KR101226620B1 - Manufacturing method of hybrid supercapacitor having a high specific capacitance - Google Patents
Manufacturing method of hybrid supercapacitor having a high specific capacitance Download PDFInfo
- Publication number
- KR101226620B1 KR101226620B1 KR1020110063422A KR20110063422A KR101226620B1 KR 101226620 B1 KR101226620 B1 KR 101226620B1 KR 1020110063422 A KR1020110063422 A KR 1020110063422A KR 20110063422 A KR20110063422 A KR 20110063422A KR 101226620 B1 KR101226620 B1 KR 101226620B1
- Authority
- KR
- South Korea
- Prior art keywords
- lithium
- hybrid supercapacitor
- electrode
- negative electrode
- doped
- Prior art date
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/13—Energy storage using capacitors
Landscapes
- Engineering & Computer Science (AREA)
- Power Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Electric Double-Layer Capacitors Or The Like (AREA)
- Manufacturing & Machinery (AREA)
Abstract
The present invention provides an anode comprising a porous activated carbon having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged, lithium-doped graphite, and lithium-doped lithium. A negative electrode comprising at least one negative electrode active material selected from soft carbon, lithium-doped hard carbon, lithium-doped activated carbon, lithium titanium-based oxide, and lithium transition metal oxide, and a separator for preventing a short circuit between the positive electrode and the negative electrode. And it relates to a method for producing a hybrid supercapacitor comprising an electrolyte solution in which lithium salt is dissolved between the positive electrode and the negative electrode. The hybrid supercapacitor according to the present invention has a high specific capacitance and an energy density due to the increase in the hybrid supercapacitor operating voltage caused by the electrode active materials of the positive electrode and the negative electrode.
Description
The present invention relates to a method of manufacturing a hybrid supercapacitor, and more particularly, to a porous activated carbon having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and having a plurality of pores that provide a passage through which electrolyte ions are introduced or discharged. A negative electrode including a positive electrode, at least one anode active material selected from lithium doped graphite, lithium doped soft carbon, lithium doped hard carbon, lithium doped activated carbon, lithium titanium-based oxide and lithium transition metal oxide The present invention relates to a method of manufacturing a hybrid supercapacitor having a high capacity per unit volume.
Supercapacitors are also commonly referred to as Electric Double Layer Capacitors (EDLCs), Supercapacitors or Ultracapacitors, which are the interface between electrodes and conductors and the electrolyte solution impregnated therewith. By using a pair of charge layers (electric double layers) each having a different sign, the deterioration due to repetition of the charge / discharge operation is very small and requires no maintenance. Accordingly, supercapacitors are mainly used in the form of backing up IC (integrated circuit) of various electric and electronic devices. Recently, the use of supercapacitors has been widely applied to toys, solar energy storage, and hybrid electric vehicle (HEV) power supply. have.
Such a supercapacitor generally includes two electrodes of a cathode and an anode impregnated with an electrolyte, a separator made of a porous material interposed therebetween to allow only ion conduction, and to prevent insulation and short circuit, and an electrolyte. It has a unit cell consisting of a gasket for preventing leakage and preventing insulation and short circuit, and a metal cap as a conductor for packaging them. One or more unit cells (usually, 2 to 6 in the case of a coin type) configured as described above are stacked in series and completed by combining two terminals of a positive electrode and a negative electrode.
The performance of the supercapacitor is determined by the electrode active material and the electrolyte, and in particular, the main performances such as the capacitance are mostly determined by the electrode active material. Activated carbon is mainly used as such an electrode active material. In general, activated carbon used as an electrode active material of a supercapacitor has a high specific surface area activated carbon of 1500 m 2 / g or more.
However, with the expansion of applications of supercapacitors, higher specific capacitances and energy densities are required, and thus, development of activated carbons expressing higher capacitances is required.
Conventionally, activated carbon is most widely used as an electrode active material of a cathode and an anode of a supercapacitor. Recently, research on a hybrid supercapacitor in which an activated carbon is replaced with another material has been actively conducted.
The problem to be solved by the present invention is an anode comprising a porous activated carbon having a plurality of pores having an average interlayer distance d 002 in the range 3.385 ~ 0.445nm and provides a passage through which electrolyte ions are introduced or discharged, graphite doped with lithium, lithium Hybrid having a high capacity per unit volume is composed of a cathode comprising at least one anode active material selected from a soft carbon doped with a lithium, a hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium-based oxide and lithium transition metal oxide The present invention provides a method for manufacturing a supercapacitor.
The present invention provides an anode comprising a porous activated carbon having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged, lithium-doped graphite, and lithium-doped lithium. A negative electrode comprising at least one negative electrode active material selected from soft carbon, lithium-doped hard carbon, lithium-doped activated carbon, lithium titanium-based oxide, and lithium transition metal oxide, and a separator for preventing a short circuit between the positive electrode and the negative electrode. And it provides a hybrid supercapacitor having an improved specific capacitance including an electrolyte solution in which lithium salt is dissolved between the positive electrode and the negative electrode.
The specific surface area of the porous activated carbon is preferably in the range of 300 to 1300 m 2 / g.
The lithium transition metal oxide is a complex metal oxide having a layered structure, a spinel structure, or an olivine structure containing lithium and a transition metal, and the transition metal is iron (Fe), cobalt (Co), nickel (Ni), molybdenum ( It is preferably at least one metal selected from the group consisting of Mo), tungsten (W) and copper (Cu).
The lithium oxide Tata nyumgye is preferably Li 4 Ti 5 O 12 or Li [Li 1/3 Ti 5 /3] O 4.
The lithium salt may be composed of at least one salt selected from LiPF 6 , LiBF 4 , LiClO 4 , Li (CF 3 SO 2 ) 2 , LiCF 3 SO 3 , LiSbF 6, and LiAsF 6 .
