KR20140120269A - Electrode assembly and secondary battery using the same - Google Patents

Abstract

The present invention relates to an electrode assembly for a secondary battery and a secondary battery using the same, capable of improving electricity conductivity, ion conductivity, and a capacity of a battery by forming a porous conductive metal layer on a particle surface of a cathode active substance layer and/or an anode active substance layer by a deposition method so that a metal network by the porous conductive metal layer can be formed other than an electronic conduction network by a conductive agent mixed with an active substance in an electrode. The electrode assembly for a secondary battery according to the present invention comprises a cathode including a cathode collector and a cathode active substance layer formed on at least one surface of the cathode collector; an anode including a anode collector and an anode active substance layer formed on at least one surface of the anode collector; a porous separation membrane formed between the cathode and the anode; and a porous conductive metal layer which is formed on the surface of at least either the cathode active substance layer or the anode active substance layer and has multiple pores to allow lithium ion to be moved.

Description

BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to an electrode assembly for a secondary battery,

The present invention relates to an electrode assembly for a secondary battery capable of improving the electrical conductivity and ion conductivity by forming a porous conductive metal layer on the particle surface of the active material layer, and a secondary battery using the same.

The lithium secondary battery generates electric energy by oxidation and reduction reactions when lithium ions are intercalated / deintercalated at the positive electrode and the negative electrode. The lithium secondary battery is manufactured by using a material capable of reversibly intercalating / deintercalating lithium ions as an active material for the positive electrode and the negative electrode and filling an organic electrolyte solution or a polymer electrolyte between the positive electrode and the negative electrode.

The lithium secondary battery comprises an electrode assembly in which a negative electrode plate and a positive electrode plate are wound or laminated in a predetermined form with a separator (separator) therebetween, and a case accommodating the electrode assembly and the electrolyte.

The basic function of the separator of the lithium secondary battery is to prevent short circuit by separating the positive electrode and the negative electrode, and further, it is important to maintain high ionic conductivity by sucking the electrolyte necessary for the battery reaction. In particular, in the case of a lithium secondary battery, an additional function is required to prevent movement of a substance inhibiting the cell reaction or ensure safety when an abnormality occurs.

A secondary battery including a lithium ion secondary battery and a lithium ion polymer battery having a high energy density and a large capacity must have a relatively high operating temperature range and the temperature is raised when the battery is continuously used in a high rate charge / discharge state, The separator is required to have higher heat resistance and thermal stability than those required for ordinary separators. In addition, it should have excellent cell characteristics such as rapid charge / discharge and high ion conductivity capable of coping with low temperature.

The separator is located between the positive and negative electrodes of the battery and maintains the electrolyte solution to provide the passage of ion conduction. When the temperature of the battery becomes excessively high, a part of the separator melts to block the current, I have.

When the temperature rises further and the separator melts, a large hole is formed and a short circuit occurs between the anode and the cathode. This temperature is called SHORT CIRCUIT TEMPERATURE. In general, the separator should have a lower SHUTDOWN temperature and a higher short-circuit temperature.

In the case of a polyethylene separator, there is a possibility that a short circuit may be caused when the abnormal heat of the battery shrinks at 150 ° C or more to expose the electrode portion. Therefore, it is very important to have both a closing function and a heat resistance for a high energy density, large-sized secondary battery. That is, a separator having excellent heat resistance and small heat shrinkage and excellent cycle performance in accordance with high ion conductivity is required.

As the material for the separator, a polyolefin-based microporous polymer membrane such as polypropylene or polyethylene or a multi-layer thereof is usually used. Conventional separators have the drawback that the porous separator also shrinks due to pore clogging of the porous membrane due to internal short-circuit or heat generation due to overcharging, because the porous membrane layer is in the form of sheet or film. Therefore, when the sheet-like separator shrinks due to internal heat generation of the battery and shrinks, the separator shrinks and the missing portion directly contacts the anode and cathode, resulting in ignition, rupture and explosion.

Currently, LiCoO ₂ is used as a cathode active material in almost all commercialized lithium secondary batteries. LiCoO ₂ is a material with excellent charge / discharge characteristics, high electron conductivity, excellent rate characteristics and excellent thermal stability. However, in recent years, there is a need for a cathode active material for a lithium secondary battery having a high voltage and a large capacity. In the case of LiCoO ₂ , if the charge / discharge of 4.3 V or more is continuously performed, the cathode active material is liable to react with the electrolyte due to lattice strain or destruction of crystal structure The lifetime characteristics and the safety are deteriorated. In addition, Co, which is the starting material of cathode active material, is in a trend of increasing in price continuously because of its shortage of reserves. Further toxic and environmental pollution problems are needed to develop alternative cathode active materials.

LiNiO ₂ , LiMn ₂ O ₄ , LiFePO ₄ , and Li (NixCoyMnz) O ₂ are examples of a cathode active material for a lithium secondary battery, which has been actively researched and developed at present. LiNiO ₂ , however, is not only difficult to synthesize, but also has a problem with thermal stability and is difficult to commercialize. LiMn ₂ O ₄ is partly commercialized at a low price, but due to Jnn-Teller distortion due to Mn 3+, The characteristics are not good. In addition, LiFePO ₄ is excellent in low cost and safety, and is currently being studied for HEV. However, it is difficult to apply LiFePO ₄ to other fields due to its low conductivity.

