が第1室に漏洩することを防止することができる。 溶 Further, the thermal spraying system according to the first embodiment further includes a first working exhaust chamber provided between the first chamber and the second chamber and maintained at a higher pressure atmosphere than the second chamber. For this reason, the thermal spray system can prevent the powder material used for the processing in the second chamber from leaking into the first chamber.
また、第1の実施形態に係る溶射システムは、第2室と第3室の間に設けられ、第2室よりも高圧雰囲気に維持される第2の作動排気室をさらに備える。このため、溶射システムは、第2室内の処理に用いられる粉末材料等が第3室に漏洩することを防止することができる。また、溶射システムは、第2室内の処理にリチウム粉末が用いられる際は、第3室内の処理に用いられる水と接触して発火することを防止することができる。 The thermal spraying system according to the first embodiment further includes a second working exhaust chamber provided between the second chamber and the third chamber and maintained at a higher pressure atmosphere than the second chamber. For this reason, the thermal spray system can prevent the powder material and the like used for the processing in the second chamber from leaking into the third chamber. Further, when the lithium powder is used for the processing in the second chamber, the thermal spraying system can prevent the fire from coming into contact with the water used for the processing in the third chamber.
また、第1の実施形態に係る溶射システムは、第3室と第4室の間に設けられ、第3室よりも高圧雰囲気に維持される第3の作動排気室をさらに備える。このように、溶射システムは、各室の状態を個別に制御して処理を実行することができる。また、溶射システムは、各室の内部雰囲気が混ざりあうことを防止することができる。 The thermal spray system according to the first embodiment further includes a third working exhaust chamber provided between the third chamber and the fourth chamber and maintained in a higher-pressure atmosphere than the third chamber. In this manner, the thermal spraying system can execute processing by individually controlling the state of each chamber. Further, the thermal spray system can prevent the internal atmospheres of the respective chambers from being mixed.
また、第1の実施形態にかかる溶射システムは、溶射処理と表面処理とを別室で実行する。このため、炭酸リチウムおよび酸化リチウムが過度に生成されて、リチウム二次電池の効率向上に寄与する活性のリチウム金属の絶対量が減少することがない。また、表面安定化のために供給されるガスが室内に残留して活性のリチウム金属の絶対量を減少させることがない。また、表面安定化のために供給されるガスを、溶射処理のために排気する必要がなく、スループットの低下を抑制することができる。 溶 In addition, the thermal spraying system according to the first embodiment executes the thermal spraying process and the surface treatment in separate rooms. For this reason, lithium carbonate and lithium oxide are not generated excessively, and the absolute amount of active lithium metal that contributes to the improvement of the efficiency of the lithium secondary battery does not decrease. In addition, the gas supplied for stabilizing the surface does not remain in the room and does not reduce the absolute amount of active lithium metal. Further, the gas supplied for stabilizing the surface does not need to be exhausted for the thermal spraying process, so that a decrease in throughput can be suppressed.
<第2の実施形態>
第1の実施形態に係る溶射システム100は、基材Wの第1の表面上に溶射による被膜を形成するものとした。これに限らず、溶射システム100は、基材Wの第1および第2の表面上に溶射による被膜を形成するように構成してもよい。
<Second embodiment>
The
図6A、図6Bおよび図6Cは各々、第2の実施形態に係る溶射システムの構成例1乃至構成例3を示す図である。 6A, 6B, and 6C are diagrams illustrating Configuration Examples 1 to 3 of the thermal spraying system according to the second embodiment.