In addition, the present invention is a hybrid supercapacitor by mixing a porous activated carbon powder, a conductive material, a binder and a dispersion medium having a plurality of pores having an average interlayer distance d 002 ranges from 3.385 to 0.445 nm and provides a passage through which electrolyte ions are introduced or discharged Preparing a composition for a positive electrode and compressing the composition for a hybrid supercapacitor positive electrode to form an electrode, or coating the hybrid supercapacitor positive electrode composition with a metal foil to form an electrode or forming the electrode for the hybrid supercapacitor positive electrode Pushing the composition with a roller to form a sheet and attaching it to a metal foil to form an electrode; drying the composition for hybrid supercapacitor positive electrode formed in an electrode at a temperature of 100 ° C. to 350 ° C. to form a positive electrode; Graphite doped with lithium, soft carbon doped with lithium, lithium Preparing a composition for a hybrid supercapacitor negative electrode by mixing at least one negative electrode active material, a conductive material, a binder and a dispersion medium selected from hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium oxide and lithium transition metal oxide, The hybrid supercapacitor negative electrode composition is compressed to form an electrode, or the hybrid supercapacitor negative electrode composition is coated on a metal foil to form an electrode, or the hybrid supercapacitor negative electrode composition is pushed with a roller to form a sheet. Forming an electrode by attaching it to a metal foil, drying the composition for a hybrid supercapacitor negative electrode formed in the electrode form at a temperature of 100 ° C. to 350 ° C., and forming an anode, and an average interlayer distance d 002 ranging from 3.385 to 0.445 nm. And flows into or out of electrolyte ions A positive electrode comprising a porous activated carbon having a plurality of pores for providing a furnace, a negative electrode comprising the negative electrode active material, and a separator for preventing a short circuit between the positive electrode and the negative electrode between the positive electrode and the negative electrode, Provided is a method of manufacturing a hybrid supercapacitor having an improved specific capacitance, including injecting an electrolyte solution in which lithium salt is dissolved between a positive electrode and the negative electrode.
The porous activated carbon powder having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged is subjected to carbonization of the carbon material in an inert atmosphere at a temperature in the range of 550 to 1000 ° C. And activating the carbonized carbon material with alkali, and neutralizing and washing the activated product with an acid.
The activating treatment may include mixing the carbonized carbon material and the alkali in a weight ratio of 1: 1 to 1: 5, pulverizing the mixed product and in an inert atmosphere at a temperature of 600 to 900 ° C. And heat treating, wherein the alkali may be potassium hydroxide (KOH) or potassium hydroxide (NaOH).
The hybrid supercapacitor positive electrode composition has an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and 100 parts by weight of the porous activated carbon powder having a plurality of pores that provide a passage through which electrolyte ions are introduced or discharged, and 100% by weight of the porous activated carbon powder. The amount may include 2 to 20 parts by weight of the conductive material, 2 to 20 parts by weight of the binder, and 200 to 300 parts by weight of the dispersion medium based on 100 parts by weight of the porous activated carbon powder.
It is preferred that the specific surface area of the porous activated carbon powder having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and having a plurality of pores providing a passage through which electrolyte ions are introduced or discharged is in the range of 300 to 1300 m 2 / g.
The hybrid supercapacitor negative electrode composition may include at least one negative electrode active material selected from graphite doped with lithium, soft carbon doped with lithium, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium-based oxide, and lithium transition metal oxide. 100 parts by weight, 2 to 15 parts by weight of the conductive material and 2 to 10 parts by weight of the binder are added to 100 parts by weight of the negative electrode active material, and the dispersion medium is greater than 200 parts by weight and 300 parts by weight based on 100 parts by weight of the negative electrode active material. Preference is given to adding in small amounts.
The lithium-doped graphite, lithium-doped soft carbon, lithium-doped hard carbon, or lithium-doped activated carbon includes a working electrode containing graphite, soft carbon, hard carbon, or activated carbon, and a counterpart containing lithium foil. Arranging electrodes spaced apart from each other, injecting an electrolyte solution in which lithium salt is dissolved so that the working electrode and the counter electrode are impregnated, applying a voltage of -0.1 V to 0.6 V to the working electrode, and the counterpart Lithium from the electrode and the lithium salt may be obtained through the step of doping and electrodepositing the surface and the inside of graphite, soft carbon, hard carbon or activated carbon.
According to the present invention, an anode comprising a porous activated carbon having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged, doped with lithium-doped graphite and lithium A hybrid supercapacitor having a high capacity per unit volume is composed of a negative electrode comprising at least one anode active material selected from one of soft carbon, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium-based oxide, and lithium transition metal oxide. And a method for producing the same.
1 is a state diagram of use of the electrode according to the present invention.
2 is a view illustrating a state in which lead wires are attached to a positive electrode and a negative electrode.
3 is a view showing a state of forming a winding device.
4 is a view showing a state in which the winding element is inserted into the metal cap.
5 is a diagram illustrating a part of the hybrid supercapacitor cut away.
6 is a graph showing the average interlayer distance according to the carbonization temperature of the carbon material prepared according to Experimental Example 1.
FIG. 7 is a transmission electron microscope (TEM) photograph showing a carbon material before carbonization treatment after carbonization according to Experimental Example 1. FIG.
8 is a transmission electron microscope (TEM) photograph showing a porous activated carbon prepared according to Experimental Example 1. FIG.
9 is a graph showing discharge characteristics with time variation of a hybrid supercapacitor manufactured according to Experimental Example 2. FIG.
Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. However, the following embodiments are provided to those skilled in the art to fully understand the present invention, and may be modified in various forms, and the scope of the present invention is limited to the embodiments described below. It doesn't happen. Wherein like reference numerals refer to like elements throughout.
The present invention relates to a positive electrode comprising porous activated carbon having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged, graphite doped with lithium, and lithium. Doped graphitizable carbon (hereinafter referred to as "soft carbon"), lithium doped graphitizable carbon (hereinafter referred to as "hard carbon"), lithium doped activated carbon, lithium titanium A negative electrode comprising at least one negative electrode active material selected from the group oxides and lithium transition metal oxides, a separator for preventing a short circuit between the positive electrode and the negative electrode, and a lithium salt is dissolved between the positive electrode and the negative electrode It provides a hybrid supercapacitor comprising an electrolyte solution.
The anode of the hybrid supercapacitor of the present invention uses an electrode including porous activated carbon having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and having a plurality of pores that provide a passage through which electrolyte ions are introduced or discharged.
In a preferred embodiment of the present invention, the porous activated carbon used as the electrode active material of the anode of the hybrid supercapacitor is composed of porous carbon having an average interlayer distance d 002 of 3.385 to 0.445 nm and a specific surface area of 300 to 1300 m 2 / g. The porous activated carbon is a porous material having numerous pores that provide a passage through which electrolyte ions, a dispersion medium, and the like are introduced or discharged.
The porous activated carbon may be obtained by carbonizing and activating a graphitizable carbon material. The graphitizable carbon material may be pitch or coke or the like.
The negative electrode of the hybrid supercapacitor of the present invention is graphite doped with lithium, soft carbon doped with lithium, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium oxide and lithium transition. It comprises at least one negative electrode active material selected from metal oxides. The lithium titanium oxide is a complex metal oxide containing lithium and titanium, and the like can be Li 4 Ti 5 O 12, Li [Li 1/3 Ti 5/3] O 4 Examples. The lithium transition metal oxide is a complex metal oxide having a layered structure, a spinel structure, or an olivine structure containing lithium and a transition metal, and the transition metal is iron (Fe), cobalt (Co), nickel (Ni), molybdenum (Mo). ), At least one metal selected from the group consisting of tungsten (W) and copper (Cu). Examples of such lithium transition metal oxides include LiCoO 2 , LiNi 1/3 Co 1/3 Mn 1/3 O 2 , and the like.