Therefore, Li (NixCoyMnz) O ₂ is the most popular material as an alternative cathode active material of LiCoO ₂ . This material is less expensive than LiCoO ₂ and has the advantage of being used at high capacity and high voltage, but it has a disadvantage of poor rate characteristics and lifetime at high temperature. In order to overcome such disadvantages, a method of coating a surface of a cathode active material with a conductive metal or a method of doping a material such as Al, Mg, Ti, Zr, Sn, Ca, And the coating method has a problem of increasing the price in mass production using a wet method. However, there is an increasing trend of increasing the characteristics of the metal by dry doping at present. to be.

In recent years, attempts have been made to improve the electrochemical characteristics of lithium secondary batteries through Ti doping. However, in order to dope the cathode active material using TiO ₂ , Temperature and a large amount of firing time are required.

Accordingly, in order to prevent deterioration of the battery performance as described above, lithium secondary batteries that can uniformly distribute the additive elements to the cathode active material and improve the structural stability and electrochemical characteristics by maximizing the doping effect Studies on cathode active materials for secondary batteries are needed.

Korean Patent Laid-Open No. 10-2010-56106 proposes a positive electrode active material for a lithium secondary battery that maximizes the doping effect of an additive element and has excellent structural stability and electrochemical characteristics.

However, since the conventional anode or cathode electrode is composed of an active material, a conductive agent, and a binder, in the case of a large-capacity battery, an electronic conduction network is formed by a conductive material by an active material layer, and in particular, a gel polymer electrolyte battery has a low ion conductivity The electronic conductivity network alone has a limitation on the ion conductivity.

Korean Patent Publication No. 10-2010-56106

An object of the present invention is to provide a porous conductive metal layer on the surface of an electrode active material layer to improve the ionic conductivity by forming a metal network using a porous conductive metal layer in addition to an electronic conduction network formed by a conductive agent mixed with an active material inside the electrode, And an electrode assembly for a secondary battery capable of improving the performance of the battery, and a secondary battery using the same.

Another object of the present invention is to provide an electrode assembly for a secondary battery which can improve the electrical conductivity of the electrode surface by adding a metal network in addition to the electronic conduction network and thereby increase the moving speed of the lithium ion, And a secondary battery using the same.

It is to be understood that both the foregoing general description and the following detailed description of the present invention are exemplary and explanatory and are intended to provide further explanation of the invention as claimed. .

In order to achieve the above object, the present invention provides an electrode assembly for a secondary battery, comprising: a negative electrode including a negative electrode current collector and a negative electrode active material layer formed on at least one side of the negative electrode current collector; A positive electrode comprising a positive electrode collector and a positive electrode active material layer formed on at least one surface of the positive electrode collector; A porous separator formed between the cathode and the anode; And a porous conductive metal layer formed on a surface of at least one of the anode active material layer and the cathode active material layer and having a plurality of pores to allow movement of lithium ions.

The negative electrode and the positive electrode each have an electronic conduction network made of a conductive material mixed with an active material inside the electrode and a metal network made of the porous conductive metal layer. As a result, the electrical conductivity, the ion conductivity, and the capacity of the battery can be improved.

The conductive metal layer is preferably formed in the form of a plurality of point particles on the surface of the anode active material layer or the cathode active material layer so as to form a metal network, and pores are formed between the particles and the particles to move lithium ions.

The conductive metal layer formed on the cathode active material layer of the present invention may be formed of Al or Ni, and the conductive metal layer formed on the anode active material layer may be formed of Cu or Ni.

The conductive metal layer is preferably formed to a thickness of 30 to 400 Å, and is preferably formed by a vacuum deposition method. The conductive metal layer formed on the anode active material layer may be set to a range of 30 to 300 angstroms and the conductive metal layer formed on the cathode active material layer may be set to a range of 110 to 400 angstroms.

The electrode assembly according to the present invention is assembled in a case and filled with an electrolyte to constitute a secondary battery.

Wherein the electrolyte solution comprises an organic electrolyte solution containing a non-aqueous organic solvent, a solute of a lithium salt, a monomer for forming a gel polymer, and a polymerization initiator, and the electrolyte is impregnated with the porous separation membrane, To form a gel polymer electrolyte, and the porous separator serves as an electrolyte matrix in the gel polymer electrolyte.

In addition, the electrolyte solution may be an organic electrolyte solution including a non-aqueous organic solvent and a solute of a lithium salt.

The electrode assembly according to the present invention can be applied to a secondary battery such as a lithium ion battery or a lithium polymer battery.

As described above, in the electrode assembly for a secondary battery of the present invention, the porous conductive metal layer is formed on the surface of the particles of the negative electrode active material layer and / or the positive electrode active material layer by a deposition method, In addition to the network, a metal network made of a porous conductive metal layer can be formed to improve electrical conductivity, ion conductivity, and capacity of the battery.

