[go: up one dir, main page]

WO2013125853A1 - Sodium secondary battery and method for manufacturing sodium secondary battery - Google Patents

Sodium secondary battery and method for manufacturing sodium secondary battery Download PDF

Info

Publication number
WO2013125853A1
WO2013125853A1 PCT/KR2013/001338 KR2013001338W WO2013125853A1 WO 2013125853 A1 WO2013125853 A1 WO 2013125853A1 KR 2013001338 W KR2013001338 W KR 2013001338W WO 2013125853 A1 WO2013125853 A1 WO 2013125853A1
Authority
WO
WIPO (PCT)
Prior art keywords
positive electrode
space
secondary battery
active material
sodium
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/KR2013/001338
Other languages
French (fr)
Korean (ko)
Inventor
김정수
김영솔
채제현
선희영
고원상
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SK Innovation Co Ltd
Ceramatec Inc
Original Assignee
SK Innovation Co Ltd
Ceramatec Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SK Innovation Co Ltd, Ceramatec Inc filed Critical SK Innovation Co Ltd
Priority to KR1020147023654A priority Critical patent/KR102047761B1/en
Publication of WO2013125853A1 publication Critical patent/WO2013125853A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/36Accumulators not provided for in groups H01M10/05-H01M10/34
    • H01M10/38Construction or manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/36Accumulators not provided for in groups H01M10/05-H01M10/34
    • H01M10/39Accumulators not provided for in groups H01M10/05-H01M10/34 working at high temperature
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to a sodium secondary battery and a method for manufacturing the same, and easy to process, to a method for manufacturing a sodium secondary battery that is easy to control the thickness of the electrode and the content of the active material.
  • a battery may be classified into a disposable primary battery and a rechargeable battery that can be charged many times.
  • the secondary battery has been popularized as an essential energy source of portable electronic devices such as laptops, camcorders, and mobile phones in that it can be used many times.
  • This secondary battery is composed of a negative electrode, a positive electrode, an electrolyte and a current collector.
  • a reduction reaction caused by electrons generated at the negative electrode occurs, and the current collector supplies electrons generated from the negative electrode to the positive electrode active material when the battery is discharged, or electrons supplied from the positive electrode to the negative electrode active material at the time of charging. do.
  • sodium secondary batteries use molten metal sodium (Na) as the cathode, sulfur (S) as the anode, and the cathode and the cathode are selective for sodium ions, as in Korean Patent Publication No. 19960002926. It is configured to be segregated into a solid electrolyte tube made of alumina or ceramic having permeability, so that sodium ions can pass through the solid electrolyte tube.
  • Sodium secondary battery has excellent competitiveness in terms of supply and demand for materials and manufacturing cost by using rich sodium on the earth, and has the advantage of making a large capacity battery into a simple structure compared to lithium ion batteries.
  • the sodium secondary battery has a similar energy density as that of the conventional secondary battery, and is inexpensive, and can be manufactured with a long power conservation time. Therefore, when used as a secondary battery for renewable energy storage such as solar or wind power, a large capacity of electric power can be used. It is emerging as a next-generation storage medium that can be stored efficiently.
  • An object of the present invention is to provide a sodium secondary battery that prevents peeling or desorption of a positive electrode active material layer from a current collector, free of battery design according to capacity, and can be miniaturized and easy to manufacture.
  • An object of the present invention is to provide a method of manufacturing a sodium secondary battery that can easily control the thickness of a cathode active material, a method of manufacturing a small size cathode of a large-capacity battery, and can easily control the thickness of an electrode and the content of an active material.
  • a method of manufacturing a sodium secondary battery according to the present invention includes the steps of: a) inserting a current collector into a cathode space partitioned from a cathode space by a sodium ion conductive solid electrolyte; And b) injecting an active material containing a positive electrode active material into the positive electrode space into which the current collector is inserted.
  • step b) comprises the steps of b1) injecting a particulate phase containing a cathode active material and conductive particles into the cathode space; And injecting a binder solution containing a viscosity modifier and a binder into the anode space and drying the same.
  • step b3) a slurry containing a positive electrode active material, a conductive particle, a viscosity regulator and a binder in the positive electrode space and drying; Can be.
  • step a) is a cylindrical metal housing, one end of which is sealed in one end and the other end is open, located inside the metal housing, Providing a sodium ion conductive solid electrolyte tube, a safety tube, and a wicking tube on which molten sodium is loaded, the anode space having a concentric structure sequentially positioned from the outer side to the inner side, wherein the anode space is disposed between the solid electrolyte tube and the metal housing. It may be a space of.
  • the current collector may be wound to have a concentric structure with the metal housing.
  • the current collector may be in the form of a foam (foam), film (film), mesh (mesh), felt (felt) or porous foil (perforated film) shape .
  • the current collector may be one or more selected from carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite and graphene.
  • the conductive particles may include carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene or a mixture thereof.
  • the particulate form may contain 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material.
  • the cathode active material may include nickel hydroxide (Ni (OH) 2 ).
  • the binder solution may have a viscosity of 0.01 P to 10,000 P.
  • the viscosity of the slurry may be 0.01 P to 10,000 P.
  • the viscosity modifier is carboxymethyl cellulose (CMC; carboxymethyl cellulose), methyl cellulose (methylcellulose), ethyl cellulose (ethyl cellulose) and hydroxypropyl methyl cellulose (HPMC) at least one selected from hydroxypropyl methylcellulose
  • the binder may be polytetrafluoroethylene (PTFE; polytetrafluoroethylene), polyvinyl alcohol (PVA), polyolefine, polyethylene oxide (PEO), or polyethylen oxide (PEO). Mixtures thereof.
  • the binder solution may contain a binder of 0.1 to 20% by weight.
  • the slurry is based on 100 parts by weight of the positive electrode active material, 0.1 to 20 parts by weight of conductive particles, 0.1 to 10 parts by weight of the viscosity regulator and 0.1 to 20 parts by weight of the binder It may contain.
  • step b) injecting an electrolyte into the anode space; may be further performed.
  • Sodium secondary battery according to the present invention comprises a sodium ion conductive solid electrolyte partitioning the negative electrode space and the positive electrode space; A sodium-containing cathode located in the cathode space; And a current collector positioned in the positive electrode space and a particulate form filling the positive electrode space in which the current collector is located, wherein the particulate includes a positive electrode containing a positive electrode active material.
  • the particulate form filling the positive electrode space may be bound by drying of a binder injected into the positive electrode space in a solution form.
  • the particulate may further include conductive particles.
  • the particulate form may contain 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material.
  • the cathode active material may include nickel hydroxide (Ni (OH) 2 ).
  • the negative electrode may be molten sodium.
  • the particulate may fill the positive electrode space to a height corresponding to the level of molten sodium in the negative electrode space.
  • the sodium secondary battery is located in the cylindrical metal housing, the metal housing, the sodium ion conductive solid electrolyte is located with a concentric structure sequentially from the outside of the metal housing to the inside A tube, a safety tube, and a wicking tube carrying molten sodium are included, and the anode space may be a space between the solid electrolyte tube and the metal housing.
  • the empty space of the anode space filled with particulates may be filled with an electrolyte solution.
  • the particulate and the binder solution is added sequentially or integrated into a slurry to produce a positive electrode in the positive electrode space itself, as a slurry
  • the process is simplified, the required investment costs are reduced, and the process input manpower is also reduced.
  • the sodium secondary battery according to the present invention not only frees the design of the battery, but also prevents peeling or detaching of the current collector and the positive electrode active material layer, and has an advantage of controlling the capacity of the battery by simply changing the size of the positive electrode space.
  • FIG. 1 is a cross-sectional view showing an example of a battery structure in a manufacturing method according to an embodiment of the present invention
  • FIG. 2 is a cross-sectional view showing an example of a manufacturing method according to an embodiment of the present invention
  • FIG. 3 is a process chart showing an example of a manufacturing method according to an embodiment of the present invention.
  • FIG. 4 is a process chart showing another example of a manufacturing method according to an embodiment of the present invention.
  • FIG. 5 is a cross-sectional view of a secondary battery according to an exemplary embodiment of the present invention.
  • a method of manufacturing a sodium secondary battery according to the present invention includes the steps of: a) inserting a current collector into a cathode space partitioned from a cathode space by a sodium ion conductive solid electrolyte; And b) injecting an active material containing a positive electrode active material into the positive electrode space into which the current collector is inserted.
  • step b) comprises the steps of b1) injecting a particulate phase containing a cathode active material and conductive particles into the cathode space; And injecting a binder solution containing a viscosity modifier and a binder into the anode space and drying the same.
  • the current collector is introduced into a positive electrode space partitioned by a sodium ion conductive solid electrolyte, separated from the positive electrode active material, and then the current collector and the positive electrode in the positive electrode space.
  • a sodium secondary battery is manufactured by binding an active material.
  • the particles and the binder including the positive electrode active material are sequentially or simultaneously introduced into the positive electrode space into which the current collector is inserted, thereby binding between particles including the positive electrode active material and between the particles and the current collector.
  • the particles and the binder including the positive electrode active material are sequentially or simultaneously introduced into the positive electrode space into which the current collector is inserted, thereby binding between particles including the positive electrode active material and between the particles and the current collector.
  • the prepared positive electrode is not wound, molded and / or cut and inserted into a battery, Since the anode is manufactured directly in the anode space of the structure itself, the anode can be manufactured in a very simple process compared to the conventional process according to the order of the slurry production, application, drying, rolling, winding, and insertion into the anode space.
  • a battery of a whole new system is designed by different kinds of positive electrode active materials, or a structure in which a plurality of positive electrodes are stacked to design a desired level of capacity while using the same positive electrode active materials. There was a limit to which a change must be made.
  • the capacity of the battery can be changed only through an extremely simple method of changing the size of the anode space or controlling the total amount of particulates injected into the anode space. That is, the manufacturing method according to the present invention is extremely easy and free to design the battery according to the capacity, only the separation distance between the current collector and the current collector in the positive electrode space and / or the case (including a conductive case) for separating the battery from the outside By controlling the separation distance between the) and the current collector, the thickness of the positive electrode active material layer can be adjusted, it is very easy to control the thickness of the positive electrode active material layer, there is an advantage that a large-capacity battery can be manufactured in a small size.
  • step b) comprises the steps of b1) injecting a particulate phase containing a positive electrode active material and conductive particles into the positive electrode space; And b2) injecting and drying a binder solution containing a viscosity modifier and a binder into the anode space.
  • step b) is a step of b3) adding a slurry containing a positive electrode active material, a conductive particle, a viscosity control agent and a binder in the positive electrode space and drying; It may include.
  • the current collector is introduced into the positive electrode space, the particle input including the positive electrode active material and the binder solution containing the binder are sequentially performed, or the current collector is injected into the positive electrode space and the positive electrode active material and the binder are sequentially added. It may comprise the step of the input of the slurry comprising a sequentially.
  • the particulate phase may further contain conductive particles together with the positive electrode active material, which serves to reduce the resistance between the current collector and the positive electrode active material, that is, to reduce the internal resistance of the battery. Can play a role.
  • the particulate form may contain 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material.
  • the weight ratio of the conductive particles to the positive electrode active material is a weight ratio in which a low resistance path can be uniformly formed between the positive electrode active material and the current collector without interfering with the positive electrode reaction generated in the positive electrode active material.
  • the thickness of the positive electrode active material layer is usually limited in order to secure stable formability (processability) of the positive electrode.
  • the amount of the positive electrode active material decreases as the conductors introduced to decrease the internal resistance of the battery decrease, so that the amount of the conductor and the positive electrode active material can only be adjusted to a level that appropriately decreases the resistance and ensures adequate capacity. .
  • the manufacturing method according to an embodiment of the present invention is to prepare a positive electrode (current collector and positive electrode active material) in the positive electrode space by packing a particulate containing a positive electrode active material in the positive electrode space, so that the positive electrode active material layer from the thickness constraint
  • the particulate phase may contain an amount of conductive particles that are determined primarily in consideration of the reduction in battery internal resistance. That is, compared with the prior art, the particulate form can freely contain an amount of conductive particles that can effectively reduce the internal resistance of the battery.
  • the average particle size (diameter) of the positive electrode active material may be 1 ⁇ m to 100 ⁇ m, the average particle size of the conductive particles may be 0.1 ⁇ m to 30 ⁇ m. If the average particle size of the positive electrode active material is too small, less than 1 ⁇ m, the specific surface area of the positive electrode active material becomes large, but there is a risk that the smooth input of the binding solution or the smooth input and stable contact of the electrolyte described below are impaired. There is a risk that a binder is required to degrade battery characteristics.
  • the average particle size of the positive electrode active material is too large to exceed 100 ⁇ m, there is a risk that the battery characteristics are deteriorated by the reduction of the specific surface area of the positive electrode active material.
  • the conductive particles form a low resistance path between the positive electrode active material particles, the positive electrode active material and the current collector to reduce the internal resistance of the battery, and the amount of the positive electrode active material filled by the conductive particles in the same volume of the positive electrode space is reduced.
  • the average particle size (diameter) of the positive electrode active material is 1 ⁇ m to 100 ⁇ m
  • the average particle size of the conductive particles may be 0.1 ⁇ m to 30 ⁇ m.
  • step b) after step b) is performed, more specifically, after step b2) or b3) is performed, c) injecting an electrolyte into the anode space; Can be.
  • the electrolyte serves to conduct sodium ions quickly and uniformly
  • the electrolyte salt (sodium salt) contained in the electrolyte may include hydroxide, borate, phosphate, or a mixture thereof.
  • the electrolyte salt may be sodium hydroxide (NaOH), trisodium phosphate (Na 3 PO 4 ), sodium pyrophosphate (Na 2 HPO 4 ), sodium metaborate (NaBO 2 ), borax (Na 2 B 4 O 7 ), Boric acid (H 3 BO 3 ) or mixtures thereof.
  • the electrolyte may include an aqueous or non-aqueous electrolyte, and the electrolyte may contain 2 to 50 wt% of an electrolyte salt.
  • i) injecting a negative electrode into the positive electrode space and the negative electrode space by a sodium ion conductive solid electrolyte i) injecting a negative electrode into the positive electrode space and the negative electrode space by a sodium ion conductive solid electrolyte; It may further include.
  • At least a sodium ion conductive solid electrolyte is injected into the sealed battery case, and the space inside the battery case is divided into a positive electrode space and a negative electrode space by a sodium ion conductive solid electrolyte. ; Injecting a cathode into the cathode space; Manufacturing a positive electrode in the positive electrode space through steps a) and b), optionally steps a), b) and c); And sealing the battery case.
  • At least a sodium ion conductive solid electrolyte is injected into the sealed battery case, and the space inside the battery case is divided into a positive electrode space and a negative electrode space by a sodium ion conductive solid electrolyte. ; Manufacturing a positive electrode in the positive electrode space through steps a) and b), optionally steps a), b) and c); Injecting a cathode into the cathode space; And sealing the battery case.
  • the negative electrode introduced into the negative electrode space is an electrode on which the negative electrode active material layer is formed on the negative electrode current collector, or a negative electrode such as rod-shaped conductive graphite on the negative electrode active material forming a liquid phase at a battery operating temperature
  • the current collector may be charged.
  • the cathode (cathode active material) may be metal sodium.
  • the positive electrode active material may be nickel hydroxide.
  • the step of applying a physical vibration to the anode space may be further performed.
  • the physical vibration can be any vibration as long as it causes a uniform and homogeneous filling of powder particles.
  • various physical vibrations such as an impact from an ultrasonic impact between a battery case and an external object, to an ultrasonic vibration. This can be used.
  • b1) a step of injecting a particulate phase containing a positive electrode active material and conductive particles into the anode space; And b2) injecting and drying a binder solution containing a viscosity modifier and a binder into the positive electrode space, and when the positive electrode is prepared, the binder solution binds the particles introduced into the particles and at the same time, the particles and the current collector. It can serve to bind.
  • the viscosity modifier contained in the binding solution may be a cellulose based at least one selected from carboxymethyl cellulose (CMC), methyl cellulose (methylcellulose), ethyl cellulose and hydroxypropyl methylcellulose (HPMC). .
  • CMC carboxymethyl cellulose
  • methylcellulose methylcellulose
  • HPMC hydroxypropyl methylcellulose
  • the binder contained in the binding solution may include polytetrafluoroethylene (PTFE), polyvinyl alcohol (PVA), polyolefine, polyethylene oxide (PEO) or a mixture thereof.
  • the binder contained in the binding solution serves to bind the particles and the particles and the current collector to each other with physical strength.
  • the binder solution may contain 0.1 to 20% by weight of the binder, the content of this binder does not interfere with the positive electrode reaction, does not interfere with the conduction of sodium ions, and after drying of the binder solution, even when a physically stable positive electrode is produced
  • the electrolyte may be added homogeneously.
  • the solvent of the binding solution may be a substance in which the viscosity modifier and binder described above are dissolved.
  • the viscosity modifier is carboxymethyl cellulose (CMC; carboxymethyl cellulose), methyl cellulose (methylcellulose), ethyl cellulose (ethyl cellulose) and hydroxypropyl methylcellulose (HPMC)
  • the binder may include polytetrafluoroethylene (PTFE; polytetrafluoroethylene), polyvinyl alcohol (PVA; polyvinyl alcohol), polyolefin (polyolefine), polyethylene oxide (PEO; polyethylen oxide) or a mixture thereof
  • the solvent of the slurry may be a substance in which a viscosity modifier and a binder are dissolved.
  • the slurry (active material slurry) is 0.1 to 0.1 parts based on 100 parts by weight of the positive electrode active material in terms of stable binding with the current collector, smooth and homogeneous packing, and easy ion transfer by the electrolyte solution injected into the positive electrode space after slurry drying. It may contain 20 parts by weight of conductive particles, 0.1 to 10 parts by weight of the viscosity regulator and 0.1 to 20 parts by weight of the binder, the viscosity regulator may be contained so that the slurry can have a viscosity of 0.01 P to 10,000 P at room temperature normal pressure.
  • the sodium secondary battery of the present invention and a method of manufacturing the same may include all structures of the sodium secondary battery in which the sealed case and the inner space of the sealed case are partitioned into a positive electrode space and a negative electrode space by a sodium ion conductive solid electrolyte. have.
  • the tubular structure may include a cell structure used in a conventional molten sodium sulfur battery, and may include a tubular structure in which the positive electrode is located at the center.
  • the sodium secondary battery to be manufactured may include a plate-like structure, which is a plate-shaped sodium ion conductive solid electrolyte is placed in a sealed case having an inner space, the inner space is the positive electrode space and the negative electrode space It includes a structure that is divided into compartments.
  • FIG. 1 is an example illustrating a method of manufacturing a sodium secondary battery according to an exemplary embodiment of the present invention. That is, FIG. 1 is a view illustrating an example of a battery structure partitioned into a positive electrode space and a negative electrode space by a sodium ion conductive solid electrolyte in a method of manufacturing a sodium secondary battery according to an embodiment of the present invention.
  • the metal housing 100 is positioned at the outermost side, the wicking tube 420 is positioned at the center thereof, and the metal housing 100 is disposed at the outer side of the metal housing 100 inside the metal housing 100.
  • the solid electrolyte tube 300, the safety tube 410, and the wicking tube 420 may be sequentially provided.
  • the solid electrolyte tube 300, the safety tube 410 and the wicking tube 420 has a concentric structure, to provide a battery structure provided inside the metal housing 100 Can be.
  • the metal housing 100 may include a cylindrical shape in which one end of both ends is sealed and the other end is open, and a cover (not shown) for sealing the open end of the metal housing 100 after the manufacture of the battery is completed. It may include.
  • a solid electrolyte tube 300 that selectively transmits sodium ions may be positioned adjacent to the metal housing 100.
  • the solid electrolyte of the solid electrolyte tube 300 includes a solid electrolyte conventionally used in the battery field for the selective conduction of sodium ions.
  • the wicking tube 420 positioned at the innermost, ie central portion of the metal housing 100 may have a tube shape having a through hole formed at a lower end thereof, and the safety tube 410 is a wicking tube. Located outside the 420 may have a predetermined distance and have a structure surrounding the wicking tube (420).
  • the negative electrode active material including molten sodium may be provided inside the wicking tube 420, and fills an empty space between the wicking tube 420 and the safety tube 410 through a through hole formed under the wicking tube 420. It can have
  • the dual structure of the wicking tube 420 and the safety tube 410 prevents a violent reaction between the positive electrode active material and the negative electrode active material when the solid electrolyte tube 300 breaks, and maintains a constant level of molten sodium even during discharge due to capillary force. It is a sustainable structure.
  • FIG. 1 illustrates an example of a battery structure including a cylindrical metal housing, a tubular solid electrolyte, a tubular safety tube, and a wicking tube
  • the present invention provides a technique for directly manufacturing a cathode in an anode space.
  • the present invention is not limited by the shape, material or size of the battery structure.
  • FIG. 2 is a cross-sectional view of a method for manufacturing a sodium secondary battery according to an embodiment of the present invention. After the battery structure shown in FIG. 1 is provided, a space between the metal housing 100 and the solid electrolyte tube 300 is provided. An example of the step of forming an anode in the phosphorous anode space 1 is shown in detail.
  • the slurry containing the positive electrode active material is not wound and inserted into the current collector in the positive electrode space 1 of the provided battery structure, and the positive electrode active material is not attached (or fixed).
  • the current collector itself active material unformed current collector
  • the current collector may be in the form of a foam, film, mesh, felt or porous foil, and the current collector may be carbon, nickel, titanium, yttrium, calcium, chromium, One or more may be selected from cobalt, zinc, graphite and graphene.