Hereinafter, a method of producing porous activated carbon having a plurality of pores having an average interlayer distance d 002 in a range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged will be described in more detail.
A graphitizable carbon material is prepared, and the graphitizable carbon material is carbonized. Graphitizable carbon materials may be petroleum pitch, coal based pitch, petroleum coke, coal based coke and the like. The carbonization treatment is preferably carried out in an inert atmosphere for 10 minutes to 12 hours at a temperature of about 550 to 1000 ℃, preferably about 700 to 750 ℃. The inert atmosphere refers to a gas atmosphere such as nitrogen (N 2 ) and arcon (Ar).
The activation treatment is performed on the carbonized carbon material. In the activation treatment, carbonized carbon material and alkali such as potassium hydroxide (KOH), potassium hydroxide (NaOH), etc. are mixed and pulverized in a ratio of 1: 1 to 1: 5 in a weight ratio, and then the temperature is about 600 to 900 ° C. It is preferably carried out in an inert atmosphere for 10 minutes to 12 hours. The milling may be performed by ball milling, jet milling or the like. As a specific example of the grinding step, the ball milling step will be described. The graphitizing carbon material is charged into a ball milling machine, and is milled by rotating at a constant speed using the ball milling machine. The size of the balls, the milling time, the rotation speed of the ball miller, and the like are adjusted so as to be crushed to the target particle size. As the milling time increases, the particle size of the graphitized carbon powder gradually decreases, thereby increasing the specific surface area. The balls used for ball milling can be ceramic balls such as alumina (Al 2 O 3 ), zirconia (ZrO 2 ), and the balls may be all the same size or may be used together with balls having two or more sizes It is possible. The size of the ball, the milling time, and the rotation speed per minute of the ball mill are adjusted. For example, the size of the ball is set in the range of about 1 to 30 mm, and the rotation speed of the ball mill is about 50 to 500 rpm And ball milling can be performed for 1 to 50 hours.
After the activation treatment, neutralization treatment with an acid such as hydrochloric acid (HCl) and nitric acid (HNO 3 ) in order to remove the alkaline component, followed by rinsing with distilled water is sufficient. After washing, it is sufficiently dried for 10 minutes to 6 hours at a temperature of about 100 to 180 ° C.
The above-mentioned process can obtain porous activated carbon powder having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and a specific surface area in the range of 300 to 1300 m 2 / g.
Hereinafter, a method of manufacturing a positive electrode of a hybrid supercapacitor using the porous activated carbon powder having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged will be described. .
The positive electrode manufacturing method of the hybrid supercapacitor comprises a porous activated carbon powder, a conductive material, a binder, and a dispersion medium having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged. Preparing a hybrid supercapacitor positive electrode composition and compressing the hybrid supercapacitor positive electrode composition to form an electrode, or coating the hybrid supercapacitor positive electrode composition to a metal foil to form an electrode, or the hybrid super The composition of the capacitor positive electrode is pushed with a roller into a sheet state and attached to a metal foil to form an electrode, and the resultant formed in the form of an electrode is dried at a temperature of 100 ° C. to 350 ° C. to form a positive electrode of the hybrid supercapacitor. Include.
The porous activated carbon powder, as described above, carbonizing the graphitizable carbon material in an inert atmosphere at a temperature in the range of 550 to 1000 ° C., and activating the carbonized carbon material by mixing with the alkali. The step and the activated treated product can be obtained by neutralizing with acid and washing.
The activating treatment may include mixing the carbonized carbon material and the alkali in a weight ratio of 1: 1 to 1: 5, pulverizing the mixed product and in an inert atmosphere at a temperature of 600 to 900 ° C. And heat treating, wherein the alkali may be potassium hydroxide (KOH) or potassium hydroxide (NaOH).
The hybrid supercapacitor positive electrode composition is 100 parts by weight of the porous activated carbon powder, 2 to 20 parts by weight of a conductive material based on 100 parts by weight of the porous activated carbon powder, 2 to 20 parts by weight of a binder based on 100 parts by weight of the porous activated carbon powder, It may include 200 to 300 parts by weight of the dispersion medium based on 100 parts by weight of the porous activated carbon powder.
The specific surface area of the porous activated carbon is preferably in the range of 300 to 1300 m 2 / g.
The conductive material is not particularly limited as long as it is an electronic conductive material that does not cause chemical change, and examples thereof include metal powder or metal such as natural graphite, artificial graphite, carbon black, acetylene black, ketjen black, carbon fiber, copper, nickel, aluminum, silver, and the like. Fiber and the like.
In addition, the binder is polytetrafluoroethylene (PTFE), polyvinylidenefloride (PVDF), carboxymethylcellulose (CMC), polyvinyl alcohol (poly vinyl alcohol; PVA), polyvinyl butyral One or two or more selected from polyvinyl butyral (PVB), poly-N-vinylpyrrolidone (PVP), styrene butadiene rubber (SBR), and the like may be used.
The dispersion medium may be an organic solvent such as ethanol (EtOH), acetone, isopropyl alcohol, methyl pyrrolidone (NMP), propylene glycol, or water.
Hereinafter, the above-described average interlayer distance d 002 ranges from 3.385 to 0.445 nm and uses an anode including porous activated carbon having a plurality of pores that provide passages through which electrolyte ions are introduced or discharged. A method of manufacturing a hybrid supercapacitor will be described.
The hybrid supercapacitor of the present invention has a positive electrode including porous activated carbon having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged, and lithium-doped graphite and lithium A negative electrode including one or more negative electrode active materials selected from soft carbon doped with lithium, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium-based oxide, and lithium transition metal oxide; A separator may be disposed between the positive electrode and the negative electrode to prevent a short circuit between the positive electrode and the negative electrode, and an electrolyte solution in which lithium salt is dissolved may be injected between the positive electrode and the negative electrode.
The negative electrode is one selected from graphite doped with lithium, soft carbon doped with lithium, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium-based oxide, and lithium transition metal oxide. The negative electrode active material, the conductive material, the binder, and the dispersion medium are mixed to prepare a composition for a hybrid supercapacitor negative electrode, and the hybrid supercapacitor negative electrode composition is compressed to form an electrode, or the hybrid supercapacitor negative electrode composition is formed on a metal foil. Coating to form in the form of an electrode, or the composition for the hybrid supercapacitor negative electrode is pushed to a sheet state by a roller and attached to a metal foil to form an electrode, and the resultant formed in the form of an electrode dried to a temperature of 100 ℃ ~ 350 ℃ can do. The composition for the hybrid supercapacitor negative electrode is graphite doped with lithium, soft carbon doped with lithium, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium oxide and lithium transition metal. 100 parts by weight of the at least one negative electrode active material selected from the oxide, 2 to 15 parts by weight of the conductive material and 2 to 10 parts by weight of the binder are added to 100 parts by weight of the negative electrode active material, and the dispersion medium is 200 parts by weight to 100 parts by weight of the negative electrode active material. It is preferable to add by making it larger than a weight part and smaller than 300 weight part. It is preferable that the specific surface area of the said negative electrode active material is 0.1-100 m <2> / g.