1 is a cross-sectional view illustrating an electrode assembly for a secondary battery according to a first embodiment of the present invention.
2 is a cross-sectional view illustrating an electrode assembly for a secondary battery according to a second embodiment of the present invention.
3 is an enlarged view conceptually showing a state in which an electroconductive metal layer is deposited on the surface of the active material layer of the present invention.
4A is a SEM photograph of a 2000-fold magnification photograph of the negative electrode sample of Comparative Example 1. Fig.
4B to 4E are SEM photographs of the negative electrode samples of Examples 2 to 5 at 2000 times magnification.
FIG. 5A is an SEM photograph of the positive electrode sample of Comparative Example 2 taken at 2000 times magnification. FIG.
Figs. 5B to 5C are SEM photographs of the positive electrode samples of Examples 8 to 10 at 2000 times magnification. Fig.

Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings. The sizes and shapes of the components shown in the drawings may be exaggerated for clarity and convenience. In addition, terms defined in consideration of the configuration and operation of the present invention may be changed according to the intention or custom of the user, the operator. Definitions of these terms should be based on the content of this specification.

FIG. 1 is a cross-sectional view showing an electrode assembly according to a first embodiment of the present invention, and FIG. 2 is a sectional view of an electrode assembly according to a second embodiment of the present invention.

1 and 2, an electrode assembly 10 for a secondary battery according to the present invention mainly includes a negative electrode 1 and a positive electrode 2.

The negative electrode 1 is disposed opposite to the positive electrode 2 and includes a pair of negative electrode active material layers 13a and 13b formed on both surfaces of the negative electrode collector 11 to form a bi-cell. The negative electrode 1 may have a structure in which a negative electrode active material layer is provided on one surface of the negative electrode collector 11 when a pull cell is formed.

The positive electrode 2 includes positive electrode active material layers 23a and 23b formed on both surfaces of the positive electrode collector 21 to form a bi-cell. The positive electrode 2 may have a structure in which a positive electrode active material layer is formed on one surface of the positive electrode collector 21 when a pull cell is formed.

The positive electrode active material layer (23a, 23b) is and reversibly including a positive electrode active material capable of migration intercalation and de-intercalation of lithium ions, and a typical example of such a positive electrode active material is LiCoO _2, LiNiO _2, LiNiCoO _2, LiFeO _4, LiMnO ₂ , LiMn ₂ O ₄ , V ₂ O ₅ , V ₆ O ₁₃ , LiNiCoAlO ₂ , LiNi _1-xy Co _x M _y O ₂ (0 ≤ x ≤ 1, 0 ≤y ≤ 1, 0 ≤ x + y ≤ 1, M is a metal such as Al, Sr, Mg, or La) or a lithium-transition metal such as Li [Ni _x Co _1-xy Mn _y ] O ₂ (where 0 <x <0.5, 0 <y <0.5) Oxides can be used.

The cathode active material may be classified into five types such as lithium cobalt (LCO), lithium nickel cobalt manganese (NCM), lithium nickel cobalt aluminum (NCA), lithium manganese (LMO) and lithium iron phosphate Respectively. In this case, it is also possible to use five kinds of active materials alone as the cathode active material, or a hybrid type in which, for example, a layered NCM or NCA and a spinel LMO are mixed.

However, in the present invention, it is of course possible to use other kinds of cathode active materials in addition to the cathode active material.

The negative electrode active material layers 13 and 13a include a negative electrode active material capable of intercalating and deintercalating lithium ions. Examples of the negative electrode active material include a carbonaceous negative electrode of crystalline or amorphous carbon, carbon fiber, Active material, tin oxide, lithiated lithium, lithium, lithium alloy, and mixtures thereof.

The negative electrode 1 and the positive electrode 2 are prepared by mixing an appropriate amount of an active material, a conductive agent, a binder and an organic solvent to prepare a slurry, and then the negative electrode and the positive electrode current collector 11, Cast slurry, dried and rolled.

Examples of the conductive agent include graphite, carbon black, acetylene black, ketjen black, channel black, furnace black, lamp black, summer black, carbon fiber, metal fiber, carbon fluoride, aluminum, nickel powder, zinc oxide, potassium titanate , Titanium oxide, and polyphenylene derivatives can be used.

For example, a positive electrode is formed by casting a slurry composed of LiCoO ₂ , Super-P carbon, and PVdF as an active material, a conductive agent, and a binder on an aluminum foil, and using a negative electrode such as MCMB (mesocarbon microbeads), Super- The constructed slurry can be cast on an aluminum foil. It is preferable to roll-press the anode and the cathode in order to increase the adhesive force between the particles and the metal foil after each slurry is cast.

The porous separation membranes 3a and 3b formed on the surface of the negative electrode 1 in a multilayer structure are formed by covering the negative electrode active material layers 13a and 13b with a first material comprising a polymer capable of conducting electrolytic solution, And inorganic porous polymer web layers 33a and 33b made of ultrafine fibers of a mixture of inorganic polymer film layers 31a and 31b and a heat resistant polymer or a mixture of heat resistant polymer and swelling polymer and inorganic particles.

The separators 3a and 3b may be separately formed without being formed directly on the cathode 1, and then may be inserted between the cathode and the anode to be sealed when assembling the cathode and the anode.

A metal network is formed on the particle surface of the anode active material layer 13a and the cathode active material layer 23a in addition to the electron conduction network made of carbon black or other conductive agent contained in the anode active material layer and the cathode active material layer, Porous conductive metal layers 50, 60 are formed which can improve performance.