図6Aに示す溶射システム100Aは、ローダ室1Aと、第1の差動排気室2Aと、第1の溶射処理室3Aと、第2の差動排気室4Aと、第1の表面処理室5Aと、第2の溶射処理室6Aと、第2の表面処理室7Aと、第4の差動排気室8Aと、を備える。各部の構成および機能は、第1の実施形態と同様である。
6A includes a loader chamber 1A, a first
ただし、図6Aに示す溶射システム100Aにおいては、基材Wの第1の表面が第1の溶射処理室3Aおよび第1の表面処理室5Aにおいて処理された後、基材Wの第2の表面が第2の溶射処理室6Aおよび第2の表面処理室7Aにおいて処理される。このため、図6Aの溶射システム100Aは、2つの溶射処理室(第1の溶射処理室3A、第2の溶射処理室6A)と2つの表面処理室(第1の表面処理室5A、第2の表面処理室7A)を備える。そして、第1の溶射処理室3Aと第2の溶射処理室6Aとは二階建て構造に配置されている。また、図6Aの溶射システム100Aにおいては、ローダ室とアンローダ室とを一つにまとめたローダ室1Aが設けられている。溶射システム100Aにおいては、第1の表面処理室5A内で基材Wの搬送方向を反転させ、第2の表面が上方を向くように基材Wが搬送される。
However, in the
なお、図6Aの例では、第2の差動排気室4Aは、第1の表面処理室5Aに搬入される基材Wおよび第1の表面処理室5Aから搬出される基材Wの双方が通過する。ただし、これに限らず、第1の表面処理室5Aに搬入される基材Wが通過する差動排気室と、第1の表面処理室5Aから搬出される基材Wが通過する差動排気室とを別個に設けてもよい。
In the example of FIG. 6A, the second
図6Bに示す溶射システム100Bは、ローダ室1Bと、第1の差動排気室2Bと、溶射処理室3Bと、第2の差動排気室4Bと、表面処理室5Bと、アンローダ室6Bと、を備える。図6Bに示す溶射システム100Bは、基材Wの第1の表面および第2の表面の双方を同時に処理するよう構成される。ローダ室1Bから搬送される基材Wは、溶射処理室3Bにおいて、基材Wの搬送経路を2方向から挟むように配置された溶射部31Bの間を通過する。このとき、基材Wの第1の表面および第2の表面の双方に被膜が形成される。そして、基材Wは、第2の差動排気室4Bを通過した後、表面処理室5Bに入り、同時に第1の表面および第2の表面上の被膜の表面処理が実現される。なお、図6Bの例では表面処理室5Bの後段に差動排気室を配置していないが、差動排気室を配置するよう変形してもよい。また、図6Bの例では、表面処理室5B内にガイドローラを設置して基材Wの搬送方向を制御している。ただし、基材W上の被膜品質に影響する場合は、表面処理室5B内で被膜表面が安定化した後に基材Wがガイドローラに接触するよう、ガイドローラの位置を変更してもよい。
The
図6Cに示す溶射システム100Cは、ローダ室1C、第1の差動排気室2C、第1の溶射処理室3C、第2の差動排気室4C、第1の表面処理室5Cを備える。さらに溶射システム100Cは、第3の差動排気室6C、第2の溶射処理室7C、第4の差動排気室8C、第2の表面処理室9C、アンローダ室10Cを備える。図6Cの溶射システム100Cが備える構成要素は、図6Aに示す溶射システム100Aと概ね同様であるが、2階建て構造とする部分を減少させている。なお、図6Cの例においても、第2の表面処理室9Cの後段に差動排気室を配置してもよい。
溶 The
このように、実施形態に係る溶射システムは、各室の配置を工夫することによって様々な構造の建造物に配置できる。 Thus, the thermal spray system according to the embodiment can be arranged in buildings having various structures by devising the arrangement of each room.
<第3の実施形態>
上記実施形態に係る溶射システムはさらに、溶射処理時の熱による基材Wへのダメージを抑制するための冷却機構を備えてもよい。以下に、第3の実施形態として、冷却機構34を備える溶射システム100Dについて説明する。
<Third embodiment>
The thermal spray system according to the above embodiment may further include a cooling mechanism for suppressing damage to the base material W due to heat during thermal spraying. Hereinafter, as a third embodiment, a
図7は、第3の実施形態に係る溶射システム100Dが備える冷却機構34について説明するための図である。なお、第3の実施形態に係る溶射システム100Dは、溶射処理室3D内で溶射処理により発生する熱の影響を抑制する冷却機構34を備える以外は、第1の実施形態に係る溶射システム100と同様の構成である。このため、第1の実施形態と同様の構成要素は同様の参照符号で表示し詳細な説明および/または図示を省略する。
FIG. 7 is a diagram for explaining a
図7に示す冷却機構34は、冷却ローラ35と、ガイドローラ36と、冷媒供給部37と、を備える。
冷却 The
冷却ローラ35は、溶射処理室3D内の溶射部31の噴射口の下方かつ、基材Wの搬送経路上に配置される。冷却ローラ35は、冷媒が流れる冷媒流路35Aを内部に有する。冷却ローラ35は、ローダ室1から巻き出される基材Wを搬送可能な幅および径に形成される。また、冷却ローラ35の径は、後述する冷却条件を満足する大きさに形成される。
(4) The cooling
ガイドローラ36は、溶射処理室3D内の基材Wの搬送経路上に配置される。ガイドローラ36は、基材Wの搬送経路上において冷却ローラ35よりもローダ室1側に配置される。ガイドローラ36は、冷却ローラ35に基材Wが到達する前に、基材Wの搬送方向を変更することにより、冷却ローラ35上での基材Wの搬送距離を増加させる。たとえば、図7に示すように、ガイドローラ36は、冷却ローラ35よりも第2の差動排気室4に近い位置に配置される。なお、ガイドローラ36を設けなくても、冷却ローラ35上での基材Wの搬送距離が後述する冷却条件を満足できる場合にはガイドローラ36を設けなくてもよい。また、ガイドローラ36と冷却ローラ35との相対的位置関係は特に限定されない。また、図7には一つのガイドローラ36を図示するが、ガイドローラ36の数は特に限定されない。冷却ローラ35上での基材Wの搬送距離を調整するために、任意の数のガイドローラ36を配置することができる。