  • the current collector may be introduced into the anode space 1 in a rolled state in order to effectively collect electric charges while widening the reaction area of the electrode, and the current collector may be wound and input to have a concentric structure with the metal housing 100.
  • the present invention may not be limited by the shape of the current collector.
  • the manufacturing method according to an embodiment of the present invention which winds up a current collector that is not provided with an active material and then inserts it into the positive electrode space, may prevent desorption between the active material and the current collector generated during winding, and a large amount of positive electrode active material on the current collector This has the advantage of being suitable for the manufacture of large capacity sodium batteries to be provided.
  • the cathode active material in the case of using a single layer current collector for manufacturing a large capacity sodium battery having a capacity of 500 Ah or more, it is necessary to coat the cathode active material to a thickness of 250 mm or more. In this case, the shape of the electrode itself becomes thick and dried. Difficulties arise in machining the electrodes. That is, when the current collector with a thick positive electrode active material layer is processed into a dried shape, peeling or desorption of the positive electrode active material layer occurs, the mechanical strength is lowered, a lot of energy is consumed during processing, and the electrode is dried. There is a problem that the stability is not maintained.
  • the positive electrode active material generated during rolling of the electrode as the wound current collector is put into the positive electrode space Free from peeling or desorption of the layer, the material, thickness and shape of the current collector can be determined in consideration of the mechanical ductility, mechanical strength, and electrical properties of the current collector, thereby making it easier to manufacture the battery, and only the anode space.
  • the thickness of the positive electrode active material can be controlled by adjusting the size and / or the winding interval of the current collector, and the mass production process is simplified, thereby reducing the investment cost and the production cost.
  • the number of windings and the winding interval (D of FIG. 2) of the current collector may be designed in consideration of the capacity of the battery, and the size of the positive electrode space 1 also takes into account the capacity of the battery. Of course, it can be designed.
  • FIG. 3 is an example of a process diagram in which the above-described battery structure is provided, and a metal current collector is introduced into the positive electrode space 1, and then the step of introducing a particulate phase containing the positive electrode active material is shown in detail.
  • the positive electrode space 1 into which the current collector 200 is introduced Into the particulate phase containing the positive electrode active material and the conductive particles, and then a step of adding a binder solution containing a viscosity modifier and a binder into the positive electrode space (1) in which the particulate phase is added and dried.
  • the positive electrode active material contained on the particles may include nickel hydroxide (Ni (OH) 2 ), and the conductive particles, which are conductive particles, may be used as long as the conductive particles are commonly used for the positive electrode of a secondary battery, particularly a nickel hydrogen battery.
  • the conductive particles may contain carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene, or mixtures thereof.
  • the particulate phase contains a mixed powder of the positive electrode active material particles and the conductive particles, the conductive particles are anodic reaction (Ni (OH) 2 ⁇ NiOOH) is generated It reduces the resistance between the positive electrode active material (nickel hydroxide) and the current collector.
  • the particulate matter is injected into the positive electrode space 1 into which the wound current collector 200 is inserted, and between the wound current collector, the current collector 200 and the metal housing 100.
  • the space between the) and between the solid electrolyte 300 and the metal housing 100 may be filled with particulates.
  • the thickness of the active material coated on the current collector can be controlled.
  • the winding interval of the current collector may be changed in consideration of the capacity of the battery.
  • the winding interval of the current collector is 0.01 to 5 mm.
  • the particulate is introduced into the anode space 1 in a dry powder state, it is formed in the empty space between the cathode active material particles and the conductive particles contained in the powder, between the particles Empty spaces may be filled with the binding solution.
  • the volume at which the binding solution is filled can be controlled by the average particle size of the particulates.
  • the average particle size (diameter) of the positive electrode active material contained on the particles may be 1 ⁇ m to 100 ⁇ m, and the average particle size of the conductive particles may be 0.1 ⁇ m to 30 ⁇ m.
  • the size of the positive electrode active material particles and the conductive particles described above is uniformly mixed between the positive electrode active material and the conductive particles, and when the particle is stably attached to the current collector 200 by the binding solution when the anode active material 1 is injected into the anode space 1. It is a preferred size for forming an active material layer having stable physical strength.
  • the current collector 200 is inserted into the positive electrode space 1 of the provided battery structure, filled with particulates, and then a binder solution containing a viscosity modifier and a binder is added thereto. After drying, the positive electrode may be manufactured.
  • the binder solution physically and stably fixes the injected particulate phase to a current collector, and serves to uniformly fill the particulate space in the anode space 1.
  • the viscosity of the binder solution may be 0.01 P to 10,000 P, and the viscosity modifier contained in the binder solution is carboxymethyl cellulose (CMC), methyl cellulose, ethyl cellulose and hydroxypropyl methyl cellulose.
  • CMC carboxymethyl cellulose
  • HPMC hydroxypropyl methylcellulose
  • the binder is polytetrafluoroethylene (PTFE; polytetrafluoroethylene), polyvinyl alcohol (PVA; polyvinyl alcohol), polyolefin (polyolefine), polyethylene oxide (PEO; polyethylen oxide) Or mixtures thereof.
  • the binder solution may contain 0.1 to 20% by weight of the binder.
  • the solvent of the binder solution may be any substance in which the viscosity modifier and the binder are dissolved, but water, alcohol, glycerin, or a mixed solvent thereof may be used in view of easy drying at low temperatures.
  • the binder solution may have a viscosity of 0.01 P to 10,000 P at room temperature and normal pressure, which flows through the empty space between the particulate powder particles filled in the anode space into which the current collector 200 is inserted, and flows between the particles and between the particles and the current collector. It is a viscosity at which the binding solution can be uniformly distributed in the anode space by capillary force while binding uniformly.
  • the viscosity of the binder solution may be adjusted by the content of the above-described viscosity regulator, for example, the binder solution may contain a viscosity modifier so that the viscosity of the solution is 0.01 P to 10,000 P.
  • the binder contained in the binding solution may serve to bind the particles and the particles and the current collector to each other with physical strength.
  • the binder solution may contain 0.1 to 20% by weight of the binder, which does not interfere with the anodic reaction by the binder during charging or discharging, does not interfere with the conduction of sodium ions entering through the solid electrolyte tube, and physically Even when a stable positive electrode is prepared, the electrolyte may be added homogeneously after drying of the binding solution.
  • the battery structure for a more uniform packing of the particulate form within a short time before the step of injecting the particulate into the anode space and / or after the addition of the binder solution is dried The step of applying a physical vibration to the can be further performed.
  • the vibration of the battery structure may include a vibration process including an ultrasonic vibration applied to the side or bottom surface of the metal housing 100.
  • the particulate may be injected to fill at least a portion of the anode space (1), for example, an empty space between the wicking tube 420 and the safety tube (410) Particulates can be filled to a level corresponding to the level (height) of molten sodium filling.
  • the binding solution may also be added to fill at least a portion of the anode space 1, and, for example, the binding solution may be filled at a level where all particulates may be impregnated.
  • the positive electrode in the positive electrode space (1) in which the current collector is injected Injecting and drying an active material slurry containing an active material, conductive particles, a viscosity modifier, and a binder may be performed.
  • the positive electrode active material contained in the particulate may include nickel hydroxide (Ni (OH) 2 ), and the conductive particles, which are conductive particles, may be used in secondary batteries, particularly nickel hydrogen batteries. Any conductive particles commonly used for the positive electrode can be used.
  • the conductive particles may contain carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene, or mixtures thereof.
  • the viscosity modifiers are carboxymethyl cellulose (CMC), methyl cellulose (methylcellulose), ethyl cellulose and hydroxypropyl methylcellulose (HPMC).
  • CMC carboxymethyl cellulose
  • HPMC hydroxypropyl methylcellulose
  • the binder may be polytetrafluoroethylene (PTFE), polyvinyl alcohol (PVA), polyolefine, polyethylene oxide (PEO) or mixtures thereof.
  • the slurry may be a solvent in which the viscosity modifier and the binder are dissolved, but water, alcohol, glycerin, or a mixed solvent thereof may be used in view of easy drying at low temperatures.
  • the active material slurry is 0.1 to 20 parts by weight based on 100 parts by weight of the positive electrode active material in terms of stable binding with the current collector, smooth and homogeneous packing, and easy ion transfer by the electrolyte solution that is added to the positive electrode space after slurry drying. It may contain conductive particles, 0.1 to 10 parts by weight of the viscosity regulator and 0.1 to 20 parts by weight of the binder, the average particle size (diameter) of the positive electrode active material may be 1 ⁇ m to 100 ⁇ m, the average particle size of the conductive particles is 0.1 May be in the range from about 30 ⁇ m.
  • a step of applying physical vibration to the battery structure may be further performed, and the physical vibration may include ultrasonic vibration.
  • the active material slurry may be added to fill at least a portion of the positive electrode space (1), for example, the wicking tube 420 and the safety tube 410
  • the slurry may be filled at a level corresponding to the level (height) of molten sodium filling the void space therebetween.
  • the current collector is inserted into the positive electrode space, and the particulate and the binder solution are sequentially added or the active material slurry is added, followed by drying to remove the solvent of the binder solution or slurry. Step is performed.
  • the active material slurry may be applied to a current collector and then dried to use drying conditions performed in a conventional manufacturing method of manufacturing an electrode for a secondary battery. For example, drying may be performed at a temperature of 50 to 150 ° C. .
  • the step of introducing the electrolyte into the anode space may be further performed.
  • the electrolyte serves to conduct sodium ions quickly and uniformly
  • the electrolyte salt (sodium salt) contained in the electrolyte may include hydroxide, borate, phosphate, or a mixture thereof.
  • the electrolyte salt may be sodium hydroxide (NaOH), trisodium phosphate (Na 3 PO 4 ), sodium pyrophosphate (Na 2 HPO 4 ), sodium metaborate (NaBO 2 ), borax (Na 2 B 4 O 7 ), Boric acid (H 3 BO 3 ) or mixtures thereof.
  • the electrolyte solution includes an aqueous electrolyte solution, and the electrolyte solution may contain 2 to 50 wt% of an electrolyte salt.
  • the step of introducing the metal sodium into the wicking tube after the addition of the electrolyte and sodium, sealing the upper part of the metal housing, Forming an electrode terminal on the outer wall of the metal housing, which may make an electrical closed loop with the external rod, may be further performed.
  • the introduction of sodium, the sealing of the metal housing and the formation of the electrode terminal may be used in the method and structure used in the conventional method for manufacturing a sodium sulfur battery having a structure similar to Figure 1, the description thereof is omitted. do.
  • the present invention provides a sodium secondary battery.
  • the sodium secondary battery according to the present invention includes a sodium ion conductive solid electrolyte, a negative electrode and a positive electrode.
  • the sodium ion conductive solid electrolyte partitions the cathode space and the anode space.
  • the sodium ion conductive solid electrolyte may be disposed in an inner space of a battery case (including a conductive case) that separates the battery internal components from the outside, and may partition the inner space of the battery case into a cathode space and an anode space.
  • the current collector may be located in the positive electrode space, and the positive electrode space in which the current collector is located may be filled with particulates containing a positive electrode active material. That is, the particulate form may fill the entire anode space or a predetermined region where the current collector is located at a predetermined height.
  • the sodium secondary battery according to the present invention comprises a sodium ion conductive solid electrolyte partitioning the cathode space and the anode space; A cathode space in which the cathode is located; And a positive electrode space in which a current collector is charged and filled with particles (packed) including a positive electrode active material.
  • the sodium secondary battery may be manufactured by the above-described manufacturing method.
  • the active material layer containing the positive electrode active material is not laminated in the current collector, but the particulate phase containing the positive electrode active material fills the positive electrode space, and the current collector is charged on the particles filling the positive electrode space.
  • the shape it is free from peeling or desorption of the positive electrode active material layer generated during rolling of the electrode (anode), and it is possible to control the thickness of the positive electrode active material by only adjusting the size of the positive electrode space and / or the winding interval of the current collector.
  • the capacity design of the battery is extremely easy and free, and the mass production process is simplified, which can reduce the investment cost and production cost.
  • the current collector may be in the form of a foam (film), film (film), mesh (mesh), felt (felt) or porous foil (perforated film),
  • the whole may be one or more selected from carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite and graphene.
  • the current collector located in the positive electrode space may be a wound shape or a structure in which a plurality of current collectors are spaced apart from each other.
  • the thickness of the active material coated on the current collector may be controlled by the winding interval of the current collector.
  • the winding interval of the current collector may be 0.01 to 5mm.
  • the arrangement of the current collector may be sufficient as long as the electric field can be uniformly formed in consideration of the physical shape of the anode space.
  • the current collector to be injected into the positive electrode may have a structure in which a plurality of current collectors are connected to each other by a conductive member and spaced apart from each other at equal intervals.
  • the plurality of cylinders, elliptical cylinders or triangular to octagonal polygonal collectors may have concentric structures and spaced apart arrangements.
  • the height of the current collector may be at least a height filled with particulates in the anode space. That is, the current collector may have a structure partially embedded in the particles.
  • the sodium ion conductive solid electrolyte may be a material used for selective conduction of sodium ions to a conventional sodium secondary battery.
  • the sodium ion conductive solid electrolyte may include a sodium super ionic conductor (NaSICON), ⁇ ′′ alumina, or a laminate thereof.
  • the particulate form may contain a positive electrode active material, and the positive electrode active material (positive electrode active material particles) contained in the particulate may include nickel hydroxide.
  • the anode reaction may be Ni (OH) 2 ⁇ NiOOH.
  • the average particle size (diameter) of the positive electrode active material contained in particulate form may be 1 ⁇ m to 100 ⁇ m. If the average particle size of the positive electrode active material is too small, less than 1 ⁇ m, the specific surface area of the positive electrode active material becomes large, but the uniform distribution of the binder is difficult, which may reduce the binding and physical stability of the particles forming the positive electrode in the battery. Excess binder may be required for the binding of P, thereby reducing the substantial surface area (particulate surface area) that can react with sodium ions. If the average particle size of the positive electrode active material is too large to exceed 100 ⁇ m, there is a risk that the battery characteristics are deteriorated by the reduction of the specific surface area of the positive electrode active material.
  • the particulate may further contain conductive particles together with the positive electrode active material.
  • the conductive particles form a low resistance path between the positive electrode active material and the current collector contained on the particles filling the positive electrode space to a certain height, thereby reducing the internal resistance of the battery.
  • the conductive particles may contain carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene or a mixture thereof.
  • the particulate form may further contain 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material.
  • the weight ratio of the conductive particles to the positive electrode active material is a weight ratio in which a low resistance path can be uniformly formed between the positive electrode active material and the current collector without interfering with the positive electrode reaction generated in the positive electrode active material.
  • the average particle size (diameter) of the positive electrode active material may be 1 ⁇ m to 100 ⁇ m, and the average particle size of the conductive particles may be 0.1 ⁇ m to 30 ⁇ m.
  • the size of the conductive particles prevents the amount of the positive electrode active material from being filled by the conductive particles in the same volume of the positive electrode space, and reduces the amount of conductive particles in the interstitial space of the positive electrode active material. Size.
  • the particulate form filling the positive electrode space in which the current collector is located may be bound by a binder, and the binding may be made by drying a solution binder. That is, the solution phase binder located in the inter-particle void space of the anode space may be phase-converted from the liquid phase to the solid phase by volatilization of the liquid phase (including the solvent), and may be bound between the particles and the particles and between the particles and the current collector.
  • the particulate form filling the positive electrode space may be a binder between particles and between the particles and the current collector by drying of a binder injected into the positive electrode space as a solution.
  • the particulate form filling the anode space may be a binder in the anode space by being injected into the anode space in powder form, and then added to the anode space and dried in solution.
  • the particulate form filling the anode space may be bound in the anode space by being poured into the anode space as a slurry together with a binder dissolved in a solvent and then dried.
  • the positive electrode according to the embodiment of the present invention may be manufactured directly in the positive electrode space.
  • the positive electrode according to the exemplary embodiment of the present invention may contain 0.1 to 20 parts by weight of the binder based on 100 parts by weight of the positive electrode active material.
  • the binder content is an amount that can stably bind the particulate phase filling the anode space to a certain height while minimizing the reduction of the reactive surface area of the particulate phase.
  • the binder may include polytetrafluoroethylene (PTFE), polyvinyl alcohol (PVA), polyolefine, polyethylene oxide (PEO) or a mixture thereof.
  • the positive electrode according to an embodiment of the present invention may further contain 0.1 to 10 parts by weight of a viscosity modifier based on 100 parts by weight of the positive electrode active material.
  • a viscosity modifier may be a residue remaining on the positive electrode as the positive electrode is manufactured directly in the positive electrode space.
  • the binder solution or slurry may contain a viscosity control agent for easy introduction and uniform distribution of the above-mentioned binding solution or slurry (positive electrode active material slurry) in the positive electrode space, and when the solvent is volatilized, the viscosity control agent may be positive May remain.
  • the viscosity modifier may be a cellulose based one or more selected from carboxymethyl cellulose (CMC), methyl cellulose, methyl cellulose, ethyl cellulose and hydroxypropyl methylcellulose (HPMC).
  • the positive electrode may further include an electrolyte, and the empty space in which the positive electrode space is filled and left by the particle phase, that is, the space between the particles and the particle, the space between the particles and the battery case And / or the space between the particle and the current collector may be filled by the electrolyte solution. That is, the positive electrode includes a current collector located in the positive electrode space; Particulate form filling the anode space; And an electrolyte solution filling at least the inter-particle void space, wherein the particulate form may be particulate in a state bound by a binder.
  • the electrolyte serves to conduct sodium ions quickly and uniformly
  • the electrolyte salt (sodium salt) contained in the electrolyte may include hydroxide, borate, phosphate, or a mixture thereof.
  • the electrolyte salt may be sodium hydroxide (NaOH), trisodium phosphate (Na 3 PO 4 ), sodium pyrophosphate (Na 2 HPO 4 ), sodium metaborate (NaBO 2 ), borax (Na 2 B 4 O 7 ), Boric acid (H 3 BO 3 ) or mixtures thereof.
  • the electrolyte may include an aqueous or non-aqueous electrolyte, and the electrolyte may contain 2 to 50 wt% of an electrolyte salt.
  • the negative electrode positioned in the negative electrode space includes a negative electrode active material used in a conventional sodium secondary battery.
  • the negative electrode may be a laminate in which a negative electrode active material layer is formed on the negative electrode current collector, or may be metal sodium. More specifically, in the operating state of the cell, the negative electrode may be molten sodium.
  • the capacity of the battery can be designed by the amount of particulates filling the anode space, so that even if the anode volume of the same volume, by the degree of filling by the particulate phase Battery capacity may vary.
  • the amount of particulate matter (the height of the anode space filled by the particulate phase, or the volume of the anode space filled by the particulate phase) filling the anode space can be appropriately adjusted in consideration of the target cell design.
  • the particulates are formed at a height corresponding to the level of molten sodium in the cathode space.
  • FIG. 5 is an example illustrating a cross section of a sodium secondary battery according to an exemplary embodiment of the present invention.
  • FIG. 5 illustrates an example of a structure of a tubular sodium secondary battery in which a negative electrode is located at the center, but the sodium secondary battery according to the present invention may have any battery structure known in a conventional sodium sulfur secondary battery.
  • the sodium secondary battery according to the present invention may have a structure of a tubular sodium secondary battery in which a positive electrode is located at the center, and of course, may have a flat structure.
  • a metal housing 100 corresponding to the battery case is positioned at the outermost portion, a wicking tube 420 is positioned at the center thereof, and the metal housing 100 is located at the center thereof.
  • the solid electrolyte tube 300, the safety tube 410 and the wicking tube 420 may be provided in sequence. That is, from the outside of the metal housing 100 to the inside, the solid electrolyte tube 300, the safety tube 410 and the wicking tube 420 has a concentric structure, between the metal housing 100 and the solid electrolyte tube 300
  • the current collector 200 may be located in the anode space.
  • the current collector 200 may be in a rolled state as shown in FIG. 5, but a plurality of current collectors may be spaced apart from each other and positioned in the positive electrode space.
  • the positive electrode space in which the current collector 200 is located may be filled with particulates P bound to each other by drying a binder injected into the positive electrode space in a liquid phase in the positive electrode space.
  • the height of the anode space filled with particulate matter (P) is at least a level of molten sodium of the cathode, specifically, a level corresponding to the level of molten sodium (H) filling the void space between the wicking tube 420 and the safety tube 410.
  • the particulate phase may be filled up to or more.
  • the empty space remaining in the anode space and filled with particles that is, the space between the particles and the particles, the space between the particles and the metal housing, and / or the space between the particles and the current collector may be filled with the electrolyte, and the electrolyte is located at least in the anode space. It is possible to fill the anode space with a level where all particulates can be impregnated.
  • the sodium battery according to the exemplary embodiment of the present invention is disposed on the metal housing 100 to have a cover and ring shape to seal the inside of the metal housing, and is located above the metal housing 100.
  • An insulator electrically insulating between the metal housing 100 and the solid electrolyte tube 300 may be provided, and an electrode terminal positioned around an upper end of the metal housing 100 may be provided. Of course, it may include more.