The porous conductive metal layers 50 and 60 include a porous first conductive metal layer 50 formed on the surface of the anode active material layer 13a and a porous second conductive metal layer 60 formed on the surface of the cathode active material layer 23a. .

The thicknesses of the first and second conductive metal layers 50 and 60 are preferably set to 30 to 400 angstroms, respectively. More preferably, the first conductive metal layer 50 is set to a range of 30 to 300 angstroms, and the second conductive metal layer 60 is set to a range of 110 to 400 angstroms.

When the thickness of each of the first and second conductive metal layers 50 and 60 is less than 30 ANGSTROM, the resistance increases and the improvement of the electrical conductivity is insignificant. When the thickness of the first and second conductive metal layers 50 and 60 exceeds 400 ANGSTROM, It adversely affects battery characteristics.

The resistance of the first conductive metal layer 50 formed on the surface of the anode active material layer 13a increases as the thickness increases or decreases and the second conductive metal layer 60 formed on the surface of the cathode active material layer 23a increases, As the thickness increases or decreases, the resistance value and electrical conductivity tend to increase.

Here, the first conductive metal layer 50 may be formed of Cu or Ni, and the second conductive metal layer 60 may be formed of Al or Ni.

A plurality of pores 70 are formed in the porous conductive metal layers 50 and 60 so that lithium ions can pass therethrough. That is, when the conductive metal layers 50 and 60 completely cover the particle surfaces of the active material layers 13a and 23a, the movement of lithium ions is suppressed and the performance is lowered. Therefore, the pores 70 capable of sufficiently moving lithium ions are secured .

3, the conductive metal layers 50 and 60 are formed by a deposition method such as thermal evaporation or electron-beam evaporation, and the conductive metal layer 50 60 are deposited so that the conductive metal layers 50 and 60 are partially interconnected to each other in the form of point particles 80 by appropriately adjusting the deposition conditions so that the particles 80 and 80 ), While securing the pores 70 partially so that the lithium ions can sufficiently pass through the pores.

The deposition method for forming the conductive metal layer may be a sputtering method, a chemical vapor deposition (CVD) method, or a physical vapor deposition (PVD) method in addition to the thermal evaporation described above.

As described above, in this embodiment, by forming the three-dimensional metal network having the pores 70, which are the passages through which the lithium ions pass through the conductive metal layers 50 and 60 by the deposition method, on the surface of the particles of the anode active material layer and the cathode active material layer , The electric conductivity and the ion conductivity can be improved, and thus the performance of the electrode can be improved.

Particularly, in the case of the gel polymer electrolyte battery, the ion conductivity drops. In the anode active material layer and the cathode active material layer of the present embodiment, the conductive metal layer is formed in the form of point particles, The pores 70 can be partially secured while forming the network to improve the electrical conductivity and the ion conductivity, thereby improving the performance of the battery.

When a gel polymer electrolyte is used to construct a flexible battery, the porous conductive metal layer is formed on the surface of the anode active material layer and the cathode active material layer of the present embodiment to improve electrical conductivity and ion conductivity, have.

 It is also possible to use a porous polymer web obtained by electrospinning a swelling polymer in place of the first inorganic polymer film layers 31a and 31b as the separation membranes 3a and 3b. For example, the porous polymer web may be prepared by dissolving a swelling polymer in a solvent to form a spinning solution, then spinning the spinning solution onto the negative electrode active material layer to form a porous polymer web made of microfine fibers, , PVDF), the porous polymer web is calendered at a temperature lower than the melting point of the porous polymer web.

The first inorganic polymer film layers 31a and 31b formed so as to cover the negative electrode active material layers 13a and 13b in the negative electrode 1 are made of a polymer capable of conducting electrolytic solution and swelling electrolyte, (Polyvinylidene fluoride), poly-ethylen oxide (PEO), polymethylmethacrylate (PMMA), and thermoplastic polyurethane (TPU). In addition, the first inorganic filler polymer film layers 31a and 31b are formed by dissolving the polymer in a solvent to form a spinning solution, and then spinning solution is electrospun onto the negative active material layer to form a porous polymer web of ultrafine fibrous phase , The polymeric film layers 31a and 31b of the inorganic porous material are obtained by heat-treating or calendering the porous polymeric web at a temperature lower than the melting point of the polymer.

The reason why the heat treatment temperature can be performed at a temperature slightly lower than the melting point of the polymer is that the solvent remains in the polymer web and the inorganic web film is formed while the polymer web is completely melted by the heat treatment to be.

The inorganic polymer film layers 31a and 31b made of a material capable of swelling the electrolyte solution and capable of conducting electrolyte ions are electrospun directly on the surfaces of the negative electrode active material layers 13a and 13b to form the negative electrode active material layers 13a and 13b, 13b, swelling is caused by the electrolytic solution, thereby preventing the formation of spaces between the negative electrode active material layers 13a, 13b and the film while maintaining the conduction of lithium ions, thereby preventing lithium ions from accumulating and precipitating into lithium metal can do. As a result, formation of dendrites on the surface of the negative electrode 1 can be suppressed, and safety can be improved.