The separator may be a polyethylene nonwoven fabric, a polypropylene nonwoven fabric, a polyester nonwoven fabric, a polyacrylonitrile porous separator, a poly (vinylidene fluoride) hexafluoropropane copolymer porous separator, a cellulose porous separator, a kraft paper or a rayon fiber, and the like. If the separator is generally used in the field is not particularly limited.
On the other hand, the electrolyte of the electrolyte solution filled in the hybrid supercapacitor of the present invention can be used that the lithium salt is dissolved as a non-aqueous electrolyte. The lithium salt is not particularly limited as a lithium salt commonly used in capacitors, for example, LiPF 6 , LiBF 4 , LiClO 4 , Li (CF 3 SO 2 ) 2 , LiCF 3 SO 3 , LiSbF 6 or LiAsF 6 Etc.
Although the solvent of the said electrolyte solution is not specifically limited, A cyclic carbonate solvent, a linear carbonate solvent, an ester solvent, an ether solvent, a nitrile solvent, and an amide solvent can be used. For example, ethylene carbonate, propylene carbonate, butylene carbonate, vinylene carbonate, or the like may be used as the cyclic carbonate solvent, and dimethyl carbonate, methyl ethyl carbonate, diethyl carbonate, or the like may be used as the chain carbonate solvent. The ester solvent may be methyl acetate, ethyl acetate, propyl acetate, methyl propionate, ethyl propionate, γ-butyrolactone, etc., and the ether solvent may be 1,2-dimethoxyethane, 1 , 2-diethoxyethane, tetrahydrofuran, 1,2-dioxane, 2-methyltetrahydrofuran, etc. may be used, and acetonitrile may be used as the nitrile solvent, and the amide solvent may be used. Dimethylformamide and the like can be used.
Hereinafter, a method of doping lithium to graphite, soft carbon, hard carbon or activated carbon will be described.
A working electrode coated with the graphite, soft carbon, hard carbon, or activated carbon on a metal foil and a counter electrode made of lithium foil are disposed to be spaced apart from each other, and an electrolyte solution in which lithium salt is dissolved is placed in the working electrode. And the working electrode and the counter electrode are immersed in the electrolyte. The lithium salt is not particularly limited as a lithium salt commonly used in capacitors, for example, LiPF 6 , LiBF 4 , LiClO 4 , Li (CF 3 SO 2 ) 2 , LiCF 3 SO 3 , LiSbF 6 or LiAsF 6 Etc. can be used. Although the solvent which comprises the said electrolyte solution is not specifically limited, A cyclic carbonate solvent, a linear carbonate solvent, ester solvent, an ether solvent, a nitrile solvent, an amide solvent, etc. can be used. Ethylene carbonate, propylene carbonate, butylene carbonate, vinylene carbonate, and the like may be used as the cyclic carbonate solvent, and dimethyl carbonate, methyl ethyl carbonate, diethyl carbonate, etc. may be used as the chain carbonate solvent. As the ester solvent, methyl acetate, ethyl acetate, propyl acetate, methyl propionate, ethyl propionate, γ-butyrolactone, and the like may be used. The ether solvent may be 1,2-dimethoxyethane or 1,2-diene. Methoxyethane, tetrahydrofuran, 1,2-dioxane, 2-methyltetrahydrofuran, etc. may be used, and acetonitrile may be used as the nitrile solvent, and dimethylformamide may be used as the amide solvent. Can be used.
In the reactor arranged as described above, a voltage of -0.1 V to 0.6 V as a power supply to the working electrode including graphite, soft carbon, hard carbon or activated carbon using lithium foil as a counter electrode. Is applied. It is preferable to apply -0.1 to 0.6V to the working electrode. Even though lithium doping occurs when the applied voltage is less than -0.1V, uniform doping may be difficult and doping when the applied voltage exceeds 0.6V. Since the amount of lithium is small, there may be a limit in improving the energy density per unit volume of the hybrid supercapacitor, and therefore, it is preferable to apply a voltage within the above range. The time for applying the voltage is preferably about 5 minutes to 120 minutes. When the time for applying the voltage is less than 5 minutes, the amount of lithium doped is small, which limits the energy density per unit volume of the hybrid supercapacitor. For example, when the time for applying the voltage exceeds 120 minutes, it is difficult to expect an improvement in energy density per unit volume.
When a voltage is applied to the working electrode, lithium is doped (electrodeposited) on the surface of graphite, soft carbon, hard carbon or activated carbon constituting the working electrode. Lithium from the lithium foil forming the counter electrode reaches the surface of graphite, soft carbon, hard carbon or activated carbon through the electrolyte and is doped on the surface of graphite, soft carbon, hard carbon or activated carbon, and is also included in the electrolyte. Lithium from the lithium salts thus reached reaches the graphite, softcarbon, hardcarbon or activated carbon surface and is doped to the surface of the graphite, softcarbon, hardcarbon or activated carbon. The lithium foil forming the counter electrode acts as a source of lithium in doping graphite, soft carbon, hard carbon or activated carbon with lithium, and lithium salts contained in the electrolyte are also used as graphite, soft carbon, hard carbon or activated carbon. It acts as a source of lithium in doping. Lithium doped in graphite, soft carbon, hard carbon or activated carbon by the lithium electrodeposition method reduces the potential of the cathode in the hybrid capacitor used as the negative electrode. Intercalation and deintercalation occur quickly by the doped lithium. Hybrid supercapacitors have a high energy density per unit volume by insertion and desorption by lithium doped on the surface of graphite, soft carbon, hard carbon or activated carbon. In addition, graphite, soft carbon, hard carbon or activated carbon constituting the working electrode has a large number of pores (pore), by the lithium electrodeposition method described above lithium is doped only on the surface of graphite, soft carbon, hard carbon or activated carbon. But also doping is carried out in the deep position inside the graphite, soft carbon, hard carbon or activated carbon along the pores connected to the inner or bulk (vulk). As such, lithium is doped not only on the surface of graphite, soft carbon, hard carbon, or activated carbon, but also on the bulk (inside), so that insertion and desorption processes occur in the bulk of graphite, soft carbon, hard carbon, or activated carbon during charging and discharging.
Hereinafter, embodiments according to the present invention will be described in more detail, and the present invention is not limited to the following examples.