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Secondary Cells (AREA)

Description

나트륨 이차전지 및 나트륨 이차전지의 제조방법Sodium secondary battery and manufacturing method of sodium secondary battery

본 발명은 나트륨 이차전지 및 이의 제조방법에 관한 것으로, 가공이 용이하며, 전극의 두께 조절 및 활물질의 함량 조절이 용이한 나트륨 이차전지의 제조방법에 관한 것이다.The present invention relates to a sodium secondary battery and a method for manufacturing the same, and easy to process, to a method for manufacturing a sodium secondary battery that is easy to control the thickness of the electrode and the content of the active material.

일반적으로 전지는 일회용의 일차전지와 여러 차례 충전이 가능한 이차전지로 구분할 수 있다. 이 중, 이차전지는 여러 차례 사용이 가능하다는 점에서, 노트북, 캠코더, 및, 핸드폰과 같은 휴대용 전자기기의 필수적인 에너지원으로 대중화되었다.Generally, a battery may be classified into a disposable primary battery and a rechargeable battery that can be charged many times. Among them, the secondary battery has been popularized as an essential energy source of portable electronic devices such as laptops, camcorders, and mobile phones in that it can be used many times.

최근, 이차전지는 전력 저장을 위한 대용량전지, 운송 수단에 적용되는 중형 전지, 및 휴대용 기기의 전원으로 사용되는 소형 전지에 이르기까지 그 사용 목적에 따라 전지의 형태 및 크기가 변화되어 사용 범위가 확대되고 있는 추세이다.In recent years, secondary batteries have been changed in size and size depending on their purpose, ranging from large-capacity batteries for power storage, medium-size batteries applied to transportation vehicles, and small batteries used as power sources for portable devices. It is becoming a trend.

이러한 이차전지는 음극, 양극, 전해질 및 집전체로 구성된다. 양극에서는 음극에서 발생된 전자에 의한 환원반응이 발생하며, 집전체는 전지의 방전시에 음극으로부터 발생되는 전자를 양극 활물질로 공급하거나 충전시에는 양극으로부터 공급되는 전자를 음극 활물질로 공급하는 역할을 한다.This secondary battery is composed of a negative electrode, a positive electrode, an electrolyte and a current collector. In the positive electrode, a reduction reaction caused by electrons generated at the negative electrode occurs, and the current collector supplies electrons generated from the negative electrode to the positive electrode active material when the battery is discharged, or electrons supplied from the positive electrode to the negative electrode active material at the time of charging. do.

이러한 이차전지 중 나트륨 이차전지는, 대한민국 공개공보 제19960002926호와 같이, 음극으로 용융 금속 나트륨(Na)을 사용하며, 양극으로 황(S)을 사용하고, 음극과 양극이 나트륨 이온에 대하여 선택적인 투과성을 갖는 알루미나 또는 세라믹으로 이루어지는 고체전해질 튜브로 격리되도록 구성되어, 나트륨 이온이 고체전해질 튜브를 통과할 수 있도록 형성된다.Among these secondary batteries, sodium secondary batteries use molten metal sodium (Na) as the cathode, sulfur (S) as the anode, and the cathode and the cathode are selective for sodium ions, as in Korean Patent Publication No. 19960002926. It is configured to be segregated into a solid electrolyte tube made of alumina or ceramic having permeability, so that sodium ions can pass through the solid electrolyte tube.

나트륨 이차전지는 지구상에 풍부한 나트륨을 이용함에 따라 재료 수급성 및 제조원가 측면에서 뛰어난 경쟁력을 갖추고 있으며, 대용량의 전지를 리튬이온전지 대비 단순한 구조로 만들 수 있는 장점을 갖고 있다.Sodium secondary battery has excellent competitiveness in terms of supply and demand for materials and manufacturing cost by using rich sodium on the earth, and has the advantage of making a large capacity battery into a simple structure compared to lithium ion batteries.

이에 따라, 나트륨 이차전지는 기존 이차전지와 유사한 에너지밀도를 가지면서도 값이 싸고, 전력보존 시간도 길게 제작할 수 있어서 태양광이나 풍력 등 신재생 에너지 저장용 이차전지로 활용될 경우, 대용량의 전력을 효율적으로 저장할 수 있는 차세대 저장 매체로 대두되고 있다.Accordingly, the sodium secondary battery has a similar energy density as that of the conventional secondary battery, and is inexpensive, and can be manufactured with a long power conservation time. Therefore, when used as a secondary battery for renewable energy storage such as solar or wind power, a large capacity of electric power can be used. It is emerging as a next-generation storage medium that can be stored efficiently.

그러나, 용융된 유황을 음극으로 사용하는 경우, 약 350℃ 이상의 고온 동작 온도가 필요하며, 이에 따라 유황을 대체할 수 있는 양극에 대한 연구가 지속되고 있다. 본 출원인은 유황 대비 전지 용량의 감소를 방지하며, 200℃ 이하의 상대적으로 낮은 동작 온도에서 운전 가능한 양극으로 수산화니켈이 매우 적합함을 발견하였으며, 이러한 발견을 기반으로, 전해액 내 침지되는 양극의 반응 면적을 최대화 하면서도, 제조 공정이 용이하고, 활물질의 함량 조절이 용이한 양극의 제조방법을 제안하기에 이르렀다.However, when molten sulfur is used as the cathode, a high temperature operating temperature of about 350 ° C. or more is required, and thus research on an anode that can replace sulfur is continued. Applicant has found that nickel hydroxide is very suitable as a positive electrode that can prevent the reduction of battery capacity compared to sulfur and can be operated at relatively low operating temperature below 200 ° C. Based on this finding, reaction of positive electrode immersed in electrolyte While maximizing the area, it has come to propose a method for producing a positive electrode easy to manufacture process, easy to control the content of the active material.

본 발명의 목적은 집전체로부터 양극 활물질층의 박리 또는 탈착이 방지되며, 용량에 따른 전지의 설계가 자유로울 뿐만 아니라, 소형화 가능하며, 제조가 용이한 나트륨 이차전지를 제공하는 것이며, 본 발명의 다른 목적은 양극 활물질의 두께 조절이 용이하며, 대용량 전지를 작은 크기양극 제조 방법이 용이하며, 전극의 두께 조절 및 활물질의 함량 조절이 용이한 나트륨 이차전지의 제조방법을 제공하는 것이다.SUMMARY OF THE INVENTION An object of the present invention is to provide a sodium secondary battery that prevents peeling or desorption of a positive electrode active material layer from a current collector, free of battery design according to capacity, and can be miniaturized and easy to manufacture. An object of the present invention is to provide a method of manufacturing a sodium secondary battery that can easily control the thickness of a cathode active material, a method of manufacturing a small size cathode of a large-capacity battery, and can easily control the thickness of an electrode and the content of an active material.

본 발명에 따른 나트륨 이차전지의 제조방법은 a) 나트륨 이온 전도성 고체전해질에 의해 음극 공간과 구획되는 양극 공간에 집전체를 삽입하는 단계; 및 b) 집전체가 삽입된 양극 공간에 양극활물질을 함유하는 활물질을 투입하는 단계;를 포함한다.A method of manufacturing a sodium secondary battery according to the present invention includes the steps of: a) inserting a current collector into a cathode space partitioned from a cathode space by a sodium ion conductive solid electrolyte; And b) injecting an active material containing a positive electrode active material into the positive electrode space into which the current collector is inserted.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, b) 단계는 b1) 양극 공간에 양극활물질 및 도전입자를 함유하는 입자상을 투입하는 단계; 및 양극 공간에 점도 조절제 및 바인더를 함유하는 결착 용액을 투입하고 건조하는 단계;를 포함할 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, step b) comprises the steps of b1) injecting a particulate phase containing a cathode active material and conductive particles into the cathode space; And injecting a binder solution containing a viscosity modifier and a binder into the anode space and drying the same.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, b) 단계는 b3) 양극 공간에 양극활물질, 도전입자, 점도 조절제 및 바인더를 함유하는 슬러리를 투입하고 건조하는 단계;를 포함할 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, b) step b3) a slurry containing a positive electrode active material, a conductive particle, a viscosity regulator and a binder in the positive electrode space and drying; Can be.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, a) 단계는 양 단 중 일 단이 밀폐되고 다른 일 단이 개방된 원통형의 금속 하우징, 금속 하우징 내부에 위치하며, 금속 하우징의 외측에서 내측으로 순차적으로 동심 구조를 가지며 위치하는 나트륨 이온 전도성 고체전해질 튜브, 안전튜브 및 용융 나트륨이 담지되는 위킹튜브를 제공하는 단계;를 포함할 수 있으며, 양극 공간은 고체전해질 튜브와 금속 하우징 사이의 공간일 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, step a) is a cylindrical metal housing, one end of which is sealed in one end and the other end is open, located inside the metal housing, Providing a sodium ion conductive solid electrolyte tube, a safety tube, and a wicking tube on which molten sodium is loaded, the anode space having a concentric structure sequentially positioned from the outer side to the inner side, wherein the anode space is disposed between the solid electrolyte tube and the metal housing. It may be a space of.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 집전체는 금속 하우징과 동심 구조를 갖도록 권취될 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the current collector may be wound to have a concentric structure with the metal housing.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 집전체는 폼(foam), 필름(film), 메쉬(mesh), 펠트(felt) 또는 다공성 박(perforated film) 형상일 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the current collector may be in the form of a foam (foam), film (film), mesh (mesh), felt (felt) or porous foil (perforated film) shape .

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 집전체는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트 및 그래핀에서 하나 이상 선택된 것일 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the current collector may be one or more selected from carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite and graphene.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 도전입자는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트, 그래핀 또는 이들의 혼합물을 포함할 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the conductive particles may include carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene or a mixture thereof.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 입자상은 양극활물질 100 중량부를 기준으로 0.5 내지 20 중량부의 도전입자를 함유할 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the particulate form may contain 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 양극활물질은 수산화니켈(Ni(OH)2)을 포함할 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the cathode active material may include nickel hydroxide (Ni (OH) 2 ).

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 결착 용액의 점도는 0.01 P 내지 10,000 P일 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the binder solution may have a viscosity of 0.01 P to 10,000 P.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 슬러리의 점도는 0.01 P 내지 10,000 P일 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the viscosity of the slurry may be 0.01 P to 10,000 P.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 점도 조절제는 카르복시메틸 셀룰로오스(CMC; carboxymethyl cellulose), 메틸 셀룰로오스(methylcellulose), 에틸 셀룰로오스(ethyl cellulose) 및 하이드록시프로필 메틸셀룰로오스(HPMC;hydroxypropyl methylcellulose)에서 하나 이상 선택된 셀룰로오스계를 포함하며, 바인더는 폴리테트라플루오르에틸렌(PTFE; polytetrafluoroethylene), 폴리비닐알콜(PVA; polyvinyl alcohol), 폴리올레핀(polyolefine), 폴리에틸렌옥사이드(PEO; polyethylen oxide) 또는 이들의 혼합물을 포함할 수 있다.In the manufacturing method of the sodium secondary battery according to an embodiment of the present invention, the viscosity modifier is carboxymethyl cellulose (CMC; carboxymethyl cellulose), methyl cellulose (methylcellulose), ethyl cellulose (ethyl cellulose) and hydroxypropyl methyl cellulose (HPMC) at least one selected from hydroxypropyl methylcellulose, and the binder may be polytetrafluoroethylene (PTFE; polytetrafluoroethylene), polyvinyl alcohol (PVA), polyolefine, polyethylene oxide (PEO), or polyethylen oxide (PEO). Mixtures thereof.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 결착 용액은 0.1~20 중량%의 바인더를 함유할 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, the binder solution may contain a binder of 0.1 to 20% by weight.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 슬러리는 양극 활물질 100 중량부를 기준으로, 0.1 내지 20 중량부의 도전입자, 0.1 내지 10 중량부의 점도 조절제 및 0.1 내지 20 중량부의 바인더를 함유할 수 있다.In the method for manufacturing a sodium secondary battery according to an embodiment of the present invention, the slurry is based on 100 parts by weight of the positive electrode active material, 0.1 to 20 parts by weight of conductive particles, 0.1 to 10 parts by weight of the viscosity regulator and 0.1 to 20 parts by weight of the binder It may contain.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, b) 단계 후, c) 양극 공간에 전해액을 투입하는 단계;가 더 수행될 수 있다.In the sodium secondary battery according to an embodiment of the present invention, after step b), c) injecting an electrolyte into the anode space; may be further performed.

본 발명에 따른 나트륨 이차전지는 음극 공간과 양극 공간을 구획하는 나트륨 이온 전도성 고체전해질; 음극 공간에 위치하는 나트륨 함유 음극; 및 양극 공간에 위치하는 집전체 및 집전체가 위치한 양극 공간을 채우는 입자상을 포함하며, 입자상은 양극활물질을 함유하는 양극;을 포함한다.Sodium secondary battery according to the present invention comprises a sodium ion conductive solid electrolyte partitioning the negative electrode space and the positive electrode space; A sodium-containing cathode located in the cathode space; And a current collector positioned in the positive electrode space and a particulate form filling the positive electrode space in which the current collector is located, wherein the particulate includes a positive electrode containing a positive electrode active material.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 양극 공간을 채우는 입자상은 용액상으로 양극 공간에 투입된 바인더의 건조에 의해 결착된 것일 수 있다. In the sodium secondary battery according to an embodiment of the present invention, the particulate form filling the positive electrode space may be bound by drying of a binder injected into the positive electrode space in a solution form.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 입자상은 도전 입자를 더 포함할 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the particulate may further include conductive particles.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 입자상은 양극활물질 100 중량부를 기준으로 0.5 내지 20 중량부의 도전입자를 함유할 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the particulate form may contain 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 양극활물질은 수산화니켈(Ni(OH)2)을 포함할 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the cathode active material may include nickel hydroxide (Ni (OH) 2 ).

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 음극은 용융 나트륨일 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the negative electrode may be molten sodium.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 입자상은 음극 공간에서의 용융 나트륨의 수위에 상응하는 높이로 양극 공간을 채울 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the particulate may fill the positive electrode space to a height corresponding to the level of molten sodium in the negative electrode space.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 나트륨 이차전지는 원통형의 금속 하우징, 금속 하우징 내부에 위치하며, 금속 하우징의 외측에서 내측으로 순차적으로 동심 구조를 가지며 위치하는 나트륨 이온 전도성 고체전해질 튜브, 안전튜브 및 용융 나트륨이 담지되는 위킹튜브를 포함하며, 양극 공간은 고체전해질 튜브와 금속 하우징 사이의 공간일 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the sodium secondary battery is located in the cylindrical metal housing, the metal housing, the sodium ion conductive solid electrolyte is located with a concentric structure sequentially from the outside of the metal housing to the inside A tube, a safety tube, and a wicking tube carrying molten sodium are included, and the anode space may be a space between the solid electrolyte tube and the metal housing.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 입자상으로 충진된 양극 공간의 빈 공간은 전해액으로 채워질 수 있다. In the sodium secondary battery according to an embodiment of the present invention, the empty space of the anode space filled with particulates may be filled with an electrolyte solution.

본 발명에 따른 제조방법은 양극 활물질이 구비되지 않은 집전체를 양극 공간에 투입한 후, 입자상 및 결착 용액을 순차적으로 혹은 슬러리로 일체화하여 투입하여, 양극 공간 자체에서 양극을 제조함에 따라, 슬리러 제조, 도포, 건조, 롤링, 권취, 양극 공간에 삽입의 순서에 따른 기존의 공정을 사용하는 것 대비하여, 공정이 간단해지고, 필요 투자비가 감소할 뿐만 아니라, 공정투입 인력도 줄어들게 되어, 원가경쟁력이 높아지며, 기존 공정 적용시의 전극의 롤링 중 발생하는 양극 활물질층의 박리 또는 탈착으로부터 자유로우며, 기계적 가공이 용이하고, 용량에 따른 전지의 설계가 자유로우며, 양극 활물질의 두께 조절이 용이하며, 대용량 전지를 작은 크기로 제조할 수 있는 장점이 있으며, 높은 양산성을 갖는 장점이 있다. In the manufacturing method according to the present invention, after the current collector is not provided with a positive electrode active material into the positive electrode space, the particulate and the binder solution is added sequentially or integrated into a slurry to produce a positive electrode in the positive electrode space itself, as a slurry Compared to the conventional process of manufacturing, coating, drying, rolling, winding, and inserting into the anode space, the process is simplified, the required investment costs are reduced, and the process input manpower is also reduced. It is higher, free from peeling or desorption of the positive electrode active material layer generated during the rolling of the electrode in the existing process, easy mechanical processing, free design of the battery according to the capacity, easy to control the thickness of the positive electrode active material, There is an advantage that a large capacity battery can be manufactured in a small size, there is an advantage having a high mass production.

본 발명에 따른 나트륨 이차전지는 전지의 설계가 자유로울 뿐만 아니라, 집전체와 양극 활물질층의 박리 또는 탈착이 방지되며, 단순히 양극 공간의 크기를 변경함으로써 전지의 용량을 조절할 수 있는 장점이 있다.The sodium secondary battery according to the present invention not only frees the design of the battery, but also prevents peeling or detaching of the current collector and the positive electrode active material layer, and has an advantage of controlling the capacity of the battery by simply changing the size of the positive electrode space.

도 1은 본 발명의 일 실시예에 따른 제조방법에서 전지 구조체의 일 예를 도시한 단면도며,1 is a cross-sectional view showing an example of a battery structure in a manufacturing method according to an embodiment of the present invention,

도 2는 본 발명의 일 실시예에 따른 제조방법의 일 예를 도시한 단면도며,2 is a cross-sectional view showing an example of a manufacturing method according to an embodiment of the present invention,

도 3은 본 발명의 일 실시예에 따른 제조방법의 일 예를 도시한 공정도이며,3 is a process chart showing an example of a manufacturing method according to an embodiment of the present invention,

도 4는 본 발명의 일 실시예에 따른 제조방법의 다른 예를 도시한 공정도이며,4 is a process chart showing another example of a manufacturing method according to an embodiment of the present invention,

도 5는 본 발명의 일 실시예에 따른 이차전지의 단면도를 도시한 도면이다.5 is a cross-sectional view of a secondary battery according to an exemplary embodiment of the present invention.

이하 첨부한 도면들을 참조하여 본 발명의 나트륨 이차전지 및 이의 제조방법를 상세히 설명한다. 다음에 소개되는 도면들은 당업자에게 본 발명의 사상이 충분히 전달될 수 있도록 하기 위해 예로서 제공되는 것이다. 따라서, 본 발명은 이하 제시되는 도면들에 한정되지 않고 다른 형태로 구체화될 수도 있으며, 이하 제시되는 도면들은 본 발명의 사상을 명확히 하기 위해 과장되어 도시될 수 있다. 또한 명세서 전체에 걸쳐서 동일한 참조번호들은 동일한 구성요소들을 나타낸다. Hereinafter, a sodium secondary battery of the present invention and a method of manufacturing the same will be described in detail with reference to the accompanying drawings. The drawings introduced below are provided by way of example so that the spirit of the invention to those skilled in the art can fully convey. Accordingly, the present invention is not limited to the drawings presented below and may be embodied in other forms, and the drawings presented below may be exaggerated to clarify the spirit of the present invention. Also, like reference numerals denote like elements throughout the specification.

이때, 사용되는 기술 용어 및 과학 용어에 있어서 다른 정의가 없다면, 이 발명이 속하는 기술 분야에서 통상의 지식을 가진 자가 통상적으로 이해하고 있는 의미를 가지며, 하기의 설명 및 첨부 도면에서 본 발명의 요지를 불필요하게 흐릴 수 있는 공지 기능 및 구성에 대한 설명은 생략한다.At this time, if there is no other definition in the technical terms and scientific terms used, it has a meaning commonly understood by those of ordinary skill in the art to which the present invention belongs, the gist of the present invention in the following description and the accompanying drawings Descriptions of well-known functions and configurations that may be unnecessarily blurred are omitted.

본 발명에 따른 나트륨 이차전지의 제조방법은 a) 나트륨 이온 전도성 고체전해질에 의해 음극 공간과 구획되는 양극 공간에 집전체를 삽입하는 단계; 및 b) 집전체가 삽입된 양극 공간에 양극활물질을 함유하는 활물질을 투입하는 단계;를 포함한다.A method of manufacturing a sodium secondary battery according to the present invention includes the steps of: a) inserting a current collector into a cathode space partitioned from a cathode space by a sodium ion conductive solid electrolyte; And b) injecting an active material containing a positive electrode active material into the positive electrode space into which the current collector is inserted.

본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, b) 단계는 b1) 양극 공간에 양극활물질 및 도전입자를 함유하는 입자상을 투입하는 단계; 및 양극 공간에 점도 조절제 및 바인더를 함유하는 결착 용액을 투입하고 건조하는 단계;를 포함할 수 있다.In the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, step b) comprises the steps of b1) injecting a particulate phase containing a cathode active material and conductive particles into the cathode space; And injecting a binder solution containing a viscosity modifier and a binder into the anode space and drying the same.