The inorganic-substance-containing porous polymer web layers 33a and 33b formed on the first inorganic polymer film layers 31a and 31b are formed by dissolving a mixture of the heat-resistant polymer or heat-resistant polymer and the swelling polymer and inorganic particles in a solvent to form a spinning solution Then, the spinning solution is electrospun onto the first inorganic filler polymer film layers 31a and 31b to form a porous polymer web composed of ultrafine fibers, and the obtained porous polymer web is calendered at a temperature below the melting point of the polymer.

The inorganic particles may be selected from the group consisting of Al ₂ O ₃ , TiO ₂ , BaTiO ₃ , Li ₂ O, LiF, LiOH, Li ₃ N, BaO, Na ₂ O, Li ₂ CO ₃ , CaCO ₃ , LiAlO ₂ , SiO ₂ , SnO ₂ , PbO ₂ , ZnO, P ₂ O ₅ , CuO, MoO, V ₂ O ₅ , B ₂ O ₃ , Si ₃ N ₄ , CeO ₂ , Mn ₃ O ₄ , Sn ₂ P ₂ O ₇ , Sn ₂ B ₂ O ₅ , Sn ₂ BPO _6, and mixtures thereof.

When the mixture is composed of a heat-resistant polymer or a heat-resistant polymer, a swellable polymer and inorganic particles, the content of the inorganic particles is preferably in the range of 10 to 25% by weight based on the total amount of the inorganic particles when the size of the inorganic particles is between 10 and 100 nm. More preferably, the inorganic particles are contained in the range of 10 to 20 wt%, and the size is in the range of 15 to 25 nm.

When the mixture is composed of a heat-resistant polymer, a swellable polymer and an inorganic particle, the heat-resistant polymer and the swellable polymer are preferably mixed in a weight ratio ranging from 5: 5 to 7: 3, more preferably 6: 4. In this case, the swelling polymer is added as a binder to facilitate bonding between the fibers.

If the mixing ratio of the heat-resistant polymer and the swelling polymer is less than 5: 5 by weight, the heat resistance is lowered and the high temperature property is not obtained. If the mixing ratio is more than 7: 3 by weight, the strength is lowered and radiation trouble occurs.

The heat-resistant polymer resin which can be used in the present invention is a resin which can be dissolved in an organic solvent for electrospinning and has a melting point of 180 ° C or higher, for example, polyacrylonitrile (PAN), polyamide, polyimide, polyamideimide, Aromatic polyesters such as poly (meta-phenylene isophthalamide), polysulfone, polyether ketone, polyethylene terephthalate, polytrimethylene terephthalate, and polyethylene naphthalate, polytetrafluoroethylene, , Polyphosphazenes such as poly {bis [2- (2-methoxyethoxy) phosphazene], polyurethane copolymers including polyurethane and polyether urethane, cellulose acetate, cellulose acetate butyrate, cellulose acetate prop Phonate and the like can be used.

The swellable polymer resin usable in the present invention is a resin which swells in an electrolytic solution and can be formed by ultrafine fibers by an electrospinning method. Examples of the swellable polymer resin include polyvinylidene fluoride (PVDF), polyvinylidene fluoride-co- Polypropylene), perfluoropolymers, polyvinyl chloride or polyvinylidene chloride, and copolymers thereof, and polyethylene glycol derivatives including polyethylene glycol dialkyl ethers and polyethylene glycol dialkyl esters, poly (oxymethylene-oligo- Polyvinyl acetate, poly (vinylpyrrolidone-vinyl acetate), polystyrene and polystyrene acrylonitrile copolymers, polyacrylonitrile methyl methacrylate copolymers, polyacrylonitrile methyl methacrylate copolymers, &Lt; / RTI &gt; Casting reel can be given to the copolymer, polymethyl methacrylate, polymethyl methacrylate copolymers and mixtures thereof.

In the first embodiment shown in FIG. 1, the separators 3a and 3b having a multilayer structure are formed on the surface of the cathode 1. However, the separators 3a and 3b may be formed on the surface of the anode 2 instead of the cathode 1. In this case, it is preferable that inorganic porous polymer web layers 33 (33a and 33b) are formed first on the surface of the anode 2 and the first inorganic polymer film layers 31 (31a and 31b) are formed on the porous polymer web layer 33 : 33a and 33b are easily adhered to each other when they are assembled with the negative electrode 1.

In the first embodiment, the two-layered structure separation membranes 3a and 3b are formed on either the cathode 1 or the anode 2. However, as in the second embodiment shown in FIG. 2, The inorganic polymer film layers 31 and 31a and 31b and inorganic porous polymer web layers 33 and 33a and 33b may be formed separately from the negative electrode 1 and the positive electrode 2.

For example, the first inorganic polymer film layer 31 (31a, 31b) is formed on the cathode 1 so as to cover the anode active material layers 13a, 13b, and the inorganic active material layers 23a, Containing porous polymeric web layer 33 (33a, 33b) may be formed on the anode 2.

It is also possible to form the second inorganic polymeric film layer on the surfaces of the inorganic-substance-containing porous polymer web layers 33a and 33b of the anode 2 in the same manner as the first inorganic polymeric film layers 31a and 31b. In this case, when the cathode (1) and the anode (2) are assembled, the first inorganic filler polymer film layers (31a, 31b) and the second inorganic filler polymer film layer are bonded to each other.