≪ Example 1 >
The composition for a hybrid supercapacitor positive electrode comprising a porous activated carbon powder, a conductive material, a binder, and a dispersion medium having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged. To prepare. The hybrid supercapacitor positive electrode composition is 100 parts by weight of the porous activated carbon powder, 2 to 20 parts by weight of a conductive material based on 100 parts by weight of the porous activated carbon powder, 2 to 20 parts by weight of a binder based on 100 parts by weight of the porous activated carbon powder, It may include 200 to 300 parts by weight of the dispersion medium based on 100 parts by weight of the porous activated carbon powder. Since the composition for the hybrid supercapacitor positive electrode is dough, it may be difficult to uniformly mix (complete dispersion), using a mixer such as a planetary mixer for a predetermined time (for example, 10 minutes to 12 hours). Stirring can obtain a composition for a hybrid supercapacitor positive electrode suitable for electrode production. Mixers, such as planetary mixers, enable the preparation of compositions for hybrid supercapacitor anodes that are uniformly mixed.
The binder is polytetrafluoroethylene (PTFE), polyvinylidenefloride (PVDF), carboxymethylcellulose (CMC), polyvinyl alcohol (PVA), polyvinyl butyral (poly vinyl butyral (PVB), poly-N-vinylpyrrolidone (PVP), styrene butadiene rubber (SBR), polyamide-imide, polyimide, and the like. One or more selected species can be mixed and used.
The conductive material is not particularly limited as long as it is an electronic conductive material that does not cause chemical change, and examples thereof include natural graphite, artificial graphite, carbon black, acetylene black, ketjen black, super-P black, carbon fiber, copper, and nickel. Metal powders such as aluminum, silver, or metal fibers.
The dispersion medium may be an organic solvent such as ethanol (EtOH), acetone, isopropyl alcohol, N-methylpyrrolidone (NMP), propylene glycol (PG) or water.
The composition of the hybrid supercapacitor positive electrode, which is a mixture of activated carbon powder, a binder, a conductive material, and a dispersion medium, is compressed to form an electrode, or the hybrid supercapacitor positive electrode is coated on a metal foil to form an electrode, or the hybrid supercapacitor The composition for the positive electrode is pushed with a roller to form a sheet and attached to a metal foil to form an electrode, and the resultant formed in the electrode form is dried at a temperature of 100 ° C. to 350 ° C. to form a positive electrode.
Referring to the example of the step of forming the positive electrode in more detail, the composition for a hybrid supercapacitor positive electrode can be molded by pressing using a roll press molding machine. Roll press molding machine aims to improve electrode density and control electrode thickness by rolling, controller to control top and bottom roll and roll thickness and heating temperature, winding to unwind and wind anode It consists of wealth. As the rolled anode passes through the roll press, the rolling process proceeds, which is then rolled up again to complete the anode. At this time, it is preferable that the pressurization pressure of a press is 5-20 ton / cm <2>, and the temperature of a roll shall be 0-150 degreeC. The composition for the hybrid supercapacitor positive electrode, which has undergone the above-described press crimping process, is subjected to a drying process according to the present invention. The drying process is carried out at a temperature of 100 ° C to 350 ° C, preferably 150 ° C to 300 ° C. At this time, when the drying temperature is less than 100 ℃ is not preferable because the evaporation of the dispersion medium is difficult, and when the high temperature drying over 350 ℃ may occur oxidation of the conductive material is not preferable. Therefore, it is preferable that drying temperature is at least 100 degreeC or more and does not exceed 350 degreeC. And the drying process is preferably carried out for about 10 minutes to 6 hours at the above temperature. This drying process improves the strength of the hybrid supercapacitor positive electrode by drying (dispersing medium evaporation) the molded composition for the hybrid supercapacitor positive electrode and binding the powder particles.
The hybrid supercapacitor positive electrode manufactured as described above may be usefully applied to a small coin-type hybrid supercapacitor with high capacity.
The negative electrode is at least one selected from graphite doped with lithium, soft carbon doped with lithium, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium oxide and lithium transition metal oxide. A negative electrode active material, a conductive material, a binder and a dispersion medium are mixed to prepare a composition for a hybrid supercapacitor negative electrode, and the hybrid supercapacitor negative electrode composition is compressed to form an electrode, or the hybrid supercapacitor negative electrode composition is coated on a metal foil. To form in the form of an electrode, or the composition for the hybrid supercapacitor negative electrode with a roller to make a sheet state, and attached to a metal foil to form an electrode, the resultant formed in the form of an electrode to be dried at a temperature of 100 ℃ to 350 ℃ Can be. The hybrid supercapacitor negative electrode composition is added to 100 parts by weight of the negative electrode active material, 2 to 15 parts by weight of the conductive material and 2 to 10 parts by weight of the binder with respect to 100 parts by weight of the negative electrode active material, and the dispersion medium is contained in 100 parts by weight of the negative electrode active material. It is preferable to add more than 200 weight part with respect to less than 300 weight part with respect to manufacture. It is preferable that the specific surface area of the said negative electrode active material is 0.1-100 m <2> / g.
1 is a state diagram of a hybrid supercapacitor electrode according to the present invention, showing a cross-sectional view of a coin-type hybrid supercapacitor to which the
The coin-type hybrid supercapacitor comprises a positive electrode comprising a porous activated carbon having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and having a plurality of pores that provide a passage through which electrolyte ions are introduced or discharged, and the lithium-doped lithium A negative electrode comprising at least one negative electrode active material selected from graphite, soft carbon doped with lithium, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium-based oxide, and lithium transition metal oxide And a separator disposed between the anode and the cathode and preventing a short circuit between the anode and the cathode in a metal cap, and injecting an electrolyte solution in which an electrolyte is dissolved between the anode and the cathode. It can be produced by sealing with a gasket.
The separator may be a polyethylene nonwoven fabric, a polypropylene nonwoven fabric, a polyester nonwoven fabric, a polyacrylonitrile porous separator, a poly (vinylidene fluoride) hexafluoropropane copolymer porous separator, a cellulose porous separator, a kraft paper or a rayon fiber, and the like. If the separator is generally used in the field is not particularly limited.
The electrolyte of the electrolyte solution filled in the hybrid supercapacitor may be one in which lithium salt is dissolved as the nonaqueous electrolyte. The lithium salt is not particularly limited as a lithium salt commonly used in capacitors, for example, LiPF 6 , LiBF 4 , LiClO 4 , Li (CF 3 SO 2 ) 2 , LiCF 3 SO 3 , LiSbF 6 or LiAsF 6 Etc.