상술한 바와 같이, 본 발명에 따른 나트륨 이차전지의 제조방법은 나트륨 이온 전도성 고체전해질에 의해 구획되는 양극 공간에, 집전체가 양극활물질과 분리된 상태로 투입된 후, 양극 공간 내에서 집전체와 양극활물질을 결착시켜 나트륨 이차전지를 제조한다.As described above, in the method for manufacturing a sodium secondary battery according to the present invention, the current collector is introduced into a positive electrode space partitioned by a sodium ion conductive solid electrolyte, separated from the positive electrode active material, and then the current collector and the positive electrode in the positive electrode space. A sodium secondary battery is manufactured by binding an active material.

즉, 양극 공간에 집전체를 투입한 후, 양극활물질을 포함하는 입자상 및 바인더를 집전체가 투입된 양극 공간에 순차적으로 또는 동시에 투입함으로써, 양극활물질을 포함한 입자간 및 입자와 집전체간 결착이 이루어질 수 있다.That is, after the current collector is introduced into the positive electrode space, the particles and the binder including the positive electrode active material are sequentially or simultaneously introduced into the positive electrode space into which the current collector is inserted, thereby binding between particles including the positive electrode active material and between the particles and the current collector. Can be.

본 발명에 따른 나트륨 이차전지의 제조방법은 집전체에 양극활물질을 함유하는 슬러리를 도포하고 건조하여 양극을 제조한 후, 제조된 양극을 권취, 성형 및/또는 절단하여 전지에 삽입하지 않고, 전지 구조체의 양극 공간 자체 내에서 직접 양극을 제조하는 방법임에 따라, 슬리러 제조, 도포, 건조, 롤링, 권취, 양극 공간에 삽입의 순서에 따른 기존의 공정 대비, 매우 간단한 공정으로 양극을 제조할 수 있으며, 양극 제조를 위한 필요 투자비 및 인력 감소가 가능하여 생산 단가를 낮출 수 있으며, 기존 공정 적용시의 전극의 롤링 중 발생하는 양극 활물질층의 박리 또는 탈착으로부터 자유로우며, 기계적 가공이 용이한 장점이 있다. 또한, 종래에는 전지의 용량을 설계 변경하기 위해서는 양극활물질의 종류를 달리하여 전체적으로 새로운 시스템의 전지를 설계하거나, 동종의 양극활물질을 이용하면서 원하는 수준의 용량을 설계하기 위해 다수개의 양극이 적층된 구조적 변경이 이루어져야 하는 한계가 있었다. 그러나, 본 발명의 제조방법은 단지 양극 공간의 크기를 변경하거나, 양극 공간에 투입되는 입자상의 총량을 제어하는 극히 단순한 방법을 통해 전지의 용량이 변화될 수 있다. 즉, 본 발명에 따른 제조방법은 용량에 따른 전지의 설계가 극히 용이하고 자유로우며, 단지 양극 공간에서의 집전체와 집전체간의 이격 거리 및/또는 전지를 외부로부터 분리하는 케이스(통전성 케이스를 포함함)와 집전체간의 이격 거리를 조절함으로써, 양극 활물질층의 두께가 조절될 수 있음에 따라, 양극 활물질층의 두께 조절이 매우 용이하며, 대용량 전지를 작은 크기로 제조할 수 있는 장점이 있다. In the method for manufacturing a sodium secondary battery according to the present invention, after applying a slurry containing a positive electrode active material to a current collector and drying to prepare a positive electrode, the prepared positive electrode is not wound, molded and / or cut and inserted into a battery, Since the anode is manufactured directly in the anode space of the structure itself, the anode can be manufactured in a very simple process compared to the conventional process according to the order of the slurry production, application, drying, rolling, winding, and insertion into the anode space. It can reduce the investment cost and manpower required for anode production, thereby lowering the production cost, free from peeling or desorption of the cathode active material layer generated during rolling of the electrode in the existing process, and easy for mechanical processing There is this. In addition, conventionally, in order to design and change the capacity of a battery, a battery of a whole new system is designed by different kinds of positive electrode active materials, or a structure in which a plurality of positive electrodes are stacked to design a desired level of capacity while using the same positive electrode active materials. There was a limit to which a change must be made. However, in the manufacturing method of the present invention, the capacity of the battery can be changed only through an extremely simple method of changing the size of the anode space or controlling the total amount of particulates injected into the anode space. That is, the manufacturing method according to the present invention is extremely easy and free to design the battery according to the capacity, only the separation distance between the current collector and the current collector in the positive electrode space and / or the case (including a conductive case) for separating the battery from the outside By controlling the separation distance between the) and the current collector, the thickness of the positive electrode active material layer can be adjusted, it is very easy to control the thickness of the positive electrode active material layer, there is an advantage that a large-capacity battery can be manufactured in a small size.

구체적으로, 본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, b) 단계는 b1) 양극 공간에 양극활물질 및 도전입자를 함유하는 입자상을 투입하는 단계; 및 b2) 양극 공간에 점도 조절제 및 바인더를 함유하는 결착 용액을 투입하고 건조하는 단계;를 포함할 수 있다.Specifically, in the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, step b) comprises the steps of b1) injecting a particulate phase containing a positive electrode active material and conductive particles into the positive electrode space; And b2) injecting and drying a binder solution containing a viscosity modifier and a binder into the anode space.

구체적으로, 본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, b) 단계는 b3) 양극 공간에 양극활물질, 도전입자, 점도 조절제 및 바인더를 함유하는 슬러리를 투입하고 건조하는 단계;를 포함할 수 있다.Specifically, in the method of manufacturing a sodium secondary battery according to an embodiment of the present invention, step b) is a step of b3) adding a slurry containing a positive electrode active material, a conductive particle, a viscosity control agent and a binder in the positive electrode space and drying; It may include.

상세하게, b) 단계는 양극 공간에 집전체의 투입, 양극활물질을 포함하는 입자상의 투입 및 바인더를 함유하는 결착용액의 투입이 순차적으로 이루어지거나, 양극 공간에 집전체의 투입 및 양극활물질 및 바인더를 포함하는 슬러리의 투입이 순차적으로 이루어지는 단계를 포함할 수 있다.Specifically, in step b), the current collector is introduced into the positive electrode space, the particle input including the positive electrode active material and the binder solution containing the binder are sequentially performed, or the current collector is injected into the positive electrode space and the positive electrode active material and the binder are sequentially added. It may comprise the step of the input of the slurry comprising a sequentially.

본 발명에 따른 일 실시예에 있어, 입자상은 양극활물질과 함께 도전 입자를 더 함유할 수 있으며, 이러한 도전 입자는 집전체와 양극활물질간의 저항을 감소시키는 역할, 즉, 전지의 내부 저항을 감소시키는 역할을 수행할 수 있다.In one embodiment according to the present invention, the particulate phase may further contain conductive particles together with the positive electrode active material, which serves to reduce the resistance between the current collector and the positive electrode active material, that is, to reduce the internal resistance of the battery. Can play a role.

구체적으로, 입자상은 양극활물질 100 중량부를 기준으로 0.5 내지 20 중량부의 도전입자를 함유할 수 있다. 양극활물질 대비 도전 입자의 중량비는 양극활물질 에서 발생하는 양극 반응을 방해하지 않으면서도 양극활물질과 집전체간 균일하게 저저항 경로가 형성될 수 있는 중량비이다. Specifically, the particulate form may contain 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material. The weight ratio of the conductive particles to the positive electrode active material is a weight ratio in which a low resistance path can be uniformly formed between the positive electrode active material and the current collector without interfering with the positive electrode reaction generated in the positive electrode active material.

종래와 같이, 집전체에 양극활물질층이 기 적층된 양극을 사용하는 경우, 양극의 안정적 성형성(가공성)을 확보하기 위해서는 양극활물질층의 두께가 제약되는 것이 통상적이다. 이러한 두께의 제약 하에서, 전지 내부 저항 감소를 위해 투입되는 도전체가 증가할수록 양극활물질의 함량이 줄어들게 되어, 적절한 저항 감소 및 적절한 용량을 담보하는 수준으로 도전체와 양극활물질의 양이 조절될 수 밖에 없다. 그러나, 본 발명의 일 실시예에 따른 제조방법은 양극 공간에 양극활물질을 포함하는 입자상을 채워(packing)하여 양극 공간에서 양극(집전체 및 양극활물질)을 제조함으로써, 양극활물질층이 두께 제약으로부터 자유로움에 따라, 입자상은 전지 내부 저항 감소를 주로 고려하여 결정되는 양의 도전입자를 함유할 수 있다. 즉, 종래에 비해, 입자상은 효과적으로 전지의 내부 저항을 감소시킬 수 있는 양의 도전 입자를 자유로이 함유할 수 있다.As in the related art, in the case of using a positive electrode in which a positive electrode active material layer is laminated on a current collector, the thickness of the positive electrode active material layer is usually limited in order to secure stable formability (processability) of the positive electrode. Under such constraints of thickness, the amount of the positive electrode active material decreases as the conductors introduced to decrease the internal resistance of the battery decrease, so that the amount of the conductor and the positive electrode active material can only be adjusted to a level that appropriately decreases the resistance and ensures adequate capacity. . However, the manufacturing method according to an embodiment of the present invention is to prepare a positive electrode (current collector and positive electrode active material) in the positive electrode space by packing a particulate containing a positive electrode active material in the positive electrode space, so that the positive electrode active material layer from the thickness constraint Depending on the freedom, the particulate phase may contain an amount of conductive particles that are determined primarily in consideration of the reduction in battery internal resistance. That is, compared with the prior art, the particulate form can freely contain an amount of conductive particles that can effectively reduce the internal resistance of the battery.

본 발명의 일 실시예에 따른 제조방법에 있어, 양극활물질의 평균 입자 크기(직경)는 1㎛ 내지 100㎛일 수 있으며, 도전입자의 평균 입자 크기는 0.1㎛ 내지 30㎛일 수 있다. 양극활물질의 평균 입자 크기가 1㎛ 미만으로 너무 작을 경우 양극활물질의 비표면적은 커지나 결착용액의 원활한 투입 또는 후술하는 전해액의 원활한 투입 및 안정적인 접촉이 저해될 위험이 있으며, 양극활물질의 결착에 다량의 바인더가 요구되어 전지 특성을 저하시킬 위험이 있다. 양극활물질의 평균 입자 크기가 100㎛를 초과하도록 너무 큰 경우, 양극활물질의 비표면적 감소에 의해 전지 특성이 저하될 위험이 있다. 도전입자는 양극활물질 입자간, 양극활물질과 집전체간 저저항 경로를 형성하여 전지 내부 저항을 감소시키는 역할을 수행하는데, 동일한 부피의 양극 공간에서 도전 입자에 의해 양극활물질이 채워지는 양이 감소되는 것을 방지하며, 효과적으로 저저항 경로를 형성하기 위해, 양극활물질의 평균 입자 크기(직경)가 1㎛ 내지 100㎛일 때, 도전입자의 평균 입자 크기는 0.1㎛ 내지 30㎛일 수 있다. In the manufacturing method according to an embodiment of the present invention, the average particle size (diameter) of the positive electrode active material may be 1 ㎛ to 100 ㎛, the average particle size of the conductive particles may be 0.1 ㎛ to 30 ㎛. If the average particle size of the positive electrode active material is too small, less than 1 μm, the specific surface area of the positive electrode active material becomes large, but there is a risk that the smooth input of the binding solution or the smooth input and stable contact of the electrolyte described below are impaired. There is a risk that a binder is required to degrade battery characteristics. If the average particle size of the positive electrode active material is too large to exceed 100 µm, there is a risk that the battery characteristics are deteriorated by the reduction of the specific surface area of the positive electrode active material. The conductive particles form a low resistance path between the positive electrode active material particles, the positive electrode active material and the current collector to reduce the internal resistance of the battery, and the amount of the positive electrode active material filled by the conductive particles in the same volume of the positive electrode space is reduced. To prevent and effectively form a low resistance path, when the average particle size (diameter) of the positive electrode active material is 1 μm to 100 μm, the average particle size of the conductive particles may be 0.1 μm to 30 μm.

본 발명의 일 실시예에 따른 제조방법은 b) 단계가 수행된 후, 보다 구체적으로, b2) 단계 또는 b3) 단계가 수행된 후, c) 양극 공간에 전해액을 투입하는 단계;가 더 수행될 수 있다.According to an embodiment of the present invention, after step b) is performed, more specifically, after step b2) or b3) is performed, c) injecting an electrolyte into the anode space; Can be.

전해액은 나트륨 이온이 빠르고 균일하게 전도되는 역할을 수행하며, 전해액에 함유되는 전해질염(나트륨염)은 수산화물, 붕산염, 인산염 또는 이들의 혼합물을 포함할 수 있다. 상세하게, 전해질염은 수산화나트륨(NaOH), 인산삼나트륨(Na3PO4), 피로인산나트륨(Na2HPO4), 메타붕산나트륨(NaBO2), 붕사(Na2B4O7), 붕산(H3BO3) 또는 이들의 혼합물을 포함할 수 있다. 이때, 전해액은 수계 또는 비수계 전해액을 포함하며, 전해액은 2 내지 50중량%의 전해질염을 함유할 수 있다.The electrolyte serves to conduct sodium ions quickly and uniformly, and the electrolyte salt (sodium salt) contained in the electrolyte may include hydroxide, borate, phosphate, or a mixture thereof. Specifically, the electrolyte salt may be sodium hydroxide (NaOH), trisodium phosphate (Na 3 PO 4 ), sodium pyrophosphate (Na 2 HPO 4 ), sodium metaborate (NaBO 2 ), borax (Na 2 B 4 O 7 ), Boric acid (H 3 BO 3 ) or mixtures thereof. In this case, the electrolyte may include an aqueous or non-aqueous electrolyte, and the electrolyte may contain 2 to 50 wt% of an electrolyte salt.

본 발명의 일 실시예에 따른 제조방법은, a) 단계 전이나 b) 단계 후, 또는 선택적으로 c) 단계 후, i) 나트륨 이온 전도성 고체전해질에 의해 양극 공간과 음극 공간에 음극을 투입하는 단계를 더 포함할 수 있다.In the manufacturing method according to an embodiment of the present invention, before the step a) or after the step b), or optionally after the step c), i) injecting a negative electrode into the positive electrode space and the negative electrode space by a sodium ion conductive solid electrolyte; It may further include.

구체적으로, 본 발명의 일 실시예에 따른 제조방법은 밀폐형 전지 케이스에 적어도, 나트륨 이온 전도성 고체전해질을 투입하여, 나트륨 이온 전도성 고체전해질에 의해 전지 케이스 내부 공간을 양극 공간과 음극 공간으로 구획하는 단계; 음극 공간에 음극을 투입하는 단계; 상술한 a) 및 b) 단계, 선택적으로 a), b) 및 c) 단계를 통해 양극 공간에서 양극을 제조하는 단계; 및 전지 케이스를 밀폐하는 단계;를 포함할 수 있다.Specifically, in the manufacturing method according to an embodiment of the present invention, at least a sodium ion conductive solid electrolyte is injected into the sealed battery case, and the space inside the battery case is divided into a positive electrode space and a negative electrode space by a sodium ion conductive solid electrolyte. ; Injecting a cathode into the cathode space; Manufacturing a positive electrode in the positive electrode space through steps a) and b), optionally steps a), b) and c); And sealing the battery case.

구체적으로, 본 발명의 일 실시예에 따른 제조방법은 밀폐형 전지 케이스에 적어도, 나트륨 이온 전도성 고체전해질을 투입하여, 나트륨 이온 전도성 고체전해질에 의해 전지 케이스 내부 공간을 양극 공간과 음극 공간으로 구획하는 단계; 상술한 a) 및 b) 단계, 선택적으로 a), b) 및 c) 단계를 통해 양극 공간에서 양극을 제조하는 단계; 음극 공간에 음극을 투입하는 단계; 및 전지 케이스를 밀폐하는 단계;를 포함할 수 있다. Specifically, in the manufacturing method according to an embodiment of the present invention, at least a sodium ion conductive solid electrolyte is injected into the sealed battery case, and the space inside the battery case is divided into a positive electrode space and a negative electrode space by a sodium ion conductive solid electrolyte. ; Manufacturing a positive electrode in the positive electrode space through steps a) and b), optionally steps a), b) and c); Injecting a cathode into the cathode space; And sealing the battery case.

본 발명의 일 실시예에 따른 제조방법에 있어, 음극 공간에 투입되는 음극은 음극 집전체상 음극활물질층이 형성된 전극이거나, 전지 동작 온도에서 액상을 형성하는 음극활물질에 봉형상의 전도성 흑연과 같은 음극 집전체가 장입된 것일 수 있다. In the manufacturing method according to an embodiment of the present invention, the negative electrode introduced into the negative electrode space is an electrode on which the negative electrode active material layer is formed on the negative electrode current collector, or a negative electrode such as rod-shaped conductive graphite on the negative electrode active material forming a liquid phase at a battery operating temperature The current collector may be charged.

본 발명의 일 실시예에 따른 제조방법에 있어, 음극(음극활물질)은 금속 소듐일 수 있다.In the manufacturing method according to an embodiment of the present invention, the cathode (cathode active material) may be metal sodium.

본 발명의 일 실시예에 따른 제조방법에 있어, 양극활물질(입자)는 수산화니켈일 수 있다. In the manufacturing method according to an embodiment of the present invention, the positive electrode active material (particle) may be nickel hydroxide.

본 발명의 일 실시예에 따른 제조방법에 있어, 양극 공간에 입자상이 투입된 후, 양극 공간에 결착 용액이 투입된 후, 또는 양극 공간에 슬러리가 투입된 후, 양극 공간 내에 위치하는 양극 구성 물질들(입자상을 포함함)의 균질하고 안정적인 충진(packing)과 고른(homogeneous) 분포를 위해, 양극 공간에 물리적 진동을 가하는 단계가 더 수행될 수 있다. 물리적 진동은 분말인 입자상의 균일하고 균질한 충진을 야기하는 진동이라면 어떤 진동이든 사용 가능하며, 구체적인 일 예로, 전지 케이스와 외부 물체간의 물리적 부딪침에 의한 충격(impact)에서 초음파 진동에 이르는 다양한 물리적 진동이 사용될 수 있다. In the manufacturing method according to an embodiment of the present invention, after the particulate phase is added to the anode space, the binder solution is added to the anode space, or after the slurry is injected into the anode space, the anode constituent materials (particulate matter) For further homogeneous and stable packing and homogeneous distribution, the step of applying a physical vibration to the anode space may be further performed. The physical vibration can be any vibration as long as it causes a uniform and homogeneous filling of powder particles. For example, various physical vibrations, such as an impact from an ultrasonic impact between a battery case and an external object, to an ultrasonic vibration. This can be used.

본 발명의 일 실시예에 따른 제조방법에 있어, b1) 양극 공간에 양극활물질 및 도전입자를 함유하는 입자상을 투입하는 단계; 및 b2) 양극 공간에 점도 조절제 및 바인더를 함유하는 결착 용액을 투입하고 건조하는 단계;를 포함하여, 양극이 제조되는 경우, 결착 용액은 입자상으로 투입된 입자들을 결착시킴과 동시에, 입자들과 집전체를 결착시키는 역할을 수행할 수 있다. In the manufacturing method according to an embodiment of the present invention, b1) a step of injecting a particulate phase containing a positive electrode active material and conductive particles into the anode space; And b2) injecting and drying a binder solution containing a viscosity modifier and a binder into the positive electrode space, and when the positive electrode is prepared, the binder solution binds the particles introduced into the particles and at the same time, the particles and the current collector. It can serve to bind.

결착 용액에 함유된 점도 조절제는 카르복시메틸 셀룰로오스(CMC; carboxymethyl cellulose), 메틸 셀룰로오스(methylcellulose), 에틸 셀룰로오스(ethyl cellulose) 및 하이드록시프로필 메틸셀룰로오스(HPMC;hydroxypropyl methylcellulose)에서 하나 이상 선택된 셀룰로오스계일 수 있다.The viscosity modifier contained in the binding solution may be a cellulose based at least one selected from carboxymethyl cellulose (CMC), methyl cellulose (methylcellulose), ethyl cellulose and hydroxypropyl methylcellulose (HPMC). .

결착 용액은 상온 상압 하 0.01 P 내지 10,000 P의 점도를 가질 수 있는데, 이는 집전체가 삽입된 양극 공간에 채워진 입자상의 입자간 빈 공간을 타고 흘러 입자상간 및 입자상과 집전체간을 균일하게 결착시키면서도 모세관력에 의해 양극 공간 내 균질하게 결착 용액이 분포할 수 있는 점도이다. 결착 용액은 상술한 점도를 만족하도록 점도 조절제를 함유할 수 있다.The binding solution may have a viscosity of 0.01 P to 10,000 P at room temperature and normal pressure, which flows through the empty space between particles filled in the anode space into which the current collector is inserted, while uniformly binding between the particles and between the particles and the current collector. It is the viscosity at which the binding solution can be homogeneously distributed in the anode space by capillary force. The binder solution may contain a viscosity modifier to satisfy the above-mentioned viscosity.