When the first inorganic filler polymer film layers 31a and 31b and the inorganic porous polymer web layers 33a and 33b are integrally formed on the cathode 2 or separately formed on the cathode 1 and the anode 2 , The thickness of the inorganic porous polymer web layers 33a and 33b is set in the range of 5 to 50 μm and the thickness of the first inorganic polymer film layers 31a and 31b is set in the range of 5 to 14 μm.

In this case, the function of the separation membrane is not limited to the inorganic-containing porous polymer web layers 33a and 33b because the inorganic-substance-containing porous polymer web layers 33a and 33b have higher porosity than the first inorganic polymer film layers 31a and 31b. And more sensitive to the thickness of the polymer film layers 31a and 31b. As described later, if the thickness of the first inorganic filler polymer film layer 31a or 31b is less than 5 μm, micro-short-circuiting occurs. If the thickness of the first inorganic filler polymer film layer 31a or 31b is more than 14 μm, the Li- The thickness of the first inorganic polymer film layers 31a and 31b is preferably adjusted in consideration of ion conductivity and energy density of the film layer.

As described above, in the present invention, the first inorganic filler polymer film layers 31a and 31b and the inorganic porous polymer web layers 33a and 33b serving as separation membranes are bonded to the negative electrode 1 or the positive electrode 2 And the cathode 1 and the anode 2 are surrounded by a sealing structure at the same time as shown in Fig.

Therefore, as shown in FIGS. 1 and 2, the electrode assembly 10 or 10a of the present invention can form unit cells by simply stacking the negative electrode 1 and the positive electrode 2, and for example, When the battery is manufactured in a large size for constituting the battery, a plurality of unit cells are simply stacked, and the case assembly is performed. Therefore, the present invention has high assembly productivity as compared with the prior art which involves a process of folding a plurality of bicells with separate separation film.

The negative electrode (1) and the positive electrode (2) are provided with a negative electrode and a positive electrode terminal in which a part of the negative electrode and the positive electrode current collector (11, 21) are protruded. The electrode assembly 10 or 10a of the present invention has a structure in which the negative electrode terminal 11a of the negative electrode 1 and the positive electrode terminal 21a of the positive electrode 2 Are laminated so as to face each other in the opposite direction.

The conventional film type separator shrinks at a high temperature. However, since the porous polymer web layers 33a and 33b contain an inorganic substance, the porous polymer web layers 33a and 33b retain their shape without being shrunk or melted at the time of heat treatment at 500 ° C.

In the conventional polyolefin film separator, since the peripheral film is continuously shrunk or melted due to the initial heat generated at the time of internal short-circuit, the part where the film separator is burned out becomes wider, so that a hard short-circuit is further generated However, the electrode of the present invention does not lead to a phenomenon in which a short-circuited portion is widened due to a small damage in a portion where an internal short-circuit occurs.

In addition, the electrode of the present invention maintains a constant voltage between 5V and 6V and a battery temperature below 100 DEG C by continuously consuming an overcharge current due to a very short, soft short-circuit, not a short circuit, Overcharge stability can also be improved.

The electrode assembly according to the present invention can constitute a lithium ion battery or a lithium polymer battery as a secondary battery.

When the electrode assembly according to the present invention constitutes a lithium ion battery (LIB), separation membranes (3a, 3b; 3) are formed on the cathode (1) and the anode (2) An electrode assembly (10, 10a) contains an electrolytic solution.

The electrolyte solution includes an organic electrolyte solution including a non-aqueous organic solvent and a solute of a lithium salt, and the lithium salt acts as a source of lithium ions in the cell to enable operation of a basic lithium battery.

When the electrode assembly according to the present invention comprises a lithium polymer battery (LPB), the lithium polymer battery includes a negative electrode (1), a positive electrode (2), and a polymer electrolyte interposed between the negative electrode and the positive electrode, It consists of a porous separator and a gel polymer that act as an electrolyte matrix.

The lithium polymer battery is formed by integrally forming a porous separator on one of the negative electrode 1 and the positive electrode 2, preferably on the surface of the negative electrode 1, or by inserting it between the negative electrode 1 and the positive electrode 2, The electrode assembly includes an electrolytic solution.

The porous separation membrane serves as an electrolyte matrix, and a composite porous membrane having a single layer of a porous polymer web made of nanofibers, a porous polymer web, an inorganic polymer film, and a porous nonwoven fabric may be used. The electrolyte solution includes a non-aqueous organic solvent and a solute of a lithium salt, a monomer for forming a gel polymer, and a polymerization initiator.

When the electrolyte solution is filled in the case where the electrode assembly is assembled into the case, the electrolyte is impregnated into the porous separator. When the gelation heat treatment process is performed, a gel polymer is synthesized by the polymerization reaction of the gel polymer forming monomer, An electrolyte is formed. In this case, the porous separator serves to separate the negative electrode 1 and the positive electrode 2 from each other while acting as an electrolyte matrix in the gel polymer electrolyte.

Hereinafter, the present invention will be described in more detail with reference to examples. However, the following examples are only illustrative of the present invention, and the scope of the present invention is not limited thereto.