Although the solvent of the said electrolyte solution is not specifically limited, A cyclic carbonate solvent, a linear carbonate solvent, an ester solvent, an ether solvent, a nitrile solvent, and an amide solvent can be used. For example, ethylene carbonate, propylene carbonate, butylene carbonate, vinylene carbonate, or the like may be used as the cyclic carbonate solvent, and dimethyl carbonate, methyl ethyl carbonate, diethyl carbonate, or the like may be used as the chain carbonate solvent. The ester solvent may be methyl acetate, ethyl acetate, propyl acetate, methyl propionate, ethyl propionate, γ-butyrolactone, etc., and the ether solvent may be 1,2-dimethoxyethane, 1 , 2-diethoxyethane, tetrahydrofuran, 1,2-dioxane, 2-methyltetrahydrofuran, etc. may be used, and acetonitrile may be used as the nitrile solvent, and the amide solvent may be used. Dimethylformamide and the like can be used.
<Example 2>
2 to 5 are diagrams illustrating a hybrid supercapacitor according to another embodiment of the present invention, and a method of manufacturing the hybrid supercapacitor will be described in detail with reference to FIGS. 2 to 5.
The composition for a hybrid supercapacitor positive electrode is prepared by mixing a porous activated carbon powder, a binder, a conductive material, and a dispersion medium having a plurality of pores which have an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and provide a passage through which electrolyte ions are introduced or discharged. The manufacturing method is the same as the method described above in Example 1.
The hybrid supercapacitor positive electrode composition is coated on a metal foil such as aluminum foil or aluminum etching foil, or the hybrid supercapacitor positive electrode composition is pushed with a roller to form a sheet. It is made into a state (rubber type) and attached to a metal foil to produce an anode shape. The aluminum etching foil means that the aluminum foil is etched in an uneven shape.
The cathode shape after the above-mentioned process is subjected to a drying process. The drying process is carried out at a temperature of 100 ° C to 350 ° C, preferably 150 ° C to 300 ° C. At this time, when the drying temperature is less than 100 ℃ is not preferable because the evaporation of the dispersion medium is difficult, and when the high temperature drying over 350 ℃ may occur oxidation of the conductive material is not preferable. Therefore, it is preferable that drying temperature is at least 100 degreeC or more and does not exceed 350 degreeC. And the drying process is preferably carried out for about 10 minutes to 6 hours at the above temperature. This drying process improves the strength of the hybrid supercapacitor positive electrode by drying (dispersing medium evaporation) the composition for the hybrid supercapacitor positive electrode and binding the powder particles.
The negative electrode is at least one selected from graphite doped with lithium, soft carbon doped with lithium, hard carbon doped with lithium, activated carbon doped with lithium, lithium titanium oxide and lithium transition metal oxide. A negative electrode active material, a conductive material, a binder, and a dispersion medium are mixed to prepare a hybrid supercapacitor negative electrode composition, and the hybrid supercapacitor negative electrode composition is compressed to form an electrode, or the hybrid supercapacitor negative electrode composition is coated on a metal foil. To form in the form of an electrode, or the composition for the hybrid supercapacitor negative electrode with a roller to make a sheet state, and attached to a metal foil to form an electrode, the resultant formed in the form of an electrode to be dried at a temperature of 100 ℃ to 350 ℃ Can be. The hybrid supercapacitor negative electrode composition is added to 100 parts by weight of the negative electrode active material, 2 to 15 parts by weight of the conductive material and 2 to 10 parts by weight of the binder with respect to 100 parts by weight of the negative electrode active material, and the dispersion medium is contained in 100 parts by weight of the negative electrode active material. It is preferable to add more than 200 weight part with respect to less than 300 weight part with respect to manufacture. It is preferable that the specific surface area of the said negative electrode active material is 0.1-100 m <2> / g.
As shown in FIG. 2, the
As shown in FIG. 3, the
The
As shown in FIG. 4, a sealing
The electrolyte is injected and sealed so that the roll-shaped winding
The electrolyte of the electrolyte solution filled in the hybrid supercapacitor may be one in which lithium salt is dissolved as the nonaqueous electrolyte. The lithium salt is not particularly limited as a lithium salt commonly used in capacitors, for example, LiPF 6 , LiBF 4 , LiClO 4 , Li (CF 3 SO 2 ) 2 , LiCF 3 SO 3 , LiSbF 6 or LiAsF 6 Etc.
Although the solvent of the said electrolyte solution is not specifically limited, A cyclic carbonate solvent, a linear carbonate solvent, an ester solvent, an ether solvent, a nitrile solvent, and an amide solvent can be used. For example, ethylene carbonate, propylene carbonate, butylene carbonate, vinylene carbonate, or the like may be used as the cyclic carbonate solvent, and dimethyl carbonate, methyl ethyl carbonate, diethyl carbonate, or the like may be used as the chain carbonate solvent. The ester solvent may be methyl acetate, ethyl acetate, propyl acetate, methyl propionate, ethyl propionate, γ-butyrolactone, etc., and the ether solvent may be 1,2-dimethoxyethane, 1 , 2-diethoxyethane, tetrahydrofuran, 1,2-dioxane, 2-methyltetrahydrofuran, etc. may be used, and acetonitrile may be used as the nitrile solvent, and the amide solvent may be used. Dimethylformamide and the like can be used.
The hybrid supercapacitor manufactured as described above is schematically illustrated in FIG. 5.
In order to observe the characteristics of the hybrid supercapacitor according to the present invention, the following experiment was conducted.
<Experimental Example 1>
Mezo carbon micro beads (Mitsubishi Chemical), which is a graphitizing carbon material, were carbonized in a nitrogen atmosphere according to the following temperature conditions (carbonization temperature). The carbonization treatment was performed for 2 hours at temperatures of 550 ° C, 600 ° C, 650 ° C, 700 ° C, 750 ° C, 800 ° C, 850 ° C and 900 ° C, respectively.
The carbonized carbon material and potassium hydroxide (KOH) were mixed at a weight ratio of 1: 4 and ground using a dry ball milling process. The ball milling process using a zirconia ball, the size of the ball was about 5mm, the rotation speed of the ball mill was set to about 100rpm, ball milling was performed for 2 hours. An activation sample mixed with carbon material and potassium hydroxide was charged to a nickel (Ni) reactor, and an activation treatment was performed at 800 ° C. for 2 hours in an argon (Ar) atmosphere.
The activated sample was neutralized with hydrochloric acid (HCl) and washed with distilled water to obtain porous activated carbon as an electrode active material for a hybrid supercapacitor.
The porous activated carbon prepared in this way has an average interlayer distance d 002 in the range of 3.385 to 0.445 nm, a specific surface area in the range of 300 to 1300 m 2 / g, and a porous having a large number of pores that provide passages through which electrolyte ions and dispersion mediums are introduced or discharged. Made of carbon.