The
冷媒供給部37は、冷却ローラ35の冷媒流路35Aに冷媒を供給する。冷媒供給部37の具体的な構成は特に限定されない。また、冷媒供給部37が供給する冷媒の種類は特に限定されず、たとえば、予め定められた温度に調整された水道水であってもよい。
The
図7を参照し、溶射システム100Dにおける基材Wの搬送について説明する。溶射システム100Dにおいては、ローダ室1内の巻出し部11から巻き出された基材Wは、第1の作動排気室2を通過して溶射処理室3Dに入る。溶射処理室3Dでは、基材Wはまずガイドローラ36の下方から上方へと巻き回される。このとき、ローダ室1からアンローダ室7へ向かう搬送方向を正方向とすると、ガイドローラ36に巻き回された基材Wの搬送方向は正方向と反対の方向となる。その後、基材Wは、ガイドローラ36よりも上方に配置される冷却ローラ35の下方から上方へと巻き回されて再び搬送方向が正方向となる。そして、基材Wは溶射処理室3Dから第2の差動排気室4、表面処理室5、第3の作動排気室6を通過してアンローダ室7内の巻き取り部71に巻き取られる。
搬 送 With reference to FIG. 7, conveyance of the base material W in the
冷却ローラ35上を基材Wが搬送されるときに、冷却ローラ35の上方に配置された溶射部31により基材W上に溶融した粉末材料が噴出され被膜が形成される。このとき、基材Wの表面は溶融した粉末材料によって加熱される。第3の実施形態では、溶射処理中、冷却ローラ35内に冷媒を流すことで、冷却ローラ35上の基材Wの温度上昇が抑制される。
(4) When the base material W is conveyed on the cooling
<冷却条件>
本発明者らは、溶射システム100Dにおいて基材Wの温度上昇を抑制するための冷却条件について検討するため実験を行い、以下の知見を得た。
(1)冷却ローラ35の径が大きいほど熱容量が大きくなるため、冷却ローラ35上を搬送される基材Wの温度を低下させることができる。
(2)冷却ローラ35と冷却ローラ35上を搬送される基材Wとの接触面積が大きいほど、基材Wの温度の上昇幅を抑制することができる。
(3)冷却ローラ35内を流れる冷媒の量が多いほど抜熱量が大きくなり、基材Wの温度の上昇幅を抑制することができる。
(4)冷却ローラ35に流す冷媒の温度変更により、基材Wの温度は変化するが、基材Wの温度の上昇幅は変化しない。
<Cooling conditions>
The present inventors conducted experiments to examine cooling conditions for suppressing a temperature rise of the base material W in the
(1) Since the heat capacity increases as the diameter of the cooling
(2) The larger the contact area between the cooling
(3) The greater the amount of the refrigerant flowing in the cooling
(4) The temperature of the base material W changes due to the change in the temperature of the coolant flowing through the cooling
(実験1:冷媒流量が冷却性能に与える影響)
実験1では、基材Wの搬送速度を固定して冷媒の流量を変化させ、冷媒の流量変化による影響を調べた。具体的には、搬送速度および流量を以下のように設定した。
・基材Wの搬送速度:0.1m/分
・冷媒の流量:2L/分、5L/分、10L/分
この結果、冷媒の温度に関わらず、基材Wの温度は溶射処理が開始してから20~30分程度で安定し、その後安定することが分かった。たとえば冷媒の流量が10L/分の場合は、2L/分の場合と比較して約5℃~7℃低い温度で基材Wの温度が安定した。このことから、冷媒の流量が大きいほど、低温で基材Wの温度を安定させることができるが、冷媒の流量に関わらず基材Wの温度が安定することが分かった。
(Experiment 1: Effect of refrigerant flow rate on cooling performance)
In
-Transfer speed of the substrate W: 0.1 m / min-Flow rate of the refrigerant: 2 L / min, 5 L / min, 10 L / min As a result, regardless of the temperature of the refrigerant, the temperature of the substrate W starts the thermal spraying process. It was found that it was stabilized in about 20 to 30 minutes after that, and then stabilized. For example, when the flow rate of the refrigerant was 10 L / min, the temperature of the base material W was stabilized at a temperature lower by about 5 ° C. to 7 ° C. than in the case of 2 L / min. From this, it was found that the larger the flow rate of the refrigerant, the more stable the temperature of the base material W at a low temperature, but the more stable the temperature of the base material W regardless of the flow rate of the refrigerant.