결착 용액에 함유되는 바인더는 폴리테트라플루오르에틸렌(PTFE; polytetrafluoroethylene), 폴리비닐알콜(PVA; polyvinyl alcohol), 폴리올레핀(polyolefine), 폴리에틸렌옥사이드(PEO; polyethylen oxide) 또는 이들의 혼합물을 포함할 수 있다. 결착 용액에 함유된 바인더는 입자상들 및 입자상과 집전체를 물리적 강도를 가지며 서로 결합시키는 역할을 수행한다. 결착 용액은 0.1 내지 20 중량%의 바인더를 함유할 수 있는데, 이러한 바인더의 함량은 양극 반응을 방해하지 않고, 나트륨 이온의 전도를 방해하지 않으며, 물리적으로 안정적인 양극이 제조되면서도, 결착 용액의 건조 후 균질하게 전해액이 투입될 수 있다.The binder contained in the binding solution may include polytetrafluoroethylene (PTFE), polyvinyl alcohol (PVA), polyolefine, polyethylene oxide (PEO) or a mixture thereof. The binder contained in the binding solution serves to bind the particles and the particles and the current collector to each other with physical strength. The binder solution may contain 0.1 to 20% by weight of the binder, the content of this binder does not interfere with the positive electrode reaction, does not interfere with the conduction of sodium ions, and after drying of the binder solution, even when a physically stable positive electrode is produced The electrolyte may be added homogeneously.

결착 용액의 용매는 상술한 점도 조절제 및 바인더가 용해되는 물질이면 무방하다.The solvent of the binding solution may be a substance in which the viscosity modifier and binder described above are dissolved.

본 발명의 일 실시예에 따른 제조방법에 있어, b3) 양극 공간에 양극활물질, 도전입자, 점도 조절제 및 바인더를 함유하는 슬러리를 투입하고 건조하는 단계;를 포함하여, 양극이 제조되는 경우, 입자상 및 결착 용액을 순차적으로 투입하는 경우와 유사하게, 점도 조절제는 카르복시메틸 셀룰로오스(CMC; carboxymethyl cellulose), 메틸 셀룰로오스(methylcellulose), 에틸 셀룰로오스(ethyl cellulose) 및 하이드록시프로필 메틸셀룰로오스(HPMC;hydroxypropyl methylcellulose)에서 하나 이상 선택된 셀룰로오스계일 수 있으며, 바인더는 폴리테트라플루오르에틸렌(PTFE; polytetrafluoroethylene), 폴리비닐알콜(PVA; polyvinyl alcohol), 폴리올레핀(polyolefine), 폴리에틸렌옥사이드(PEO; polyethylen oxide) 또는 이들의 혼합물을 포함할 수 있으며, 슬러리의 용매는 점도 조절제 및 바인더가 용해되는 물질이면 무방하다.In the manufacturing method according to an embodiment of the present invention, b3) a slurry containing a positive electrode active material, a conductive particle, a viscosity control agent and a binder in the positive electrode space and drying; including, when the positive electrode is produced, particulate And similar to the case where the binder solution is added sequentially, the viscosity modifier is carboxymethyl cellulose (CMC; carboxymethyl cellulose), methyl cellulose (methylcellulose), ethyl cellulose (ethyl cellulose) and hydroxypropyl methylcellulose (HPMC) At least one selected from cellulose-based, the binder may include polytetrafluoroethylene (PTFE; polytetrafluoroethylene), polyvinyl alcohol (PVA; polyvinyl alcohol), polyolefin (polyolefine), polyethylene oxide (PEO; polyethylen oxide) or a mixture thereof The solvent of the slurry may be a substance in which a viscosity modifier and a binder are dissolved. It is okay if.

슬러리(활물질 슬러리)는 집전체와의 안정한 결착, 원활하고 균질한 패킹(packing) 및 슬러리 건조 후 양극 공간에 투입되는 전해액에 의한 용이한 이온 전달 측면에서, 양극 활물질 100 중량부를 기준으로, 0.1 내지 20 중량부의 도전입자, 0.1 내지 10 중량부의 점도 조절제 및 0.1 내지 20 중량부의 바인더를 함유할 수 있으며, 점도 조절제는 슬러리가 상온 상압 하 0.01 P 내지 10,000 P의 점도를 가질 수 있도록 함유될 수 있다.The slurry (active material slurry) is 0.1 to 0.1 parts based on 100 parts by weight of the positive electrode active material in terms of stable binding with the current collector, smooth and homogeneous packing, and easy ion transfer by the electrolyte solution injected into the positive electrode space after slurry drying. It may contain 20 parts by weight of conductive particles, 0.1 to 10 parts by weight of the viscosity regulator and 0.1 to 20 parts by weight of the binder, the viscosity regulator may be contained so that the slurry can have a viscosity of 0.01 P to 10,000 P at room temperature normal pressure.

이하, 음극이 중심에 위치하는 튜브형 구조를 갖는 나트륨 이차전지를 구체적인 일 예로 하여, 본 발명의 제조방법을 상세히 설명하나, 이는 본 발명의 이해를 돕기 위해 제시된 것이며, 본 발명이 나트륨 이차전지의 구조에 의해 한정될 수 없음은 물론이다. 상술한 바와 같이, 본 발명의 나트륨 이차전지 및 이의 제조방법은 밀폐형 케이스 및 밀폐형 케이스의 내부 공간이 나트륨 이온 전도성 고체전해질에 의해 양극 공간과 음극 공간으로 구획되는 나트륨 이차전지의 모든 구조를 포함할 수 있다. 튜브형 구조는 통상의 용융나트륨유황 전지에서 사용되는 전지 구조를 포함할 수 있으며, 양극이 중심에 위치하는 튜브형 구조를 포함할 수 있다. 또한, 제조하고자 하는 나트륨 이차전지는 평판형 구조를 포함할 수 있는데, 이러한 평판형 구조는 내부 공간을 갖는 밀폐형 케이스에 평판형태의 나트륨 이온 전도성 고체전해질이 위치함으로써, 내부 공간이 양극 공간과 음극 공간으로 분리 구획되는 구조를 포함한다. Hereinafter, a specific example of a sodium secondary battery having a tubular structure in which a negative electrode is positioned in the center will be described in detail. However, the manufacturing method of the present invention will be described in detail, which is presented to help understanding of the present invention, and the present invention provides a structure of a sodium secondary battery. Of course, it can not be limited by. As described above, the sodium secondary battery of the present invention and a method of manufacturing the same may include all structures of the sodium secondary battery in which the sealed case and the inner space of the sealed case are partitioned into a positive electrode space and a negative electrode space by a sodium ion conductive solid electrolyte. have. The tubular structure may include a cell structure used in a conventional molten sodium sulfur battery, and may include a tubular structure in which the positive electrode is located at the center. In addition, the sodium secondary battery to be manufactured may include a plate-like structure, which is a plate-shaped sodium ion conductive solid electrolyte is placed in a sealed case having an inner space, the inner space is the positive electrode space and the negative electrode space It includes a structure that is divided into compartments.

도 1은 본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법을 도시한 일 예로, 전지 구조체 제공단계의 일 예를 상세 도시한 단면도이다. 즉, 도 1은 본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법에 있어, 나트륨 이온 전도성 고체전해질에 의해 양극 공간과 음극 공간으로 구획된 전지 구조체의 일 예를 도시한 도면이다1 is an example illustrating a method of manufacturing a sodium secondary battery according to an exemplary embodiment of the present invention. That is, FIG. 1 is a view illustrating an example of a battery structure partitioned into a positive electrode space and a negative electrode space by a sodium ion conductive solid electrolyte in a method of manufacturing a sodium secondary battery according to an embodiment of the present invention.

도 1에 도시한 바와 같이, 전지 구조체는 최 외각에 금속 하우징(100)이 위치하며, 그 중심에 위킹 튜브(420)가 위치하고, 금속 하우징(100)의 내부에 금속 하우징(100)의 외각에서 중심 방향으로, 고체전해질 튜브(300), 안전 튜브(410) 및 위킹 튜브(420)가 순차적으로 구비될 수 있다.As shown in FIG. 1, in the battery structure, the metal housing 100 is positioned at the outermost side, the wicking tube 420 is positioned at the center thereof, and the metal housing 100 is disposed at the outer side of the metal housing 100 inside the metal housing 100. In the center direction, the solid electrolyte tube 300, the safety tube 410, and the wicking tube 420 may be sequentially provided.

즉, 금속 하우징(100)의 외측에서 내측으로, 고체전해질 튜브(300)안전 튜브(410) 및 위킹 튜브(420)가 동심구조를 가지며, 금속 하우징(100) 내부에 구비된 전지 구조체를 제공할 수 있다.That is, from the outside of the metal housing 100 to the inside, the solid electrolyte tube 300, the safety tube 410 and the wicking tube 420 has a concentric structure, to provide a battery structure provided inside the metal housing 100 Can be.

금속 하우징(100)은 양 단 중 일 단이 밀폐되고 다른 일단이 개방된 원통형을 포함할 수 있으며, 전지의 제조가 완료된 후 금속 하우징(100)의 개방된 일 단을 밀폐시키는 덮개(미도시)를 포함할 수 있다. 금속 하우징(100)과 인접하여 나트륨 이온을 선택적으로 투과시키는 고체전해질 튜브(300)가 위치할 수 있다. The metal housing 100 may include a cylindrical shape in which one end of both ends is sealed and the other end is open, and a cover (not shown) for sealing the open end of the metal housing 100 after the manufacture of the battery is completed. It may include. A solid electrolyte tube 300 that selectively transmits sodium ions may be positioned adjacent to the metal housing 100.

고체전해질 튜브(300)의 고체전해질은 나트륨 이온의 선택적 전도를 위해 전지 분야에서 통상적으로 사용되는 고체전해질을 포함하며, 일 예로, 나트륨초이온전도체(Na super ionic conductor, NaSICON), β"알루미나 또는 이들의 적층체를 포함할 수 있다. 금속 하우징(100)의 최 내측, 즉 중심에 위치하는 위킹튜브(420)는 하단에 관통홀이 형성된 튜브 형상일 수 있으며, 안전튜브(410)는 위킹튜브(420) 외측에 위치하여 일정 이격 거리를 가지며 위킹튜브(420)를 감싸는 구조를 가질 수 있다.The solid electrolyte of the solid electrolyte tube 300 includes a solid electrolyte conventionally used in the battery field for the selective conduction of sodium ions. For example, a sodium super ion conductor (NaSICON), β "alumina or The wicking tube 420 positioned at the innermost, ie central portion of the metal housing 100 may have a tube shape having a through hole formed at a lower end thereof, and the safety tube 410 is a wicking tube. Located outside the 420 may have a predetermined distance and have a structure surrounding the wicking tube (420).

용융 나트륨을 포함하는 음극 활물질은 위킹튜브(420) 내부에 구비될 수 있으며, 위킹튜브(420) 하부에 형성된 관통홀을 통해 위킹튜브(420)와 안전튜브(410) 사이의 빈 공간을 채우는 구조를 가질 수 있다. The negative electrode active material including molten sodium may be provided inside the wicking tube 420, and fills an empty space between the wicking tube 420 and the safety tube 410 through a through hole formed under the wicking tube 420. It can have

위킹튜브(420) 및 안전튜브(410)의 이중 구조는 고체전해질 튜브(300)의 파손시 양극 활물질과 음극 활물질간의 격렬한 반응을 방지하며, 모세관력에 의해 방전시에도 용융 나트륨의 수위를 일정하게 유지할 수 있는 구조이다.The dual structure of the wicking tube 420 and the safety tube 410 prevents a violent reaction between the positive electrode active material and the negative electrode active material when the solid electrolyte tube 300 breaks, and maintains a constant level of molten sodium even during discharge due to capillary force. It is a sustainable structure.

비록, 도 1에 원통형의 금속 하우징, 튜브 형상의 고체전해질, 튜브 형상의 안전튜브 및 위킹튜브를 포함하는 전지구조체의 일 예를 도시하였으나, 본 발명은 양극 공간에서 직접적으로 양극을 제조하는 기술을 제공함에 따라, 본 발명이 전지 구조체의 형상, 재질 또는 크기에 의해 한정될 수 없음은 물론이다. Although FIG. 1 illustrates an example of a battery structure including a cylindrical metal housing, a tubular solid electrolyte, a tubular safety tube, and a wicking tube, the present invention provides a technique for directly manufacturing a cathode in an anode space. As provided, of course, the present invention is not limited by the shape, material or size of the battery structure.

도 2는 본 발명의 일 실시예에 따른 나트륨 이차전지의 제조방법의 단면도를 도시한 일 예로, 도 1과 같은 전지 구조체가 제공된 후, 금속 하우징(100)과 고체전해질 튜브(300) 사이의 공간인 양극 공간(1)에 양극을 형성하는 단계의 일 예를 상세 도시한 것이다.2 is a cross-sectional view of a method for manufacturing a sodium secondary battery according to an embodiment of the present invention. After the battery structure shown in FIG. 1 is provided, a space between the metal housing 100 and the solid electrolyte tube 300 is provided. An example of the step of forming an anode in the phosphorous anode space 1 is shown in detail.

도 2의 일 예와 같이, 제공된 전지 구조체의 양극 공간(1)에 양극활물질을 함유하는 슬러리가 집전체에 도포 및 건조된 양극을 권취하여 삽입하지 않고, 양극활물질이 부착(또는 고정)되지 않은 집전체 자체(활물질 미 형성 집전체)를 위치시킬 수 있다.As in the example of FIG. 2, the slurry containing the positive electrode active material is not wound and inserted into the current collector in the positive electrode space 1 of the provided battery structure, and the positive electrode active material is not attached (or fixed). The current collector itself (active material unformed current collector) can be placed.

집전체는 폼(foam), 필름(film), 메쉬(mesh), 펠트(felt) 또는 다공성 박(perforated film)의 형태일 수 있으며, 집전체는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트 및 그래핀에서 하나 이상 선택될 수 있다.The current collector may be in the form of a foam, film, mesh, felt or porous foil, and the current collector may be carbon, nickel, titanium, yttrium, calcium, chromium, One or more may be selected from cobalt, zinc, graphite and graphene.

집전체는 전극의 반응면적을 넓히면서 효과적으로 전하를 모으기 위해 말려진(rolling) 상태로 양극 공간(1)에 투입될 수 있으며, 권취된 집전체는 금속 하우징(100)과 동심 구조를 갖도록 귄취되어 투입될 수 있으나, 본 발명이 투입되는 집전체의 형상에 의해 한정될 수 없음은 물론이다. The current collector may be introduced into the anode space 1 in a rolled state in order to effectively collect electric charges while widening the reaction area of the electrode, and the current collector may be wound and input to have a concentric structure with the metal housing 100. Although it may be, of course, the present invention may not be limited by the shape of the current collector.

활물질이 구비되지 않은 집전체를 권취한 후 양극 공간에 투입하는 본 발명의 일 실시예에 따른 제조방법은 권취시 발생하는 활물질과 집전체 간의 탈착을 방지할 수 있으며, 집전체 상 다량의 양극 활물질이 구비되어야 하는 대용량 나트륨 전지의 제조에 적합한 장점이 있다. The manufacturing method according to an embodiment of the present invention, which winds up a current collector that is not provided with an active material and then inserts it into the positive electrode space, may prevent desorption between the active material and the current collector generated during winding, and a large amount of positive electrode active material on the current collector This has the advantage of being suitable for the manufacture of large capacity sodium batteries to be provided.

구체적으로, 용량이 500Ah 이상인 대용량 나트륨 전지의 제조를 위해서 한 층의 집전체를 사용할 경우라면, 양극 활물질을 250mm이상의 두께로 코팅해야 할 필요가 있는데, 이러한 경우 전극 자체의 두께가 두꺼워지면서 말려진 형상으로 전극을 가공하는데 어려움이 발생한다. 즉, 두꺼운 양극 활물질층이 구비된 집전체를 말려진 형상으로 가공하는 경우, 양극 활물질층의 박리 또는 탈착이 발생하며, 기계적 강도가 떨어지고, 가공시 많은 에너지가 소모되며, 전극이 말려진 형상을 유지하지 못하여 안정성이 떨어지는 문제점이 발생한다. Specifically, in the case of using a single layer current collector for manufacturing a large capacity sodium battery having a capacity of 500 Ah or more, it is necessary to coat the cathode active material to a thickness of 250 mm or more. In this case, the shape of the electrode itself becomes thick and dried. Difficulties arise in machining the electrodes. That is, when the current collector with a thick positive electrode active material layer is processed into a dried shape, peeling or desorption of the positive electrode active material layer occurs, the mechanical strength is lowered, a lot of energy is consumed during processing, and the electrode is dried. There is a problem that the stability is not maintained.

이를 해소하는 방법으로, 집전체에 얇은 양극 활물질층을 형성한 후, 권취된 횟수를 증가시켜 동일양의 양극 활물질을 전지에 투입하는 방법이 있으나, 이러한 경우, 집전체의 사용량이 증가하고, 일단 활물질이 도포된 전극을 제조한 후 여러 겹으로 양극 공간내에 위치시켜야 하는 공정이 필요하게 되어, 제조단가가 상승할 뿐만 아니라, 여러겹으로 말려진 양극의 부피 증가에 의해 전지의 크기가 커지는 문제점이 있다.As a method of eliminating this, there is a method in which a thin positive electrode active material layer is formed on a current collector, and then the number of times of winding is increased to inject the same amount of the positive electrode active material into a battery. After manufacturing the electrode coated with the active material, a process that needs to be placed in the anode space in several layers is required, and not only the manufacturing cost increases but also the size of the battery increases due to the increase in the volume of the dried cathode. have.

본 발명의 일 실시예에 따른 제조방법에 있어, 양극 활물질이 구비되지 않은 집전체를 말려진 형상으로 가공한 후, 권취된 집전체를 양극 공간에 투입함에 따라, 전극의 롤링 중 발생하는 양극 활물질층의 박리 또는 탈착으로부터 자유로우며, 집전체의 기계적 연성, 기계적 강도, 전기적 특성만을 고려하여 집전체의 물질, 두께 및 형상을 결정할 수 있음에 따라, 보다 용이하게 전지 제작이 가능하며, 단지 양극 공간의 크기 및/또는 집전체의 권취 간격을 조절함으로써 양극 활물질의 두께 조절이 가능하며, 양산 공정이 단순해져 투자비 및 생산원가 측면에서 절감이 가능한 정점이 있다.In the manufacturing method according to an embodiment of the present invention, after processing a current collector that is not provided with a positive electrode active material in a dried shape, the positive electrode active material generated during rolling of the electrode as the wound current collector is put into the positive electrode space Free from peeling or desorption of the layer, the material, thickness and shape of the current collector can be determined in consideration of the mechanical ductility, mechanical strength, and electrical properties of the current collector, thereby making it easier to manufacture the battery, and only the anode space. The thickness of the positive electrode active material can be controlled by adjusting the size and / or the winding interval of the current collector, and the mass production process is simplified, thereby reducing the investment cost and the production cost.

이때, 집전체의 귄취시, 집전체의 권취 횟수 및 권취 간격(도 2의 D)은 전지의 용량을 고려하여 설계될 수 있음은 물론이며, 양극 공간(1)의 크기 또한 전지의 용량을 고려하여 설계될 수 있음은 물론이다.At this time, when winding the current collector, the number of windings and the winding interval (D of FIG. 2) of the current collector may be designed in consideration of the capacity of the battery, and the size of the positive electrode space 1 also takes into account the capacity of the battery. Of course, it can be designed.

도 3은 상술한 전지 구조체가 제공되고, 금속 집전체가 양극 공간(1)에 투입된 후, 양극 활물질을 함유하는 입자상을 투입하는 단계를 상세 도시한 공정도의 일 예이다. FIG. 3 is an example of a process diagram in which the above-described battery structure is provided, and a metal current collector is introduced into the positive electrode space 1, and then the step of introducing a particulate phase containing the positive electrode active material is shown in detail.

본 발명의 일 실시예에 따른 제조방법에 있어, 도 3에 도시한 일 예와 같이, 양극 공간(1)에 집전체(200)를 삽입한 후, 집전체(200)가 투입된 양극 공간(1)에 양극활물질 및 도전입자를 함유하는 입자상을 투입하고, 이후, 입자상이 투입된 양극 공간(1)에 점도 조절제 및 바인더를 함유하는 결착 용액을 투입하고 건조하는 단계가 수행될 수 있다.In the manufacturing method according to an embodiment of the present invention, as shown in the example shown in FIG. 3, after the current collector 200 is inserted into the positive electrode space 1, the positive electrode space 1 into which the current collector 200 is introduced ) Into the particulate phase containing the positive electrode active material and the conductive particles, and then a step of adding a binder solution containing a viscosity modifier and a binder into the positive electrode space (1) in which the particulate phase is added and dried.