<Experimental Example 2>
Cathode active material consisting of MSP20 activated carbon, RP20 activated carbon or porous activated carbon prepared according to Experimental Example 1, Super-P black (conductor, Mitsubishi Chemical, Japan), binder, carboxymethylcellulose (CMC) and styrene Butadiene rubber (SBR) and distilled water as a dispersion medium were mixed in a weight ratio of 85: 5: 5: 5 to prepare a composition for a hybrid supercapacitor positive electrode. The mixing was performed using a planetary mixer (manufacturer: T.K, model name: Hivis disper), and mixed by stirring for 1 hour using a planetary mixer.
The composition for a hybrid supercapacitor positive electrode thus prepared was coated on an aluminum etching foil, and dried. The drying process was performed for 2 hours in a convection oven of about 120 ℃.
The dried resultant was punched to φ 12 mm to prepare an electrode specimen having a diameter of 12 mm and a height of 1.2 mm, and used as an anode.
100 parts by weight of Li 4 Ti 5 O 12 and 10 parts by weight of Super-p black (manufactured by Kuraray Chemical, Japan) as a conductive material were dry mixed. Separately, 10 parts by weight of polyvinylidene fluoride (PVdF) was added to N-methyl-2-pyrrolidone (NMP), which is methyl pyrrolidone, and mixed. Then, the mixture was added to a planetary mixer (manufacturer: TK, model name: Hivis disper), mixed and stirred for 1 hour, dispersed, and then mixed by stirring for 1 hour by adding 60 parts by weight of NMP hybrid supercapacitor. The negative electrode composition was obtained.
Next, the hybrid supercapacitor negative electrode composition was coated on a 20 μm aluminum etching foil and subjected to a drying process. The drying process was performed for 2 hours in a convection oven of about 120 ℃.
The dried resultant was punched to φ 12 mm to prepare an electrode specimen having a diameter of 12 mm and a height of 1.2 mm, and used as a cathode.
A hybrid supercapacitor having a coin cell type having a diameter of 20 mm and a height of 3.2 mm was prepared using the anode and the cathode thus prepared. In manufacturing the coin cell, TEABF 4 (tetraethylammonium tetrafluoborate) 1M and LiBF 4 (lithium tetrafluoroborate) 1M were added to a propylene carbonate (PC) solvent, and the separator used was TF4035 (manufactured by NKK, Japan). Used.
6 is a graph showing the average interlayer distance according to the carbonization temperature of the hybrid supercapacitor manufactured according to Experimental Example 1. FIG. Referring to FIG. 6, the average interlayer distance d 002 of the porous activated carbon at the carbonization temperature of 550 ° C. was about 4.445 nm, and as the carbonization temperature was increased, the average interlayer distance d 002 of the porous activated carbon gradually decreased, 900. The average interlayer distance d 002 of the porous activated carbon at a carbonization temperature of 캜 was about 3.602 nm.
7 is a transmission electron microscope (TEM) photograph showing a carbon material before carbonization treatment after carbonization according to Experimental Example 1, and FIG. 8 is a transmission electron microscope showing porous activated carbon prepared according to Experimental Example 1 Transmission electron microscope (TEM). Referring to FIGS. 7 and 8, the carbonized carbon material may be seen to have a plurality of layers spaced apart by an interlayer distance, and the porous activated carbon may have a plurality of pores.
9 is a graph showing discharge characteristics with time variation of a hybrid supercapacitor manufactured according to Experimental Example 2. FIG. The charge was performed at 0.1 A for 120 minutes until the charge voltage, and the discharge was performed at 1 A at 0.1 A. In FIG. 9, (a) shows a discharge curve when MSP20 activated carbon is used as the positive electrode active material, (b) shows a discharge curve when RP20 activated carbon is used as the positive electrode active material, and (c) shows the positive electrode active material according to Experimental Example 1 The discharge curve in the case of using the prepared porous activated carbon powder.
Referring to FIG. 9, when the porous activated carbon powder prepared according to Experimental Example 1 was used as the cathode active material, the specific capacitance thereof was the highest as 68.5 F / cc.
As mentioned above, although preferred embodiment of this invention was described in detail, this invention is not limited to the said embodiment, A various deformation | transformation by a person of ordinary skill in the art within the scope of the technical idea of this invention is carried out. This is possible.
10: hybrid supercapacitor electrode 50: metal cap
60: membrane 70: gasket
110: working electrode 120: anode
130: first lead wire 140: second lead wire
150: first separator 160: second separator
170: adhesive tape 175: winding element
180: sealing rubber 190: metal cap
195: lithium foil
Claims (12)
The hybrid supercapacitor positive electrode composition is compressed to form an electrode, or the hybrid supercapacitor positive electrode composition is coated on a metal foil to form an electrode, or the hybrid supercapacitor positive electrode composition is pushed with a roller to form a sheet. Attaching to a metal foil to form an electrode;
Drying the composition for a hybrid supercapacitor positive electrode formed in an electrode form at a temperature of 100 ° C. to 350 ° C. to form a positive electrode;
At least one negative electrode active material, conductive material, binder and dispersion medium selected from lithium doped graphite, lithium doped soft carbon, lithium doped hard carbon, lithium doped activated carbon, lithium titanium oxide and lithium transition metal oxide Mixing to prepare a composition for a hybrid supercapacitor negative electrode;
The hybrid supercapacitor negative electrode composition is compressed to form an electrode, or the hybrid supercapacitor negative electrode composition is coated on a metal foil to form an electrode, or the hybrid supercapacitor negative electrode composition is pushed with a roller to form a sheet. Attaching to a metal foil to form an electrode;
Drying the composition for a hybrid supercapacitor negative electrode formed in an electrode form at a temperature of 100 ° C. to 350 ° C. to form a negative electrode; And
An anode comprising a porous activated carbon having a plurality of pores having an average interlayer distance d 002 in the range of 3.385 to 0.445 nm and providing a passage through which electrolyte ions are introduced or discharged, a cathode including the anode active material, the anode and the cathode A method of manufacturing a hybrid supercapacitor having an improved specific capacitance, comprising disposing a separator for preventing a short circuit between the positive electrode and the negative electrode, and injecting an electrolyte solution in which lithium salt is dissolved between the positive electrode and the negative electrode. .
Carbonizing the carbon material in an inert atmosphere at a temperature in the range of 550-1000 ° C .;
Activating the carbonized carbon material by mixing with alkali; And
A method of manufacturing a hybrid supercapacitor having an improved specific capacitance, which is obtained by neutralizing and treating an activated product with an acid.
Mixing the carbonized carbon material with the alkali in a weight ratio of 1: 1 to 1: 5;
Pulverizing the mixed result; And
Heat treatment in an inert atmosphere at a temperature of 600-900 ° C.,
Said alkali is potassium hydroxide (KOH) or potassium hydroxide (NaOH), characterized in that the capacity of the hybrid supercapacitor with improved specific capacity.