(Comparative Example 1)

The negative electrode was prepared by dissolving 9 g, 0.5 g and 0.5 g of graphite, a conductive material (CB) and a binder (PVdF) in NMP (N-methyl pyrrolidone) as a solvent and casting the obtained paste on a copper foil , Roll pressing was performed to increase the adhesive force between the particles and the metal foil to prepare the negative electrode of Comparative Example 1. [

A negative electrode sample of Comparative Example 1 was prepared in a size of 2Ah without metal deposition, and an SEM photograph of the negative electrode sample of Comparative Example 1 was taken at 2000 times magnification, which is shown in FIG. 4A.

(Examples 1 to 6)

A negative electrode of Comparative Example 1 was prepared in a size of 2Ah, a negative electrode sample of 2Ah size was mounted on a ceramic substrate jig of a thermal evaporator, and a jig was attached to a rotary holder of a thermal evaporator. The Cu metal was measured in proportion to the thickness to be deposited and set on a tungsten boat.

Then, the holder was rotated at a rotation speed of 2 m / s for 10 minutes under a low vacuum of 5 ^-2 torr and at a rotation speed of 2 m / s for 30 minutes in a high vacuum state of 5 ^-5 torr for 30 minutes, Copper (Cu) was deposited to a thickness of 30 angstroms, 105 angstroms, 120 angstroms, 135 angstroms, 150 angstroms and 300 angstroms on the negative electrode sample by depositing Cu metal on the negative electrode sample by setting the thermal evaporator to 3.5 V, 120 A, 1 to Example 6 were produced.

SEM photographs of the obtained samples of Examples 2 to 5 at 2000 magnifications are shown in Figs. 4B to 4E.

Resistance values and electrical conductivities of the samples of Examples 1 to 6 were measured according to the deposition thickness of copper and are shown in Table 1 together with the characteristics of Comparative Example 1.

In addition, the half cell test was carried out for Example 2 and Example 5 to determine the battery capacity at the time of discharge, and it is shown in Table 2 below.

Sample Thickness (Å) Resistance value
(m? cm) Electrical conductivity
(S / cm) Comparative Example 1 0 12.64 7.91 x 10 Example 1 30 8.001 1.04 × 10 ² Example 2 105 2.607 3.83 × 10 ² Example 3 120 2.648 3.77 x 10 ² Example 4 135 5.961 1.67 × 10 ² Example 5 150 6.460 1.54 x 10 ² Example 6 300 10.12 1.00 x 10 ²

Sample Thickness (Å) Volume
(mAh / g) Comparative Example 1 0 261.9 Example 2 105 330.4 Example 5 150 273.9

As shown in Table 1, the samples of Examples 1 to 6, in which copper was deposited on the surface of the negative electrode according to the present invention, exhibited resistance values and electrical conductivity characteristics as compared with Comparative Example 1 in which copper was not deposited And the better the thickness of the deposited copper was, the better the thin film was. However, when the thickness of the deposited copper was too thin as in Example 1 or thick as in Example 6, the resistance value increased and the electrical conductivity tended to decrease again.

As a result of the half cell test of the samples of Example 2 and Example 5, as shown in Table 2, the capacity of the battery and the deposition thickness of copper thin film were better. In particular, Example 2 in which the thickness of copper was 105 Å showed the highest resistance value, electrical conductivity and capacity.

(Comparative Example 2)

The anode was prepared by mixing 8 g, 1.5 g, and 0.5 g of a hybrid type active material, a conductive material (CB), and a binder (CMC, SBR) obtained by mixing a lithium nickel cobalt manganese (NCM) oxide and a lithium manganese Was dissolved in distilled water used as a solvent. The obtained paste was cast on an aluminum foil, and roll pressing was performed to increase the adhesive force between the particles and the metal foil to prepare the positive electrode of Comparative Example 2. [

The anode sample of Comparative Example 2 was prepared in 2Ah size without metal deposition, and the SEM photograph of the anode sample of Comparative Example 2 taken at 2000 times magnification is shown in FIG. 5A.

(Examples 7 to 11)

A positive electrode of Comparative Example 2 was prepared in a size of 2Ah, a positive electrode sample of 2Ah size was mounted on a ceramic substrate jig of a thermal evaporator, and a jig was attached to a rotary holder of a thermal evaporator. Al metal was measured in proportion to the thickness to be deposited and set on a tungsten boat.

Then, the holder was rotated at a rotation speed of 2 m / s for 10 minutes under a low vacuum of 5 ^-2 torr and at a rotation speed of 2 m / s for 30 minutes in a high vacuum state of 5 ^-5 torr for 30 minutes, Al was deposited to a thickness of 110 Å, 200 Å, 220 Å, 240 Å and 400 Å on the anode sample by depositing Al metal on the cathode sample with the thermal evaporators set at 2.8 V, 100 A, and 3 min, .

SEM photographs of the samples of Examples 8 to 10 obtained at 2000 times magnification are shown in Figs. 5B to 5D.

The samples of Examples 7 to 11 were measured for resistance and electrical conductivity according to the thickness of Al deposition and half cell test was carried out to determine the ionic conductivity and the voltage characteristic, 3.