입자상에 함유되는 양극 활물질은 수산화니켈(Ni(OH)2)을 포함할 수 있으며, 전도성 입자인 도전 입자는 이차 전지, 특히 니켈수소 전지의 양극에 통상적으로 사용되는 도전 입자이면 사용 가능하다. 일 예로, 도전입자는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트, 그래핀 또는 이들의 혼합물을 함유할 수 있다.The positive electrode active material contained on the particles may include nickel hydroxide (Ni (OH) 2 ), and the conductive particles, which are conductive particles, may be used as long as the conductive particles are commonly used for the positive electrode of a secondary battery, particularly a nickel hydrogen battery. For example, the conductive particles may contain carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene, or mixtures thereof.

상술한 바와 같이, 본 발명의 일 실시예에 따른 제조방법에 있어, 입자상은 양극활물질 입자와 도전입자의 혼합 분말을 함유하며, 도전입자는 양극반응(Ni(OH)2↔NiOOH)이 발생하는 양극활물질(수산화니켈)과 집전체간 저항을 감소시키는 역할을 수행한다. As described above, in the manufacturing method according to an embodiment of the present invention, the particulate phase contains a mixed powder of the positive electrode active material particles and the conductive particles, the conductive particles are anodic reaction (Ni (OH) 2 ↔ NiOOH) is generated It reduces the resistance between the positive electrode active material (nickel hydroxide) and the current collector.

본 발명의 일 실시예에 따른 제조방법에 있어, 권취된 집전체(200)가 삽입된 양극 공간(1)에 입자상을 투입하여, 권취된 집전체 사이, 집전체(200)와 금속 하우징(100) 사이 및 고체 전해질(300)과 금속 하우징(100) 사이의 공간이 입자상으로 채워질 수 있다. In the manufacturing method according to an embodiment of the present invention, the particulate matter is injected into the positive electrode space 1 into which the wound current collector 200 is inserted, and between the wound current collector, the current collector 200 and the metal housing 100. The space between the) and between the solid electrolyte 300 and the metal housing 100 may be filled with particulates.

이때, 상술한 바와 같이, 단지 집전체의 권취 간격(도 2의 D)을 제어함으로써, 집전체에 코팅되는 활물질의 두께가 제어될 수 있다. 집전체의 권취 간격은 전지의 용량을 고려하여 가변적으로 변화될 수 있으며, 일 예로, 집전체의 권취 간격은 0.01내지 5mm이다.At this time, as described above, only by controlling the winding interval (D of FIG. 2) of the current collector, the thickness of the active material coated on the current collector can be controlled. The winding interval of the current collector may be changed in consideration of the capacity of the battery. For example, the winding interval of the current collector is 0.01 to 5 mm.

본 발명의 일 실시예에 따른 제조방법에 있어, 입자상이 건조한 분말 상태로 양극 공간(1)에 투입됨에 따라, 분말에 함유된 양극활물질 입자 및 도전 입자 사이에 빈 공간에 형성되는데, 이러한 입자간의 빈 공간이 결착 용액으로 채워질 수 있다. In the manufacturing method according to an embodiment of the present invention, as the particulate is introduced into the anode space 1 in a dry powder state, it is formed in the empty space between the cathode active material particles and the conductive particles contained in the powder, between the particles Empty spaces may be filled with the binding solution.

이에 따라, 입자상의 평균 입자 크기에 의해 결착 용액이 채워지는 부피가 제어될 수 있다. 입자상에 함유되는 양극활물질의 평균 입자 크기(직경)는 1㎛ 내지 100㎛일 수 있으며, 도전입자의 평균 입자 크기는 0.1㎛ 내지 30㎛일 수 있다.Thus, the volume at which the binding solution is filled can be controlled by the average particle size of the particulates. The average particle size (diameter) of the positive electrode active material contained on the particles may be 1 μm to 100 μm, and the average particle size of the conductive particles may be 0.1 μm to 30 μm.

상술한 양극활물질 입자 및 도전입자의 크기는 양극활물질과 도전입자간 균질한 혼합이 이루어지면서도, 양극 공간(1)에의 투입시, 결착용액에 의해 입자상이 안정적으로 집전체(200)에 부착되면서 안정적인 물리적 강도를 갖는 활물질 층을 형성하기에 바람직한 크기이다. The size of the positive electrode active material particles and the conductive particles described above is uniformly mixed between the positive electrode active material and the conductive particles, and when the particle is stably attached to the current collector 200 by the binding solution when the anode active material 1 is injected into the anode space 1. It is a preferred size for forming an active material layer having stable physical strength.

본 발명의 일 실시예에 따른 제조방법에 있어, 제공된 전지 구조체의 양극 공간(1)에 집전체(200)를 삽입하고, 입자상을 채워넣은 후, 점도 조절제 및 바인더를 함유하는 결착 용액을 투입한 후 건조하여 양극을 제조할 수 있다.In the manufacturing method according to an embodiment of the present invention, the current collector 200 is inserted into the positive electrode space 1 of the provided battery structure, filled with particulates, and then a binder solution containing a viscosity modifier and a binder is added thereto. After drying, the positive electrode may be manufactured.

결착 용액은 투입된 입자상을 집전체 등에 물리적으로 안정되게 고정하며, 양극 공간(1)에 균질하게 입자상이 채워지도록 하는 역할을 수행한다. The binder solution physically and stably fixes the injected particulate phase to a current collector, and serves to uniformly fill the particulate space in the anode space 1.

결착 용액의 점도는 0.01 P에서 10,000 P일 수 있으며, 결착 용액에 함유된 점도 조절제는 카르복시메틸 셀룰로오스(CMC; carboxymethyl cellulose), 메틸 셀룰로오스(methylcellulose), 에틸 셀룰로오스(ethyl cellulose) 및 하이드록시프로필 메틸셀룰로오스(HPMC;hydroxypropyl methylcellulose)에서 하나 이상 선택된 셀룰로오스계일 수 있으며, 바인더는 폴리테트라플루오르에틸렌(PTFE; polytetrafluoroethylene), 폴리비닐알콜(PVA; polyvinyl alcohol), 폴리올레핀(polyolefine), 폴리에틸렌옥사이드(PEO; polyethylen oxide) 또는 이들의 혼합물을 포함할 수 있다. 이때, 결착 용액은 0.1~20 중량%의 바인더를 함유할 수 있다.The viscosity of the binder solution may be 0.01 P to 10,000 P, and the viscosity modifier contained in the binder solution is carboxymethyl cellulose (CMC), methyl cellulose, ethyl cellulose and hydroxypropyl methyl cellulose. (HPMC; hydroxypropyl methylcellulose) may be a cellulose-based selected one or more, the binder is polytetrafluoroethylene (PTFE; polytetrafluoroethylene), polyvinyl alcohol (PVA; polyvinyl alcohol), polyolefin (polyolefine), polyethylene oxide (PEO; polyethylen oxide) Or mixtures thereof. At this time, the binder solution may contain 0.1 to 20% by weight of the binder.

결착 용액의 용매는 상술한 점도 조절제 및 바인더가 용해되는 물질이면 무방하나, 저온에서의 용이한 건조 측면에서 물, 알코올, 글리세린 또는 이들의 혼합 용매를 사용할 수 있다.The solvent of the binder solution may be any substance in which the viscosity modifier and the binder are dissolved, but water, alcohol, glycerin, or a mixed solvent thereof may be used in view of easy drying at low temperatures.

결착 용액은 상온 상압 하 0.01 P 내지 10,000 P의 점도를 가질 수 있는데, 이는 집전체(200)가 삽입된 양극 공간에 채워진 입자상의 분말 입자간 빈 공간을 타고 흘러 입자상간 및 입자상과 집전체간을 균일하게 결착시키면서도 모세관력에 의해 양극 공간 내 균질하게 결착 용액이 분포할 수 있는 점도이다.The binder solution may have a viscosity of 0.01 P to 10,000 P at room temperature and normal pressure, which flows through the empty space between the particulate powder particles filled in the anode space into which the current collector 200 is inserted, and flows between the particles and between the particles and the current collector. It is a viscosity at which the binding solution can be uniformly distributed in the anode space by capillary force while binding uniformly.

결착 용액의 점도는 상술한 점도 조절제의 함량에 의해 조절될 수 있으며, 일 예로, 결착 용액은 용액의 점도가 0.01 P 내지 10,000 P가 되도록 점도 조절제를 함유할 수 있다.The viscosity of the binder solution may be adjusted by the content of the above-described viscosity regulator, for example, the binder solution may contain a viscosity modifier so that the viscosity of the solution is 0.01 P to 10,000 P.

결착 용액에 함유된 바인더는 입자상들 및 입자상과 집전체를 물리적 강도를 가지며 서로 결합시키는 역할을 수행할 수 있다. 결착 용액은 0.1 내지 20 중량%의 바인더를 함유할 수 있는데, 이를 통해 충전 또는 방전시 바인더에 의한 양극 반응을 방해하지 않고, 고체전해질 튜브를 통해 유입되는 나트륨 이온의 전도를 방해하지 않으며, 물리적으로 안정적인 양극이 제조되면서도, 결착 용액의 건조 후 균질하게 전해액이 투입될 수 있다.The binder contained in the binding solution may serve to bind the particles and the particles and the current collector to each other with physical strength. The binder solution may contain 0.1 to 20% by weight of the binder, which does not interfere with the anodic reaction by the binder during charging or discharging, does not interfere with the conduction of sodium ions entering through the solid electrolyte tube, and physically Even when a stable positive electrode is prepared, the electrolyte may be added homogeneously after drying of the binding solution.

본 발명의 일 실시예에 따른 제조방법에 있어, 양극 공간에 입자상을 투입하는 단계 및/또는 결착용액의 투입 후 건조가 이루어지기 전, 단시간 내에 보다 균일한 입자상의 채움(packing)을 위해 전지 구조체에 물리적 진동을 가하는 단계가 더 수행될 수 있다. 이때, 전지 구조체의 진동은 금속 하우징(100)의 측면 또는 밑면에 인가되는 초음파 진동을 포함한 진동 공정을 포함할 수도 있다.In the manufacturing method according to an embodiment of the present invention, the battery structure for a more uniform packing of the particulate form within a short time before the step of injecting the particulate into the anode space and / or after the addition of the binder solution is dried The step of applying a physical vibration to the can be further performed. In this case, the vibration of the battery structure may include a vibration process including an ultrasonic vibration applied to the side or bottom surface of the metal housing 100.

본 발명의 일 실시예에 따른 제조방법에 있어, 입자상은 양극 공간(1)의 적어도 일부 영역을 채우도록 투입될 수 있으며, 일 예로, 위킹튜브(420)와 안전튜브(410) 사이의 빈 공간을 채우는 용융 나트륨의 수위(높이)에 상응하는 수위로 입자상이 채워질 수 있다. 결착용액 또한, 양극 공간(1)의 적어도 일부 영역을 채우도록 투입될 수 있으며, 일 예로, 적어도 모든 입자상이 함침될 수 있는 수위로 결착용액이 채워질 수 있다. In the manufacturing method according to an embodiment of the present invention, the particulate may be injected to fill at least a portion of the anode space (1), for example, an empty space between the wicking tube 420 and the safety tube (410) Particulates can be filled to a level corresponding to the level (height) of molten sodium filling. The binding solution may also be added to fill at least a portion of the anode space 1, and, for example, the binding solution may be filled at a level where all particulates may be impregnated.

본 발명의 일 실시예에 따른 제조방법에 있어, 도 4에 도시한 일 예와 같이, 양극 공간(1)에 집전체(200)를 삽입한 후, 집전체가 투입된 양극 공간(1)에 양극활물질, 도전입자, 점도 조절제 및 바인더를 함유하는 활물질 슬러리를 투입하고 건조하는 단계가 수행될 수 있다.In the manufacturing method according to an embodiment of the present invention, as shown in the example shown in Figure 4, after inserting the current collector 200 in the positive electrode space 1, the positive electrode in the positive electrode space (1) in which the current collector is injected Injecting and drying an active material slurry containing an active material, conductive particles, a viscosity modifier, and a binder may be performed.

입자상 및 결착 용액을 순차적으로 투입하는 경우와 유사하게, 입자상에 함유되는 양극 활물질은 수산화니켈(Ni(OH)2)을 포함할 수 있으며, 전도성 입자인 도전 입자는 이차 전지, 특히 니켈수소 전지의 양극에 통상적으로 사용되는 도전 입자이면 사용 가능하다. 일 예로, 도전입자는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트, 그래핀 또는 이들의 혼합물을 함유할 수 있다.Similar to the case where the particulate and the binder solution are sequentially added, the positive electrode active material contained in the particulate may include nickel hydroxide (Ni (OH) 2 ), and the conductive particles, which are conductive particles, may be used in secondary batteries, particularly nickel hydrogen batteries. Any conductive particles commonly used for the positive electrode can be used. For example, the conductive particles may contain carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene, or mixtures thereof.

입자상 및 결착 용액을 순차적으로 투입하는 경우와 유사하게, 점도 조절제는 카르복시메틸 셀룰로오스(CMC; carboxymethyl cellulose), 메틸 셀룰로오스(methylcellulose), 에틸 셀룰로오스(ethyl cellulose) 및 하이드록시프로필 메틸셀룰로오스(HPMC;hydroxypropyl methylcellulose)에서 하나 이상 선택된 셀룰로오스계일 수 있으며, 바인더는 폴리테트라플루오르에틸렌(PTFE; polytetrafluoroethylene), 폴리비닐알콜(PVA; polyvinyl alcohol), 폴리올레핀(polyolefine), 폴리에틸렌옥사이드(PEO; polyethylen oxide) 또는 이들의 혼합물을 포함할 수 있으며, 슬러리의 용매는 점도 조절제 및 바인더가 용해되는 물질이면 무방하나, 저온에서의 용이한 건조 측면에서 물, 알코올, 글리세린 또는 이들의 혼합 용매를 사용할 수 있다.Similar to the case of sequential addition of particulate and binding solutions, the viscosity modifiers are carboxymethyl cellulose (CMC), methyl cellulose (methylcellulose), ethyl cellulose and hydroxypropyl methylcellulose (HPMC). And at least one selected from the group consisting of cellulose, and the binder may be polytetrafluoroethylene (PTFE), polyvinyl alcohol (PVA), polyolefine, polyethylene oxide (PEO) or mixtures thereof. The slurry may be a solvent in which the viscosity modifier and the binder are dissolved, but water, alcohol, glycerin, or a mixed solvent thereof may be used in view of easy drying at low temperatures.

활물질 슬러리는 집전체와의 안정한 결착, 원활하고 균질한 패킹(packing) 및 슬러리 건조 후 양극 공간에 투입되는 전해액에 의한 용이한 이온 전달 측면에서, 양극 활물질 100 중량부를 기준으로, 0.1 내지 20 중량부의 도전입자, 0.1 내지 10 중량부의 점도 조절제 및 0.1 내지 20 중량부의 바인더를 함유할 수 있으며, 양극활물질의 평균 입자 크기(직경)는 1㎛ 내지 100㎛일 수 있으며, 도전입자의 평균 입자 크기는 0.1㎛ 내지 30㎛일 수 있다.The active material slurry is 0.1 to 20 parts by weight based on 100 parts by weight of the positive electrode active material in terms of stable binding with the current collector, smooth and homogeneous packing, and easy ion transfer by the electrolyte solution that is added to the positive electrode space after slurry drying. It may contain conductive particles, 0.1 to 10 parts by weight of the viscosity regulator and 0.1 to 20 parts by weight of the binder, the average particle size (diameter) of the positive electrode active material may be 1㎛ to 100㎛, the average particle size of the conductive particles is 0.1 May be in the range from about 30 μm.

활물질 슬러리의 투입 후 및 투입된 슬러리의 건조 전, 전지 구조체에 물리적 진동을 가하는 단계가 더 수행될 수 있으며, 물리적 진동은 초음파 진동을 포함할 수 있다.After the addition of the active material slurry and before the drying of the injected slurry, a step of applying physical vibration to the battery structure may be further performed, and the physical vibration may include ultrasonic vibration.

본 발명의 일 실시예에 따른 제조방법에 있어, 활물질 슬러리는 양극 공간(1)의 적어도 일부 영역을 채우도록(packing) 투입될 수 있으며, 일 예로, 위킹튜브(420)와 안전튜브(410) 사이의 빈 공간을 채우는 용융 나트륨의 수위(높이)에 상응하는 수위로 슬러리가 채워질 수 있다. In the manufacturing method according to an embodiment of the present invention, the active material slurry may be added to fill at least a portion of the positive electrode space (1), for example, the wicking tube 420 and the safety tube 410 The slurry may be filled at a level corresponding to the level (height) of molten sodium filling the void space therebetween.

본 발명의 일 실시예에 따른 제조방법에 있어, 양극 공간에 집전체를 삽입하고, 입자상 및 결착 용액을 순차적으로 투입하거나, 활물질 슬러리의 투입이 이루어진 후, 결착 용액 또는 슬러리의 용매를 제거하는 건조 단계가 수행된다. In the manufacturing method according to an embodiment of the present invention, the current collector is inserted into the positive electrode space, and the particulate and the binder solution are sequentially added or the active material slurry is added, followed by drying to remove the solvent of the binder solution or slurry. Step is performed.

건조시, 활물질 슬러리를 집전체에 도포한 후 건조하여 이차전지용 전극을 제조하는 통상의 제조방법에서 수행되는 건조 조건을 이용할 수 있으며, 일 예로, 50~150℃ 의 온도에서 건조가 수행될 수 있다.In drying, the active material slurry may be applied to a current collector and then dried to use drying conditions performed in a conventional manufacturing method of manufacturing an electrode for a secondary battery. For example, drying may be performed at a temperature of 50 to 150 ° C. .

건조 단계가 수행된 후, 양극 공간에 전해액을 투입하는 단계가 더 수행될 수 있다.After the drying step is performed, the step of introducing the electrolyte into the anode space may be further performed.

전해액은 나트륨 이온이 빠르고 균일하게 전도되는 역할을 수행하며, 전해액에 함유되는 전해질염(나트륨염)은 수산화물, 붕산염, 인산염 또는 이들의 혼합물을 포함할 수 있다. 상세하게, 전해질염은 수산화나트륨(NaOH), 인산삼나트륨(Na3PO4), 피로인산나트륨(Na2HPO4), 메타붕산나트륨(NaBO2), 붕사(Na2B4O7), 붕산(H3BO3) 또는 이들의 혼합물을 포함할 수 있다. 전해액은 수계 전해액을 포함하며, 전해액은 2 내지 50중량%의 전해질염을 함유할 수 있다.The electrolyte serves to conduct sodium ions quickly and uniformly, and the electrolyte salt (sodium salt) contained in the electrolyte may include hydroxide, borate, phosphate, or a mixture thereof. Specifically, the electrolyte salt may be sodium hydroxide (NaOH), trisodium phosphate (Na 3 PO 4 ), sodium pyrophosphate (Na 2 HPO 4 ), sodium metaborate (NaBO 2 ), borax (Na 2 B 4 O 7 ), Boric acid (H 3 BO 3 ) or mixtures thereof. The electrolyte solution includes an aqueous electrolyte solution, and the electrolyte solution may contain 2 to 50 wt% of an electrolyte salt.

전지 구조체를 제공한 후 집전체를 삽입하기 전 또는 건조 단계가 수행된 후 위킹 튜브에 금속 나트륨을 투입하는 단계가 더 수행될 수 있으며, 전해액 및 나트륨의 투입 후, 금속 하우징 상부를 밀폐하는 단계, 금속 하우징 외벽에 외부 로드와의 전기적 폐회로(closed loop)를 이룰 수 있는 전극 단자를 형성하는 단계가 더 수행될 수 있다.After the providing of the battery structure before inserting the current collector or after the drying step is carried out the step of introducing the metal sodium into the wicking tube, after the addition of the electrolyte and sodium, sealing the upper part of the metal housing, Forming an electrode terminal on the outer wall of the metal housing, which may make an electrical closed loop with the external rod, may be further performed.

이때, 나트륨의 투입, 금속 하우징의 밀폐 및 전극 단자의 형성은 도 1과 유사한 구조를 갖는 통상의 나트륨유황 전지의 제조방법에서 사용된 방법 및 구조를 사용하여도 무방함에 따라, 이에 대한 설명은 생략한다.At this time, the introduction of sodium, the sealing of the metal housing and the formation of the electrode terminal may be used in the method and structure used in the conventional method for manufacturing a sodium sulfur battery having a structure similar to Figure 1, the description thereof is omitted. do.

본 발명은 나트륨 이차전지를 제공한다.The present invention provides a sodium secondary battery.

본 발명에 따른 나트륨 이차전지는 나트륨 이온 전도성 고체전해질, 음극 및 양극을 포함한다. The sodium secondary battery according to the present invention includes a sodium ion conductive solid electrolyte, a negative electrode and a positive electrode.

나트륨 이온 전도성 고체전해질은 음극 공간과 양극 공간을 구획한다. 상세하게, 나트륨 이온 전도성 고체전해질은 전지 내부 구성물을 외부와 분리시키는 전지 케이스(전도성 케이스를 포함함) 내부 공간에 위치하여, 전지 케이스 내부 공간을 음극 공간과 양극 공간으로 구획할 수 있다. The sodium ion conductive solid electrolyte partitions the cathode space and the anode space. In detail, the sodium ion conductive solid electrolyte may be disposed in an inner space of a battery case (including a conductive case) that separates the battery internal components from the outside, and may partition the inner space of the battery case into a cathode space and an anode space.