(実験2:基材搬送速度が冷却性能に与える影響)
実験2では、基材Wの搬送速度が冷却性能に与える影響を計測した。具体的には、以下の条件で実験2を行った。
・基材Wの搬送速度:1m/分、3m/分、5m/分、10m/分、20m/分
・冷媒の流量:2L/分、5L/分、10L/分
そして、冷却ローラ35上で基材Wを搬送しつつ、ヒータにより基材Wを加熱した。加熱開始から5分経過後の基材Wの温度を計測した。実験においては、基材Wの搬送速度が速い(たとえば20m/分)場合、基材Wの運動に伴い溶射部31から発せられる熱風が下流側に流れることが分かった。また、このために、基材Wの温度が下流側で高くなることが分かった。そこで、基材Wの搬送に伴う熱風の影響を防止するために熱風が下流に流れない機構を追加してさらに実験を行った。この結果、基材Wの搬送速度が速いほど、かつ冷媒の流量が多いほど、基材Wの温度が低くなるという結果が得られた。
(Experiment 2: Influence of substrate transfer speed on cooling performance)
In
-Transport speed of the substrate W: 1 m / min, 3 m / min, 5 m / min, 10 m / min, 20 m / min-Flow rate of refrigerant: 2 L / min, 5 L / min, 10 L / min The substrate W was heated by the heater while transporting the substrate W. Five minutes after the start of heating, the temperature of the substrate W was measured. In the experiment, it was found that when the transport speed of the base material W was high (for example, 20 m / min), the hot air emitted from the
(実験3:冷媒の温度が冷却性能に与える影響)
実験3では、冷媒の温度を変えて基材Wの温度を計測した。
・基材Wの搬送速度:1m/分、5m/分、20m/分
・冷媒の温度:20℃、60℃
この結果、冷媒の温度が低いほど、基材Wの温度も低くなることが分かった。ただし、時間経過に伴う温度変化の挙動は、冷媒の温度によっては特に違いが認められなかった。このため、基材Wの温度は、冷媒の温度により調整可能であることが分かった。
(Experiment 3: Effect of refrigerant temperature on cooling performance)
In
・ Transport speed of the substrate W: 1 m / min, 5 m / min, 20 m / min ・ Temperature of refrigerant: 20 ° C., 60 ° C.
As a result, it was found that the lower the temperature of the refrigerant, the lower the temperature of the substrate W. However, there was no particular difference in the behavior of the temperature change with time depending on the temperature of the refrigerant. For this reason, it turned out that the temperature of the base material W can be adjusted by the temperature of the refrigerant.
以上から、溶射処理による温度の上昇幅と、基材Wの望ましい温度とにあわせて、冷却ローラ35の直径、冷却ローラ35と基材Wとの接触持続距離(搬送距離)、冷媒の流量、基材Wの搬送速度を冷却条件として予め設定すればよい。設定した冷却条件が満足されている場合には、長時間溶射処理を継続しても基材Wの温度は上昇しない。
From the above, the diameter of the cooling
このように冷却条件を設定することで、冷媒として市水を使用した場合でも十分な冷却性能を実現でき、所望の温度での基材Wの処理を実現できる。 冷却 By setting the cooling conditions in this way, sufficient cooling performance can be realized even when city water is used as the refrigerant, and processing of the base material W at a desired temperature can be realized.