Sample Thickness (Å) Resistance value
(m? cm) Electrical conductivity
(S / cm) Ion conductivity
(S / cm) Volume
(mAh / g) Comparative Example 2 0 0.264 3.87 × 10 ³ 2.8 × 10 ^-4 113.9 Example 7 110 0.191 1.09 × 10 ⁴ 5.7 x 10 ^-4 120.0 Example 8 200 0.048 2.08 × 10 ⁴ 6.9 × 10 ^-4 139.8 Example 9 220 0.094 1.87 x 10 ⁴ 6.5 × 10 ^-4 127.4 Example 10 240 0.181 1.24 × 10 ⁴ 6.4 × 10 ^-4 124.4 Example 11 400 0.210 1.01 × 10 ⁴ 5.4 × 10 ^-4 117.4

As shown in Table 3, the samples of Examples 7 to 11, in which aluminum was deposited on the surface of the anode according to the present invention, showed a resistance value, electrical conductivity, ion The conductivity and the capacity of the battery were excellent. In particular, the resistance value, the electric conductivity, the ionic conductivity and the capacity were all superior to those of Comparative Example 2 in the case of Example 8 in which the thickness of aluminum was 200 Å.

However, when the thickness of the deposited aluminum was too thin as in Example 7 or thick as in Example 11, the resistance value increased again and the electrical conductivity tended to decrease. The ion conductivity and the capacity of the battery were also increased The thickness of the film was too thin or too thick, the characteristics were poor.

As described above, in the electrode assembly for a secondary battery of the present invention, the porous conductive metal layer is formed on the surface of the particles of the negative electrode active material layer and / or the positive electrode active material layer by a deposition method, In addition to the network, a metal network made of a porous conductive metal layer can be formed to improve electrical conductivity, ion conductivity, and capacity of the battery.

Particularly, when a gel polymer electrolyte is used to constitute a flexible battery, a porous conductive metal layer having a plurality of pores having a three-dimensional structure is formed on the surface of the anode active material layer and the cathode active material layer of the present embodiment to provide electrical conductivity and ion conductivity The performance of the battery can be improved.

While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is clearly understood that the same is by way of illustration and example only and is not to be construed as limited to the embodiments set forth herein. Various changes and modifications may be made by those skilled in the art.

The present invention relates to an electrode active material layer formed by partially forming a conductive metal layer on a particle surface of an electrode active material layer and forming a metal network by a porous conductive metal layer in addition to an electronic conduction network formed by a conductive agent mixed with an active material inside the electrode, As a technique capable of improving the capacity, it can be applied to a secondary battery such as a lithium ion battery or a lithium polymer battery.

1: cathode 2: anode
10, 10a: electrode assembly 11: negative electrode collector
13a, 13b: Negative electrode active material layer 21: Positive electrode collector
23a, 23b: positive active material layer 3a, 3b:
31a, 31b: inorganic hollow polymeric film layers 33a, 33b: porous polymeric web layer
50, 60: Conductive metal layer 70: Porosity
80: particles

Claims (11)

A negative electrode having a negative electrode current collector and a negative electrode active material layer formed on at least one surface of the negative electrode current collector;
A positive electrode comprising a positive electrode collector and a positive electrode active material layer formed on at least one surface of the positive electrode collector;
A porous separator formed between the cathode and the anode; And
And a porous conductive metal layer formed on a surface of at least one of the anode active material layer and the cathode active material layer and having a plurality of pores to allow movement of lithium ions. The method according to claim 1,
Wherein the negative electrode and the positive electrode each include an electronic conduction network made of a conductive material mixed with an active material inside the electrode and a metal network formed by the porous conductive metal layer. The method according to claim 1,
Wherein the conductive metal layer is deposited on the surface of the anode active material layer or the cathode active material layer in the form of a plurality of point particles to form a metal network and pores are formed between the particles and the particles to move lithium ions Electrode assembly. The method according to claim 1,
Wherein the conductive metal layer formed on the cathode active material layer is formed of Al or Ni. The method according to claim 1,
Wherein the conductive metal layer formed on the anode active material layer is formed of Cu or Ni. The method according to claim 1,
Wherein the conductive metal layer is set to a thickness of 30 to 400 ANGSTROM. The method according to claim 6,
Wherein the conductive metal layer formed on the anode active material layer is set in a range of 30 to 300 ANGSTROM and the conductive metal layer formed on the cathode active material layer is set in a range of 110 to 400 ANGSTROM. The electrode assembly for a secondary battery according to claim 1, wherein the conductive metal layer is formed by a vacuum deposition method. case;
An electrode assembly according to any one of claims 1 to 8 assembled into the case; And
And an electrolyte filled in the case. 10. The method of claim 9,
Wherein the electrolyte solution comprises an organic electrolyte solution including a non-aqueous organic solvent, a solute of a lithium salt, a monomer for forming a gel polymer, and a polymerization initiator,
Wherein the electrolyte is impregnated with the porous separator, and polymerizes the gel polymer forming monomer to form a gel polymer electrolyte, and the porous separator serves as an electrolyte matrix in the gel polymer electrolyte. . 10. The method of claim 9,
Wherein the electrolytic solution is an organic electrolytic solution containing a non-aqueous organic solvent and a solute of a lithium salt.

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