양극 공간에는 집전체가 위치할 수 있으며, 집전체가 위치하는 양극 공간은 양극활물질을 함유하는 입자상으로 충진될 수 있다. 즉, 입자상은 집전체가 위치하는 양극 공간 전체 또는 일정 영역을 일정 높이로 채울 수 있다.The current collector may be located in the positive electrode space, and the positive electrode space in which the current collector is located may be filled with particulates containing a positive electrode active material. That is, the particulate form may fill the entire anode space or a predetermined region where the current collector is located at a predetermined height.

즉, 본 발명에 따른 나트륨 이차전지는 음극 공간과 양극 공간을 구획하는 나트륨 이온 전도성 고체전해질; 음극이 위치하는 음극 공간; 및 집전체가 장입되고 양극활물질을 포함하는 입자상이 충진된(패킹된) 양극 공간;을 포함할 수 있으며, 이러한 나트륨 이차전지는 상술한 제조방법에 의해 제조된 것일 수 있다. That is, the sodium secondary battery according to the present invention comprises a sodium ion conductive solid electrolyte partitioning the cathode space and the anode space; A cathode space in which the cathode is located; And a positive electrode space in which a current collector is charged and filled with particles (packed) including a positive electrode active material. The sodium secondary battery may be manufactured by the above-described manufacturing method.

본 발명에 따른 나트륨 이차전지는 집전체에 양극활물질을 함유하는 활물질층이 적층된 형태가 아닌, 양극활물질을 함유하는 입자상이 양극 공간을 채우고, 이러한 양극 공간을 채우는 입자상에 집전체가 장입되어 있는 형태임에 따라, 전극(양극)의 롤링 중 발생하는 양극 활물질층의 박리 또는 탈착으로부터 자유로우며, 단지 양극 공간의 크기 및/또는 집전체의 권취 간격을 조절함으로써 양극 활물질의 두께 조절이 가능하며, 전지의 용량 설계가 극히 용이하고 자유로우며, 양산 공정이 단순해져 투자비 및 생산원가 측면에서 절감이 가능한 정점이 있다.In the sodium secondary battery according to the present invention, the active material layer containing the positive electrode active material is not laminated in the current collector, but the particulate phase containing the positive electrode active material fills the positive electrode space, and the current collector is charged on the particles filling the positive electrode space. According to the shape, it is free from peeling or desorption of the positive electrode active material layer generated during rolling of the electrode (anode), and it is possible to control the thickness of the positive electrode active material by only adjusting the size of the positive electrode space and / or the winding interval of the current collector. The capacity design of the battery is extremely easy and free, and the mass production process is simplified, which can reduce the investment cost and production cost.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 집전체는 폼(foam), 필름(film), 메쉬(mesh), 펠트(felt) 또는 다공성 박(perforated film)의 형태일 수 있으며, 집전체는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트 및 그래핀에서 하나 이상 선택될 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the current collector may be in the form of a foam (film), film (film), mesh (mesh), felt (felt) or porous foil (perforated film), The whole may be one or more selected from carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite and graphene.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 양극 공간에 위치하는 집전체는 권취된 형상이거나, 다수개의 집전체가 서로 이격 배열된 구조일 수 있다. 종래의 제조방법을 기준으로 상술하면, 집전체가 권취된 형상인 경우, 집전체의 권취 간격에 의해 집전체에 코팅되는 활물질의 두께가 제어될 수 있다. 구체적인 일 예로, 집전체의 권취 간격은 0.01 내지 5mm일 수 있다. 집전체가 서로 이격 배열된 경우, 배열된 집전체들은 상단, 하단 또는 그 측면이 서로 연결되어 전기적으로 통전된 상태일 수 있으며, 집전체간의 이격 거리는 0.01 내지 5mm일 수 있다. 집전체의 배열은 양극 공간의 물리적 형상을 고려하여 균일하게 전기장이 형성될 수 있는 구조이면 족하다. 비 한정적인 일 예로, 양극에 투입되는 집전체는 다수개의 집전체가 상단이 전도성 부재로 서로 연결되며 등 간격으로 서로 이격 배열된 구조일 수 있으며, 상단이 전도성 부재로 서로 연결되며, 지름이 상이한 다수개의 원통, 타원형 통 또는 삼각 내지 팔각의 다각통 형상의 집전체가 동심 구조를 가지며 이격 배열된 구조일 수 있다. 집전체의 높이는 적어도 양극 공간에서 입자상으로 채워지는 높이 이상일 수 있다. 즉, 집전체는 입자상에 일정 부분 함입된 구조를 가질 수 있다. In the sodium secondary battery according to an embodiment of the present invention, the current collector located in the positive electrode space may be a wound shape or a structure in which a plurality of current collectors are spaced apart from each other. In detail based on the conventional manufacturing method, when the current collector has a wound shape, the thickness of the active material coated on the current collector may be controlled by the winding interval of the current collector. As a specific example, the winding interval of the current collector may be 0.01 to 5mm. When the current collectors are arranged to be spaced apart from each other, the arranged current collectors may be in an electrically energized state in which the top, bottom, or sides thereof are connected to each other, and the separation distance between the current collectors may be 0.01 to 5 mm. The arrangement of the current collector may be sufficient as long as the electric field can be uniformly formed in consideration of the physical shape of the anode space. As a non-limiting example, the current collector to be injected into the positive electrode may have a structure in which a plurality of current collectors are connected to each other by a conductive member and spaced apart from each other at equal intervals. The plurality of cylinders, elliptical cylinders or triangular to octagonal polygonal collectors may have concentric structures and spaced apart arrangements. The height of the current collector may be at least a height filled with particulates in the anode space. That is, the current collector may have a structure partially embedded in the particles.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 나트륨 이온 전도성 고체전해질은 통상의 나트륨 이차전지에 나트륨 이온의 선택적 전도를 위해 사용되는 물질이면 무방하다. 구체적인 일 예로, 나트륨 이온 전도성 고체전해질은 나트륨초이온전도체(Na super ionic conductor, NaSICON), β"알루미나 또는 이들의 적층체를 포함할 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the sodium ion conductive solid electrolyte may be a material used for selective conduction of sodium ions to a conventional sodium secondary battery. As a specific example, the sodium ion conductive solid electrolyte may include a sodium super ionic conductor (NaSICON), β ″ alumina, or a laminate thereof.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 입자상은 양극활물질을 함유할 수 있으며, 입자상으로 함유되는 양극활물질(양극활물질 입자)은 수산화니켈을 포함할 수 있다. 이때, 양극 반응은 Ni(OH)2↔NiOOH일 수 있다. In the sodium secondary battery according to an embodiment of the present invention, the particulate form may contain a positive electrode active material, and the positive electrode active material (positive electrode active material particles) contained in the particulate may include nickel hydroxide. In this case, the anode reaction may be Ni (OH) 2 ↔NiOOH.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 입자상으로 함유되는 양극활물질의 평균 입자 크기(직경)는 1㎛ 내지 100㎛일 수 있다. 양극활물질의 평균 입자 크기가 1㎛ 미만으로 너무 작을 경우 양극활물질의 비표면적은 커지나 바인더의 균일한 분포가 어려워, 전지내 양극을 구성하는 입자상의 결착 및 물리적 안정성이 감소할 수 위험이 있으며, 입자상의 결착을 위해 과량의 바인더가 요구될 수 있어 나트륨 이온과 반응할 수 있는 실질적 표면적(입자상의 표면적)이 감소할 위험이 있다. 양극활물질의 평균 입자 크기가 100㎛를 초과하도록 너무 큰 경우, 양극활물질의 비표면적 감소에 의해 전지 특성이 저하될 위험이 있다.In the sodium secondary battery according to an embodiment of the present invention, the average particle size (diameter) of the positive electrode active material contained in particulate form may be 1 μm to 100 μm. If the average particle size of the positive electrode active material is too small, less than 1 μm, the specific surface area of the positive electrode active material becomes large, but the uniform distribution of the binder is difficult, which may reduce the binding and physical stability of the particles forming the positive electrode in the battery. Excess binder may be required for the binding of P, thereby reducing the substantial surface area (particulate surface area) that can react with sodium ions. If the average particle size of the positive electrode active material is too large to exceed 100 µm, there is a risk that the battery characteristics are deteriorated by the reduction of the specific surface area of the positive electrode active material.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 입자상은 양극활물질과 함께 도전입자를 더 함유할 수 있다. 도전입자는 양극 공간을 일정 높이로 채우는 입자상에 함유되는 양극활물질과 집전체간의 저저항 경로를 형성하여, 전지의 내부 저항을 감소시킬 수 있다. 구체적으로 도전입자는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트, 그래핀 또는 이들의 혼합물을 함유할 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the particulate may further contain conductive particles together with the positive electrode active material. The conductive particles form a low resistance path between the positive electrode active material and the current collector contained on the particles filling the positive electrode space to a certain height, thereby reducing the internal resistance of the battery. Specifically, the conductive particles may contain carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene or a mixture thereof.

구체적으로, 입자상은 양극활물질 100 중량부를 기준으로 0.5 내지 20 중량부의 도전입자를 더 함유할 수 있다. 양극활물질 대비 도전 입자의 중량비는 양극활물질 에서 발생하는 양극 반응을 방해하지 않으면서도 양극활물질과 집전체간 균일하게 저저항 경로가 형성될 수 있는 중량비이다. Specifically, the particulate form may further contain 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material. The weight ratio of the conductive particles to the positive electrode active material is a weight ratio in which a low resistance path can be uniformly formed between the positive electrode active material and the current collector without interfering with the positive electrode reaction generated in the positive electrode active material.

양극활물질의 평균 입자 크기(직경)는 1㎛ 내지 100㎛일 수 있으며, 도전입자의 평균 입자 크기는 0.1㎛ 내지 30㎛일 수 있다. 이러한 도전 입자의 크기는 동일한 부피의 양극 공간에서 도전 입자에 의해 양극활물질이 채워지는 양이 감소되는 것을 방지하며, 양극활물질의 입자간 공간에 도전입자가 위치하며 효과적으로 저저항 경로가 형성될 수 있는 크기이다.The average particle size (diameter) of the positive electrode active material may be 1 μm to 100 μm, and the average particle size of the conductive particles may be 0.1 μm to 30 μm. The size of the conductive particles prevents the amount of the positive electrode active material from being filled by the conductive particles in the same volume of the positive electrode space, and reduces the amount of conductive particles in the interstitial space of the positive electrode active material. Size.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 집전체가 위치한 양극 공간을 채우는 입자상은 바인더에 의해 결착된 상태일 수 있으며, 이러한 결착은 용액상 바인더의 건조에 의해 이루어진 것일 수 있다. 즉, 양극 공간의 입자간 빈 공간에 위치한 용액상의 바인더가 액상(용매를 포함함) 휘발 제거에 의해 액상에서 고상으로 상변태하며 입자와 입자간 및 입자와 집전체간 결착된 것일 수 있다.In the sodium secondary battery according to the exemplary embodiment of the present invention, the particulate form filling the positive electrode space in which the current collector is located may be bound by a binder, and the binding may be made by drying a solution binder. That is, the solution phase binder located in the inter-particle void space of the anode space may be phase-converted from the liquid phase to the solid phase by volatilization of the liquid phase (including the solvent), and may be bound between the particles and the particles and between the particles and the current collector.

보다 구체적으로, 양극 공간을 채우는 입자상은 용액상으로 양극 공간에 투입된 바인더의 건조에 의해 입자간 및 입자와 집전체간 결착된 것일 수 있다.More specifically, the particulate form filling the positive electrode space may be a binder between particles and between the particles and the current collector by drying of a binder injected into the positive electrode space as a solution.

상술한 제조방법을 참고하여, 양극 공간을 채우는 입자상은 분말상으로 양극 공간에 투입된 후, 용액상의 바인더가 양극 공간에 투입 및 건조됨으로써, 양극 공간 내에서 결착된 것일 수 있다.With reference to the above-described manufacturing method, the particulate form filling the anode space may be a binder in the anode space by being injected into the anode space in powder form, and then added to the anode space and dried in solution.

상술한 제조방법을 참고하여, 양극 공간을 채우는 입자상은 용매에 용해된 바인더와 함께 슬러리 상으로 양극 공간에 투입된 후 건조됨으로써, 양극 공간 내에서 결착된 것일 수 있다. Referring to the above-described manufacturing method, the particulate form filling the anode space may be bound in the anode space by being poured into the anode space as a slurry together with a binder dissolved in a solvent and then dried.

즉, 본 발명의 일 실시예에 따른 양극은 양극 공간 내에서 직접적으로 제조된 것일 수 있다.That is, the positive electrode according to the embodiment of the present invention may be manufactured directly in the positive electrode space.

본 발명의 일 실시예에 따른 양극은 양극 활물질 100 중량부를 기준으로, 0.1 내지 20 중량부의 바인더를 함유할 수 있다. 이러한 바인더의 함량은 양극 공간을 일정 높이로 충진하는 입자상을 안정적으로 결착시키면서도 입자상의 반응성 표면적 감소를 최소화할 수 있는 양이다. 바인더는 폴리테트라플루오르에틸렌(PTFE; polytetrafluoroethylene), 폴리비닐알콜(PVA; polyvinyl alcohol), 폴리올레핀(polyolefine), 폴리에틸렌옥사이드(PEO; polyethylen oxide) 또는 이들의 혼합물을 포함할 수 있다. The positive electrode according to the exemplary embodiment of the present invention may contain 0.1 to 20 parts by weight of the binder based on 100 parts by weight of the positive electrode active material. The binder content is an amount that can stably bind the particulate phase filling the anode space to a certain height while minimizing the reduction of the reactive surface area of the particulate phase. The binder may include polytetrafluoroethylene (PTFE), polyvinyl alcohol (PVA), polyolefine, polyethylene oxide (PEO) or a mixture thereof.

또한, 본 발명의 일 실시예에 따른 양극은 양극 활물질 100 중량부를 기준으로, 0.1 내지 10 중량부의 점도 조절제를 더 함유할 수 있다. 이러한 점도조절제는 양극 공간 내에서 직접적으로 양극이 제조됨에 따라, 양극에 잔류하는 잔류물일 수 있다. 상세하게, 양극 공간 내에 상술한 결착용액 또는 슬러리(양극활물질 슬러리)의 용이한 투입 및 균일한 분포를 위해 결착용액 또는 슬러리가 점도조절제를 함유할 수 있으며, 용매의 휘발 제거시 이러한 점도조절제가 양극에 잔류할 수 있다. 점도 조절제는 카르복시메틸 셀룰로오스(CMC; carboxymethyl cellulose), 메틸 셀룰로오스(methylcellulose), 에틸 셀룰로오스(ethyl cellulose) 및 하이드록시프로필 메틸셀룰로오스(HPMC;hydroxypropyl methylcellulose)에서 하나 이상 선택된 셀룰로오스계일 수 있다. In addition, the positive electrode according to an embodiment of the present invention may further contain 0.1 to 10 parts by weight of a viscosity modifier based on 100 parts by weight of the positive electrode active material. Such a viscosity modifier may be a residue remaining on the positive electrode as the positive electrode is manufactured directly in the positive electrode space. Specifically, the binder solution or slurry may contain a viscosity control agent for easy introduction and uniform distribution of the above-mentioned binding solution or slurry (positive electrode active material slurry) in the positive electrode space, and when the solvent is volatilized, the viscosity control agent may be positive May remain. The viscosity modifier may be a cellulose based one or more selected from carboxymethyl cellulose (CMC), methyl cellulose, methyl cellulose, ethyl cellulose and hydroxypropyl methylcellulose (HPMC).

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 양극은 전해액을 더 포함할 수 있으며, 양극 공간이 입자상에 의해 충진되고 남는 빈 공간, 즉, 입자와 입자간 공간, 입자와 전지 케이스간 공간, 및/또는 입자와 집전체간의 공간은 전해액에 의해 채워질 수 있다. 즉, 양극은 양극 공간에 위치하는 집전체; 양극 공간을 충진하는 입자상; 및 적어도 입자간 빈 공간을 채우는 전해액;을 포함할 수 있으며, 이때, 입자상은 바인더에 의해 결착된 상태의 입자상일 수 있다.In the sodium secondary battery according to an embodiment of the present invention, the positive electrode may further include an electrolyte, and the empty space in which the positive electrode space is filled and left by the particle phase, that is, the space between the particles and the particle, the space between the particles and the battery case And / or the space between the particle and the current collector may be filled by the electrolyte solution. That is, the positive electrode includes a current collector located in the positive electrode space; Particulate form filling the anode space; And an electrolyte solution filling at least the inter-particle void space, wherein the particulate form may be particulate in a state bound by a binder.

전해액은 나트륨 이온이 빠르고 균일하게 전도하는 역할을 수행하며, 전해액에 함유되는 전해질염(나트륨염)은 수산화물, 붕산염, 인산염 또는 이들의 혼합물을 포함할 수 있다. 상세하게, 전해질염은 수산화나트륨(NaOH), 인산삼나트륨(Na3PO4), 피로인산나트륨(Na2HPO4), 메타붕산나트륨(NaBO2), 붕사(Na2B4O7), 붕산(H3BO3) 또는 이들의 혼합물을 포함할 수 있다. 이때, 전해액은 수계 또는 비수계 전해액을 포함하며, 전해액은 2 내지 50중량%의 전해질염을 함유할 수 있다.The electrolyte serves to conduct sodium ions quickly and uniformly, and the electrolyte salt (sodium salt) contained in the electrolyte may include hydroxide, borate, phosphate, or a mixture thereof. Specifically, the electrolyte salt may be sodium hydroxide (NaOH), trisodium phosphate (Na 3 PO 4 ), sodium pyrophosphate (Na 2 HPO 4 ), sodium metaborate (NaBO 2 ), borax (Na 2 B 4 O 7 ), Boric acid (H 3 BO 3 ) or mixtures thereof. In this case, the electrolyte may include an aqueous or non-aqueous electrolyte, and the electrolyte may contain 2 to 50 wt% of an electrolyte salt.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 음극 공간에 위치하는 음극은 통상의 나트륨 이차전지에서 사용되는 음극활물질을 포함한다. 구체적으로, 음극은 음극 집전체에 음극활물질층이 형성된 적층체이거나, 금속 나트륨일 수 있다. 보다 구체적으로, 전지의 동작 상태에서 음극은 용융 나트륨일 수 있다. In the sodium secondary battery according to an embodiment of the present invention, the negative electrode positioned in the negative electrode space includes a negative electrode active material used in a conventional sodium secondary battery. Specifically, the negative electrode may be a laminate in which a negative electrode active material layer is formed on the negative electrode current collector, or may be metal sodium. More specifically, in the operating state of the cell, the negative electrode may be molten sodium.

본 발명의 일 실시예에 따른 나트륨 이차전지에 있어, 양극 공간을 충진하는 입자상의 양에 의해 전지의 용량이 설계될 수 있음에 따라, 동일한 부피의 양극 공간일지라도, 입자상에 의해 충진되는 정도에 의해 전지 용량이 달라질 수 있다.In the sodium secondary battery according to one embodiment of the present invention, the capacity of the battery can be designed by the amount of particulates filling the anode space, so that even if the anode volume of the same volume, by the degree of filling by the particulate phase Battery capacity may vary.

이에 따라, 양극 공간을 충진하는 입자상의 양(입자상에 의해 채워지는 양극공간의 높이, 또는 입자상에 의해 채워지는 양극 공간의 부피)은 목표하는 전지 설계를 고려하여 적절히 조절될 수 있다.Accordingly, the amount of particulate matter (the height of the anode space filled by the particulate phase, or the volume of the anode space filled by the particulate phase) filling the anode space can be appropriately adjusted in consideration of the target cell design.

그러나, 동일 부피의 양극 공간에서, 전지의 용량 및 충방전 효율을 극대화하며, 전지의 빠른 충방전 속도를 담보하는 측면에서, 입자상은 음극 공간에서의 용융 나트륨의 수위에 상응하는 높이로 양극 공간을 충진할 수 있다. 즉, 입자상은 적어도 음극 공간의 용융 나트륨(음극활물질) 수위에 해당하는 높이로 양극 공간을 채울 수 있으며, 양극 공간 전체를 모두 채울 수 있다.However, in the same volume of anode space, in terms of maximizing the capacity and charge / discharge efficiency of the battery and ensuring fast charge and discharge rate of the battery, the particulates are formed at a height corresponding to the level of molten sodium in the cathode space. Can be filled. That is, the particulate can fill the anode space at a height corresponding to at least the level of molten sodium (cathode active material) in the cathode space, it can fill the entire anode space.