今回開示された実施形態は全ての点で例示であって制限的なものではないと考えられるべきである。実に、上記した実施形態は多様な形態で具現され得る。また、上記の実施形態は、添付の請求の範囲及びその趣旨を逸脱することなく、様々な形態で省略、置換、変更されてもよい。 実 施 The embodiments disclosed this time are to be considered in all respects as illustrative and not restrictive. Indeed, the above embodiments can be embodied in various forms. The above embodiments may be omitted, replaced, or modified in various forms without departing from the scope and spirit of the appended claims.
100,100D 溶射システム
1 ローダ室(第1室)
11 巻出し部
12 吸排気口
13 吸排気部
2 第1の差動排気室
21 吸気口
22 ガス供給部
23 排気口
24 排気部
3,3D 溶射処理室(第2室)
31 溶射部
32 排気口
33 真空ポンプ
34 冷却機構
35 冷却ローラ
35A 冷媒流路
36 ガイドローラ
37 冷媒供給部
4 第2の差動排気室
41 吸気口
42 ガス供給部
43 排気口
44 排気部
5 表面処理室(第3室)
50 表面処理部
51 ガス供給部
52 ガス排出部
53 排気部
54 真空ポンプ
6 第3の差動排気室
61 吸気口
62 ガス供給部
63 排気口
64 排気部
7 アンローダ室(第4室)
71 巻き取り部
72 吸排気口
73 吸排気部
8 制御装置
81 制御部
82 操作部
83 記憶部
W 基材
100,100D
DESCRIPTION OF
71
Claims (10)
前記被膜の表面を安定化させるよう構成される表面処理部と、
前記被膜の表面の安定化の後、前記基材を巻き取るよう構成される巻き取り部と、
を備える溶射システム。 A thermal spray portion configured to form a coating on the first surface of the substrate by thermal spraying the powder material;
A surface treatment unit configured to stabilize the surface of the coating,
After stabilization of the surface of the coating, a winding unit configured to wind the substrate,
Thermal spraying system comprising:
前記表面処理部は、前記リチウム被膜の表面を酸化リチウム、炭酸リチウムまたは酸化リチウムと炭酸リチウムの混合物に変化させることにより安定化させる、
請求項1に記載の溶射システム。 The spraying unit sprays a lithium powder material to form a lithium coating on the first surface of the base material,
The surface treatment unit stabilizes the surface of the lithium coating by changing the surface of the lithium coating to lithium oxide, lithium carbonate, or a mixture of lithium oxide and lithium carbonate,
The thermal spray system according to claim 1.
前記溶射部が設けられる第2室と、
前記表面処理部が設けられる第3室と、
前記巻き取り部が設けられる第4室と、
を備え、
前記基材は、前記第1室、前記第2室、前記第3室および前記第4室各々に形成されるスリットを通って前記第1室から前記第4室へ搬送される、請求項1から4のいずれか1項に記載の溶射システム。 A first chamber in which the base material before thermal spraying is arranged in a wound state,
A second chamber in which the thermal spray section is provided;
A third chamber provided with the surface treatment unit;
A fourth chamber in which the winding section is provided;
With
The said base material is conveyed from the said 1st chamber to the said 4th chamber through the slit formed in each of the said 1st chamber, the said 2nd chamber, the said 3rd chamber, and the said 4th chamber. The thermal spraying system according to any one of claims 1 to 4.
前記被膜の表面を安定化させる表面処理工程と、
前記被膜の表面の安定化の後、基材を巻き取る巻き取り工程と、
を含む溶射方法。 Spraying a powder material to form a coating on the first surface of the substrate,
A surface treatment step of stabilizing the surface of the coating,
After stabilization of the surface of the coating, a winding step of winding the substrate,
Thermal spraying method including.
前記リチウム被膜の表面を酸化リチウム、炭酸リチウムまたは酸化リチウムと炭酸リチウムの混合物に変化させることにより安定化し、
前記リチウム被膜の安定化の後、前記基材を巻き取る
ことを含むリチウム二次電池の製造方法。 Forming a lithium coating on the first surface of the substrate by spraying the lithium powder material;
Stabilizing by changing the surface of the lithium coating to lithium oxide, lithium carbonate or a mixture of lithium oxide and lithium carbonate,
A method for manufacturing a lithium secondary battery, comprising winding the substrate after stabilizing the lithium coating.
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