A working electrode including graphite, soft carbon, hard carbon, or activated carbon and a counter electrode including lithium foil are disposed to be spaced apart from each other, and an electrolyte solution containing lithium salt dissolved therein is injected to impregnate the working electrode and the counter electrode. step;
Applying a voltage of -0.1 V to 0.6 V on the working electrode; And
A method of manufacturing a hybrid supercapacitor having improved specific capacitance, characterized in that the lithium obtained from the counter electrode and the lithium salt is obtained by being doped and deposited on the surface and the inside of graphite, soft carbon, hard carbon or activated carbon.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020110063422A KR101226620B1 (en) | 2011-06-29 | 2011-06-29 | Manufacturing method of hybrid supercapacitor having a high specific capacitance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020110063422A KR101226620B1 (en) | 2011-06-29 | 2011-06-29 | Manufacturing method of hybrid supercapacitor having a high specific capacitance |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| KR20130007080A KR20130007080A (en) | 2013-01-18 |
| KR101226620B1 true KR101226620B1 (en) | 2013-01-28 |
Family
ID=47837721
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR1020110063422A KR101226620B1 (en) | 2011-06-29 | 2011-06-29 | Manufacturing method of hybrid supercapacitor having a high specific capacitance |
Country Status (1)
| Country | Link |
|---|---|
| KR (1) | KR101226620B1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101409178B1 (en) * | 2013-04-24 | 2014-07-02 | 한국세라믹기술원 | Composite for supercapacitor electrode and manufacturing method of supercapacitor electrode using the composite |
| KR101696223B1 (en) | 2015-08-31 | 2017-01-16 | 한국전력공사 | Working car for power transmission line |
| KR102379507B1 (en) * | 2020-05-28 | 2022-03-28 | 한국수력원자력 주식회사 | High-density hybrid supercapacitor with phosphorine-based negative electrode and method of manufacturing thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002083747A (en) | 2000-09-08 | 2002-03-22 | Honda Motor Co Ltd | Activated carbon for electrode of electric double-layer capacitor |
| KR20080041720A (en) * | 2005-09-30 | 2008-05-13 | 가부시키가이샤 캬타라 | Carbonaceous material for electric double layer capacitor and electric double layer capacitor |
| JP2008130890A (en) | 2006-11-22 | 2008-06-05 | Hitachi Chem Co Ltd | Carbon material for hybrid capacitor, electrode for hybrid capacitor using carbon material, and hybrid capacitor |
| JP2008311363A (en) | 2007-06-13 | 2008-12-25 | Advanced Capacitor Technologies Inc | Method for predoping lithium ion and method for manufacturing lithium ion capacitor storage element |
-
2011
- 2011-06-29 KR KR1020110063422A patent/KR101226620B1/en not_active IP Right Cessation
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002083747A (en) | 2000-09-08 | 2002-03-22 | Honda Motor Co Ltd | Activated carbon for electrode of electric double-layer capacitor |
| KR20080041720A (en) * | 2005-09-30 | 2008-05-13 | 가부시키가이샤 캬타라 | Carbonaceous material for electric double layer capacitor and electric double layer capacitor |
| JP2008130890A (en) | 2006-11-22 | 2008-06-05 | Hitachi Chem Co Ltd | Carbon material for hybrid capacitor, electrode for hybrid capacitor using carbon material, and hybrid capacitor |
| JP2008311363A (en) | 2007-06-13 | 2008-12-25 | Advanced Capacitor Technologies Inc | Method for predoping lithium ion and method for manufacturing lithium ion capacitor storage element |
Also Published As
| Publication number | Publication date |
|---|---|
| KR20130007080A (en) | 2013-01-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR101137719B1 (en) | Manufacturing method of active carbon electrode for supercapacitor | |
| CN105489853B (en) | Composite anode active material and preparation method thereof, cathode and lithium secondary battery | |
| KR102344143B1 (en) | Predoping method for lithium, lithiumpredoped electrode, and electricity storage device | |
| KR101730956B1 (en) | Negative active material, manufacturing method thereof, and lithium battery containing the material | |
| KR101610772B1 (en) | Anode active materials and manufacturing method thereof, and anode and lithium battery using the same | |
| Lee et al. | A novel high-performance cylindrical hybrid supercapacitor with Li4− xNaxTi5O12/activated carbon electrodes | |
| CN111384388B (en) | High-energy-density lithium ion battery | |
| KR20130004536A (en) | Negative active material, manufacturing method thereof, and lithium battery containing the material | |
| KR20130012583A (en) | Composite of metal oxide nanoparticles and carbon, method for producing said composite, electrode using said composite, and electrochemical element | |
| KR101059934B1 (en) | Manufacturing method of hybrid supercapacitor | |
| KR20130028423A (en) | Electrode for supercapacitor using graphene/metal oxide nanocomposite | |
| KR101268872B1 (en) | Supercapacitor and manufacturing method of the same | |
| KR101166696B1 (en) | Supercapacitor and manufacturing method of the same | |
| KR101375623B1 (en) | Manufacturing method of supercapacitor electrode | |
| KR20170124700A (en) | Lithium-sulfur ultracapacitor and manufacturing method of the same | |
| KR101226620B1 (en) | Manufacturing method of hybrid supercapacitor having a high specific capacitance | |
| KR101340864B1 (en) | Active carbon-transition metal oxide for electrode active material and manufacturing method of the same | |
| KR101194999B1 (en) | Hybrid supercapacitor and manufacturing method of the same | |
| KR102202366B1 (en) | Negative active material for rechargeable lithium battery, method of preparing the same, and rechargeable lithium battery including the same | |
| CN113193182A (en) | Negative electrode material composition, negative electrode for lithium ion battery, and lithium ion battery | |
| KR101416804B1 (en) | Manufacturing Method For Cathode active material with Layer structure and Cathode active material thereof and hybrid capacitor comprising the same | |
| JP5927823B2 (en) | Negative electrode material for lithium ion secondary battery and method for producing the same, negative electrode for lithium ion secondary battery, and lithium ion secondary battery | |
| US10038191B2 (en) | Carbonous anode material, method for producing the same, and lithium-ion battery containing the anode material | |
| KR101166701B1 (en) | Composite for electrode of supercapacitor, method for manufacturing supercapacitor electrode using the composite, and supercapacitor using the method | |
| KR101137721B1 (en) | Manufacturing method of positive electrode for hybrid supercapacitor cell and hybrid supercapacitor cell manufactured by the method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A201 | Request for examination | ||
| E902 | Notification of reason for refusal | ||
| E701 | Decision to grant or registration of patent right | ||
| GRNT | Written decision to grant | ||
| FPAY | Annual fee payment |
Payment date: 20160108 Year of fee payment: 4 |
|
| FPAY | Annual fee payment |
Payment date: 20170119 Year of fee payment: 5 |
|
| LAPS | Lapse due to unpaid annual fee |