도 5는 본 발명의 일 실시예에 따른 나트륨 이차전지의 일 단면을 도시한 예이다. 도 5는 음극이 중심에 위치하는 튜브형 나트륨 이차전지의 구조를 일 예로 도시한 것이나, 본 발명에 따른 나트륨 이차전지는 통상의 나트륨유황 이차전지에서 알려진 어떠한 전지 구조를 가져도 무방하다. 구체적으로, 본 발명에 따른 나트륨 이차전지가 양극이 중심에 위치하는 튜브형 나트륨 이차전지의 구조를 가질 수 있음은 물론이며, 평판형 구조를 가질 수 있음은 물론이다. 5 is an example illustrating a cross section of a sodium secondary battery according to an exemplary embodiment of the present invention. FIG. 5 illustrates an example of a structure of a tubular sodium secondary battery in which a negative electrode is located at the center, but the sodium secondary battery according to the present invention may have any battery structure known in a conventional sodium sulfur secondary battery. Specifically, of course, the sodium secondary battery according to the present invention may have a structure of a tubular sodium secondary battery in which a positive electrode is located at the center, and of course, may have a flat structure.

도 5와 유사하게, 본 발명의 일 실시예에 따른 나트륨 이차전지는 최 외각에 전지 케이스에 해당하는 금속 하우징(100)이 위치하며, 그 중심에 위킹 튜브(420)가 위치하고, 금속 하우징(100)의 내부에 금속 하우징(100)의 외측에서 내측 방향으로, 고체전해질 튜브(300), 안전 튜브(410) 및 위킹 튜브(420)가 순차적으로 구비될 수 있다. 즉, 금속 하우징(100)의 외측에서 내측으로, 고체전해질 튜브(300)안전 튜브(410) 및 위킹 튜브(420)가 동심구조를 가지며, 금속 하우징(100)과 고체전해질 튜브(300)사이의 양극 공간에 집전체(200)가 위치할 수 있다. 집전체(200)는 도 5에 도시한 바와 같이 롤링된 상태일 수 있으나, 다수개의 집전체가 서로 이격되어 양극 공간에 위치할 수 있음은 물론이다. 집전체(200)가 위치하는 양극 공간은, 양극 공간에 액상으로 양극 공간에 투입된 바인더의 건조에 의해 서로 결착된 입자상(P)으로 채워질 수 있다. 입자상(P)으로 충진된 양극 공간의 높이는 적어도 음극의 용융 나트륨의 수위, 구체적으로, 위킹튜브(420)와 안전튜브(410) 사이의 빈 공간을 채우는 용융 나트륨의 수위(H)에 상응하는 수위 내지 그 이상으로 입자상이 채워질 수 있다. 이때, 양극 공간에서 입자상으로 충진되고 남는 빈 공간, 즉, 입자와 입자간의 공간, 입자와 금속 하우징간의 공간 및/또는 입자와 집전체간의 공간은 전해액으로 채워질 수 있으며, 전해액은 적어도 양극 공간에 위치하는 모든 입자상이 함침될 수 있는 수위로 양극 공간을 채울 수 있다. 비록, 도 5에 도시하지 않았으나, 본 발명의 일 실시예에 따른 나트륨 전지는 금속 하우징(100) 상부에 위치하여 금속 하우징 내부를 밀폐시키는 덮개, 링 형상을 가지며 금속 하우징(100) 상측에 위치하여 금속 하우징(100)과 고체전해질 튜브(300) 사이를 전기적으로 절연시키는 절연체, 금속 하우징(100)의 상단 둘레에 위치하는 전극단자가 구비될 수 있음은 물론이며, 음극 공간에 장입되는 집전체를 더 포함할 수 있음은 물론이다. Similar to FIG. 5, in the sodium secondary battery according to the exemplary embodiment of the present invention, a metal housing 100 corresponding to the battery case is positioned at the outermost portion, a wicking tube 420 is positioned at the center thereof, and the metal housing 100 is located at the center thereof. In the inside of the metal housing 100 from the outer side to the inside, the solid electrolyte tube 300, the safety tube 410 and the wicking tube 420 may be provided in sequence. That is, from the outside of the metal housing 100 to the inside, the solid electrolyte tube 300, the safety tube 410 and the wicking tube 420 has a concentric structure, between the metal housing 100 and the solid electrolyte tube 300 The current collector 200 may be located in the anode space. The current collector 200 may be in a rolled state as shown in FIG. 5, but a plurality of current collectors may be spaced apart from each other and positioned in the positive electrode space. The positive electrode space in which the current collector 200 is located may be filled with particulates P bound to each other by drying a binder injected into the positive electrode space in a liquid phase in the positive electrode space. The height of the anode space filled with particulate matter (P) is at least a level of molten sodium of the cathode, specifically, a level corresponding to the level of molten sodium (H) filling the void space between the wicking tube 420 and the safety tube 410. The particulate phase may be filled up to or more. In this case, the empty space remaining in the anode space and filled with particles, that is, the space between the particles and the particles, the space between the particles and the metal housing, and / or the space between the particles and the current collector may be filled with the electrolyte, and the electrolyte is located at least in the anode space. It is possible to fill the anode space with a level where all particulates can be impregnated. Although not shown in FIG. 5, the sodium battery according to the exemplary embodiment of the present invention is disposed on the metal housing 100 to have a cover and ring shape to seal the inside of the metal housing, and is located above the metal housing 100. An insulator electrically insulating between the metal housing 100 and the solid electrolyte tube 300 may be provided, and an electrode terminal positioned around an upper end of the metal housing 100 may be provided. Of course, it may include more.

Claims (25)

a) 나트륨 이온 전도성 고체전해질에 의해 음극 공간과 구획되는 양극 공간에 집전체를 삽입하는 단계; 및a) inserting a current collector into a positive electrode space partitioned from the negative electrode space by a sodium ion conductive solid electrolyte; And b) 집전체가 삽입된 양극 공간에 양극활물질을 함유하는 활물질을 투입하는 단계;b) injecting an active material containing a positive electrode active material into the positive electrode space into which the current collector is inserted; 를 포함하는 나트륨 이차전지의 제조방법.Sodium secondary battery manufacturing method comprising a. 제 1항에 있어서,The method of claim 1, 상기 b) 단계는Step b) b1) 상기 양극 공간에 양극활물질 및 도전입자를 함유하는 입자상을 투입하는 단계; 및b1) injecting a particulate phase containing a cathode active material and conductive particles into the anode space; And b2) 상기 양극 공간에 점도 조절제 및 바인더를 함유하는 결착 용액을 투입하고 건조하는 단계; b2) putting a binder solution containing a viscosity modifier and a binder into the anode space and drying; 를 포함하는 나트륨 이차전지의 제조방법.Sodium secondary battery manufacturing method comprising a. 제 1항에 있어서,The method of claim 1, 상기 b) 단계는Step b) b3) 상기 양극 공간에 양극활물질, 도전입자, 점도 조절제 및 바인더를 함유하는 슬러리를 투입하고 건조하는 단계;b3) injecting and drying a slurry containing a positive electrode active material, a conductive particle, a viscosity modifier and a binder in the positive electrode space; 를 포함하는 나트륨 이차전지의 제조방법.Sodium secondary battery manufacturing method comprising a. 제 1항에 있어서,The method of claim 1, 상기 a) 단계는 Step a) 양 단 중 일 단이 밀폐되고 다른 일 단이 개방된 원통형의 금속 하우징, 상기 금속 하우징 내부에 위치하며, 금속 하우징의 외측에서 내측으로 순차적으로 동심 구조를 가지며 위치하는 나트륨 이온 전도성 고체전해질 튜브, 안전튜브 및 용융 나트륨이 담지되는 위킹튜브를 제공하는 단계;를 포함하며,Cylindrical metal housing, one end of which is sealed at one end and the other end is open, is located inside the metal housing, sodium ion conductive solid electrolyte tube positioned with a concentric structure sequentially from the outside of the metal housing to the inside, safety Providing a tube and a wicking tube loaded with molten sodium; 상기 양극 공간은 상기 고체전해질 튜브와 금속 하우징 사이의 공간인 나트륨 이차전지의 제조방법.And the cathode space is a space between the solid electrolyte tube and the metal housing. 제 4항에 있어서,The method of claim 4, wherein 상기 집전체는 상기 금속 하우징과 동심 구조를 갖도록 권취된 나트륨 이차전지의 제조방법. The current collector is a method of manufacturing a sodium secondary battery wound so as to have a concentric structure with the metal housing. 제 1 항에 있어서,The method of claim 1, 상기 집전체는 폼(foam), 필름(film), 메쉬(mesh), 펠트(felt) 또는 다공성 박(perforated film) 형상인 나트륨 이차전지의 제조방법.The current collector is a method of manufacturing a sodium secondary battery in the form of a foam (film), film (mesh), felt (felt) or porous foil (perforated film). 제 1항에 있어서,The method of claim 1, 상기 집전체는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트 및 그래핀에서 하나 이상 선택된 나트륨 이차전지의 제조방법.The current collector is a method of manufacturing a sodium secondary battery at least one selected from carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite and graphene. 제 3항에 있어서,The method of claim 3, 상기 도전입자는 카본, 니켈, 티타늄, 이트륨, 칼슘, 크롬, 코발트, 아연, 그라파이트, 그래핀 또는 이들의 혼합물을 포함하는 나트륨 이차전지의 제조방법. The conductive particle is a method of manufacturing a sodium secondary battery comprising carbon, nickel, titanium, yttrium, calcium, chromium, cobalt, zinc, graphite, graphene or a mixture thereof. 제 8항에 있어서,The method of claim 8, 상기 입자상은 양극활물질 100 중량부를 기준으로 0.5 내지 20 중량부의 도전입자를 함유하는 나트륨 이차전지의 제조방법.The particulate phase is a method of manufacturing a sodium secondary battery containing 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material. 제1항에 있어서,The method of claim 1, 상기 양극활물질은 수산화니켈(Ni(OH)2)을 포함하는 나트륨 이차전지의 제조방법.The cathode active material is a method of manufacturing a sodium secondary battery containing nickel hydroxide (Ni (OH) 2 ). 제2항에 있어서,The method of claim 2, 상기 결착 용액의 점도는 0.01 P 내지 10,000 P인 나트륨 이차전지의 제조방법.The binder solution is a viscosity of the sodium secondary battery manufacturing method of 0.01 P to 10,000 P. 제3항에 있어서,The method of claim 3, 상기 슬러리의 점도는 0.01 P 내지 10,000 P인 나트륨 이차전지의 제조방법.The viscosity of the slurry is 0.01 P to 10,000 P manufacturing method of the sodium secondary battery. 제2항 또는 제3항에 있어서,The method according to claim 2 or 3, 상기 점도 조절제는 카르복시메틸 셀룰로오스(CMC; carboxymethyl cellulose), 메틸 셀룰로오스(methylcellulose), 에틸 셀룰로오스(ethyl cellulose) 및 하이드록시프로필 메틸셀룰로오스(HPMC;hydroxypropyl methylcellulose)에서 하나 이상 선택된 셀룰로오스계를 포함하며, 상기 바인더는 폴리테트라플루오르에틸렌(PTFE; polytetrafluoroethylene), 폴리비닐알콜(PVA; polyvinyl alcohol), 폴리올레핀(polyolefine), 폴리에틸렌옥사이드(PEO; polyethylen oxide) 또는 이들의 혼합물을 포함하는 나트륨 이차전지의 제조방법.The viscosity modifier includes a cellulose system selected from at least one selected from carboxymethyl cellulose (CMC), methyl cellulose, methyl cellulose, ethyl cellulose and hydroxypropyl methylcellulose, and the binder The polytetrafluoroethylene (PTFE; polytetrafluoroethylene), polyvinyl alcohol (PVA; polyvinyl alcohol), polyolefin (polyolefine), polyethylene oxide (PEO; polyethylen oxide) or a mixture thereof. 제2항에 있어서,The method of claim 2, 상기 결착 용액은 0.1~20 중량%의 바인더를 함유하는 나트륨 이차전지의 제조방법.The binder solution is a method of manufacturing a sodium secondary battery containing a binder of 0.1 to 20% by weight. 제3항에 있어서,The method of claim 3, 상기 슬러리는 양극 활물질 100 중량부를 기준으로, 0.1 내지 20 중량부의 도전입자, 0.1 내지 10 중량부의 점도 조절제 및 0.1 내지 20 중량부의 바인더를 함유하는 나트륨 이차전지의 제조방법.The slurry is a method of manufacturing a sodium secondary battery containing 0.1 to 20 parts by weight of conductive particles, 0.1 to 10 parts by weight of a viscosity modifier and 0.1 to 20 parts by weight of a binder based on 100 parts by weight of the positive electrode active material. 제1항에 있어서,The method of claim 1, 상기 b) 단계 후,After step b), c) 상기 양극 공간에 전해액을 투입하는 단계;를 더 포함하는 나트륨 이차전지의 제조방법.c) injecting an electrolyte into the cathode space. 음극 공간과 양극 공간을 구획하는 나트륨 이온 전도성 고체전해질;Sodium ion conductive solid electrolyte partitioning the cathode space and the anode space; 상기 음극 공간에 위치하는 나트륨 함유 음극; 및A sodium-containing negative electrode positioned in the negative electrode space; And 상기 양극 공간에 위치하는 집전체 및 집전체가 위치한 양극 공간을 채우는 입자상을 포함하며, 상기 입자상은 양극활물질을 함유하는 양극;An anode including a current collector positioned in the anode space and a cathode filled in a cathode space in which the collector is located, the particulate containing a cathode active material; 을 포함하는 나트륨 이차전지.Sodium secondary battery comprising a. 제 17항에 있어서,The method of claim 17, 상기 양극 공간을 채우는 입자상은 용액상으로 양극 공간에 투입된 바인더의 건조에 의해 결착된 나트륨 이차전지.Particles filling the positive electrode space is a sodium secondary battery that is bound by the drying of a binder injected into the positive electrode space in the form of a solution. 제 17항에 있어서,The method of claim 17, 상기 입자상은 도전 입자를 더 포함하는 나트륨 이차전지.The particulate form is a sodium secondary battery further comprises conductive particles. 제 19항에 있어서,The method of claim 19, 상기 입자상은 상기 양극활물질 100 중량부를 기준으로 0.5 내지 20 중량부의 도전입자를 함유하는 나트륨 이차전지.The particulate form is a sodium secondary battery containing 0.5 to 20 parts by weight of conductive particles based on 100 parts by weight of the positive electrode active material. 제 17항에 있어서,The method of claim 17, 상기 양극활물질은 수산화니켈(Ni(OH)2)을 포함하는 나트륨 이차전지.The cathode active material includes sodium hydroxide (Ni (OH) 2 ). 제 17항에 있어서,The method of claim 17, 상기 음극은 용융 나트륨인 나트륨 이차전지.The cathode is a sodium secondary battery is molten sodium. 제 22항에 있어서,The method of claim 22, 상기 입자상은 상기 음극 공간에서의 상기 용융 나트륨의 수위에 상응하는 높이로 상기 양극 공간을 채우는 나트륨 이차전지.And the particulate phase fills the positive electrode space to a height corresponding to the level of the molten sodium in the negative electrode space. 제 17항에 있어서,The method of claim 17, 상기 나트륨 이차전지는 원통형의 금속 하우징, 상기 금속 하우징 내부에 위치하며, 금속 하우징의 외측에서 내측으로 순차적으로 동심 구조를 가지며 위치하는 나트륨 이온 전도성 고체전해질 튜브, 안전튜브 및 용융 나트륨이 담지되는 위킹튜브를 포함하며, 상기 양극 공간은 상기 고체전해질 튜브와 금속 하우징 사이의 공간인 나트륨 이차전지.The sodium secondary battery has a cylindrical metal housing, a sodium ion conductive solid electrolyte tube, a safety tube, and a wicking tube in which molten sodium is located, which is located inside the metal housing and has a concentric structure sequentially from the outside to the inside of the metal housing. And a positive electrode space is a space between the solid electrolyte tube and the metal housing. 제 17항에 있어서,The method of claim 17, 상기 입자상으로 충진된 상기 양극 공간의 빈 공간은 전해액으로 채워진 나트륨 이차전지. The empty space of the cathode space filled with the particulate is filled with an electrolyte solution.
PCT/KR2013/001338 2012-02-24 2013-02-20 Sodium secondary battery and method for manufacturing sodium secondary battery Ceased WO2013125853A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020147023654A KR102047761B1 (en) 2012-02-24 2013-02-20 Sodium secondary battery and method for manufacturing sodium secondary battery

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR10-2012-0018924 2012-02-24
KR1020120018924A KR20130097338A (en) 2012-02-24 2012-02-24 Fabrication method of na based secondary battery

Publications (1)

Publication Number Publication Date
WO2013125853A1 true WO2013125853A1 (en) 2013-08-29

Family

ID=49005972

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR2013/001338 Ceased WO2013125853A1 (en) 2012-02-24 2013-02-20 Sodium secondary battery and method for manufacturing sodium secondary battery

Country Status (2)

Country Link
KR (2) KR20130097338A (en)
WO (1) WO2013125853A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109952669A (en) * 2017-04-06 2019-06-28 株式会社Lg化学 Manufacturing method of lithium secondary battery

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102193367B1 (en) * 2014-02-13 2020-12-21 에스케이이노베이션 주식회사 Sodium Secondary Battery having Graphite Felt
KR101914173B1 (en) * 2016-04-26 2018-11-01 주식회사 엘지화학 Sodium electrode and sodium secondary battery comprising the same

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000251930A (en) * 1999-03-02 2000-09-14 Hitachi Ltd Sodium sulfur battery and module using the same
US6245455B1 (en) * 1997-07-04 2001-06-12 Hitachi, Ltd. Sodium-sulfur secondary battery
JP2002367670A (en) * 2001-06-07 2002-12-20 Hitachi Ltd Sodium sulfur battery
JP2003178798A (en) * 2001-12-10 2003-06-27 Hitachi Ltd Sodium sulfur battery
JP2004253289A (en) * 2003-02-21 2004-09-09 Hitachi Ltd Sodium sulfur battery and method of operating the same

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1269906B (en) * 1993-04-02 1997-04-16 Programme 3 Patent Holding Electrochemical cell
KR960002923A (en) * 1994-06-08 1996-01-26 조규향 Core tube for sodium-sulfur battery or sodium-nickel chloride battery and its manufacturing method
JPH11329484A (en) * 1998-05-07 1999-11-30 Hitachi Ltd Sodium-sulfur secondary battery

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6245455B1 (en) * 1997-07-04 2001-06-12 Hitachi, Ltd. Sodium-sulfur secondary battery
JP2000251930A (en) * 1999-03-02 2000-09-14 Hitachi Ltd Sodium sulfur battery and module using the same
JP2002367670A (en) * 2001-06-07 2002-12-20 Hitachi Ltd Sodium sulfur battery
JP2003178798A (en) * 2001-12-10 2003-06-27 Hitachi Ltd Sodium sulfur battery
JP2004253289A (en) * 2003-02-21 2004-09-09 Hitachi Ltd Sodium sulfur battery and method of operating the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109952669A (en) * 2017-04-06 2019-06-28 株式会社Lg化学 Manufacturing method of lithium secondary battery

Also Published As

Publication number Publication date
KR102047761B1 (en) 2019-11-22
KR20130097338A (en) 2013-09-03
KR20140135712A (en) 2014-11-26

Similar Documents

Publication Publication Date Title
CN103280604B (en) Liquid energy storage battery monomer structure with floating body electrolytes
WO2016175560A1 (en) Electrode for electrochemical device and method for manufacturing electrode
CN116615579A (en) Vertically integrated pure lithium metal production and lithium battery production
WO2012161473A2 (en) Lithium powder, lithium vanadium oxide, lithium secondary battery using a gel-polymer electrolyte, and method for preparing an electrode thereof
WO2019093709A1 (en) Electrolyte composite for lithium-sulfur battery, electrochemical device comprising same, and preparation method therefor
CN106784623B (en) Multitube type lithium sulfur battery
US6709789B1 (en) Non-aqueous electrochemical cell
WO2013125853A1 (en) Sodium secondary battery and method for manufacturing sodium secondary battery
CN102780049B (en) Large-capacity sodium-nickel chloride single flat battery and battery pack thereof
WO2013122409A1 (en) Sodium secondary battery
WO2015065116A1 (en) Organic-inorganic complex porous membrane, separator comprising same, and electrode structure body
WO2020122459A1 (en) Anode active material for lithium secondary battery and secondary battery comprising same
CN106165185B (en) Electrode unit for electrochemical device
CN112133957A (en) A kind of ultra-thin metal shell lithium ion battery and preparation method thereof
US20200153038A1 (en) Rechargeable lithium-ion battery
US5728331A (en) Method of preparing a battery separator
WO2018186597A1 (en) Method for manufacturing lithium secondary battery
CN113823851A (en) Lithium ion battery and lithium-supplementing negative plate thereof
NL2030456B1 (en) Cathode Material Coated In situ by Copper Foam/lithium Metal Battery
WO2012086995A2 (en) Sodium-sulfur battery and method for manufacturing same
CN117199566A (en) A method for electrochemical lithium replenishment of lithium-ion batteries
KR20180127008A (en) All-solid secondary battery including sulfur composite electrode with reduced carbon content
NL2034046B1 (en) A ceramic separator for energy storage devices
KR20190038776A (en) All-solid secondary battery including sulfur composite electrode with reduced carbon content
KR102893314B1 (en) High-energy-density lithium metal-based anodes for solid-state lithium-ion batteries

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 13752211

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 20147023654

Country of ref document: KR

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 13752211

Country of ref document: EP

Kind code of ref document: A1