Titanium oxide-based supercapacitor electrode material and method of manufacturing same
10192690 ยท 2019-01-29
Assignee
Inventors
Cpc classification
C04B2235/3232
CHEMISTRY; METALLURGY
Y02E60/13
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
C04B35/62897
CHEMISTRY; METALLURGY
International classification
C04B35/622
CHEMISTRY; METALLURGY
Abstract
A titanium oxide-based supercapacitor electrode material and a method of manufacturing same. A reactive substance of the titanium oxide-based supercapacitor electrode material is a conductive titanium oxide. The conductive titanium oxide is a sub-stoichiometric titanium oxide, reduced titanium dioxide, or doped reduced titanium dioxide obtained by further doping an element in reduced titanium dioxide. The titanium oxide-based supercapacitor electrode material has a carrier concentration greater than 10.sup.18 cm.sup.3, and the titanium oxide-based supercapacitor electrode material has a specific capacitance 20 F/g to 1,740 F/g at a charge/discharge current of 1 A/g.
Claims
1. A titanium oxide-based supercapacitor electrode material, comprising a conductive titanium oxide as an active substance, wherein the conductive titanium oxide is selected from the group consisting of titanium sub-oxide, reduced titanium dioxide, and doped reduced titanium dioxide, a whole or a surface of the titanium sub-oxide, the reduced titanium dioxide, or the doped reduced titanium dioxide having amorphous layers comprising defect structures and activated Ti.sup.3+; and the titanium oxide-based supercapacitor electrode material has a density of charge carrier higher than 10.sup.18 cm.sup.3, and a specific capacitance in a range of 20 F/g1,740 F/g, under a charge-discharge current of 1 A/g; and the titanium sub-oxide, the reduced titanium dioxide, or the doped reduced titanium dioxide is prepared by a step of performing a high surface reduction treatment on titanium dioxide to obtain the titanium sub-oxide or the reduced titanium dioxide, or by a step of performing the high surface reduction treatment and a doping treatment on titanium dioxide to obtain the doped reduced titanium dioxide; wherein the high surface reduction treatment is performed at 200500 C. for 212 hours.
2. The titanium oxide-based supercapacitor electrode material according to claim 1, characterized in that the specific capacitance of the titanium oxide-based supercapacitor electrode material is in a range of 20 F/g1,872 F/g at a charge-discharge rate of 2 mV/s, 15 F/g1,130 F/g at a charge-discharge rate of 10 mV/s, 10 F/g930 F/g at a charge-discharge rate of 50 mV/s, and 10 F/g571 F/g at a charge-discharge rate of 100 mV/s, respectively, and has an attenuation of less than 5% after 1,000 cycles, less than 8% after 5,000 cycles, and less than 10% after 10,000 cycles, respectively.
3. The titanium oxide-based supercapacitor electrode material according to claim 1, characterized in that the titanium oxide-based supercapacitor electrode material can serve as a positive electrode active material, a negative electrode active material, or a synergic material in a supercapacitor, and the titanium oxide-based supercapacitor electrode material can be used to construct a symmetric supercapacitor with both of a positive electrode and a negative electrode comprising the titanium oxide-based supercapacitor electrode material.
4. The titanium oxide-based supercapacitor electrode material according to claim 1, characterized in that a doping element of the doped reduced titanium dioxide is a metal element and/or a non-metal element, the metal element is one or more elements selected from the group consisting of vanadium, chromium, manganese, iron, cobalt, nickel, copper, niobium, molybdenum, tantalum, ruthenium, silver, platinum, tungsten, cadmium, and rhodium, and the non-metal element is one or more elements selected from the group consisting of hydrogen, nitrogen, carbon, boron, sulfur, selenium, phosphorus, fluorine, chlorine, bromine, and iodine.
5. The titanium oxide-based supercapacitor electrode material according to claim 4, characterized in that a thickness of the amorphous layer is 0.5 nm or more.
6. The titanium oxide-based supercapacitor electrode material according to claim 4, characterized in that the defect structure includes oxygen vacancies, interstitial titanium, and/or direct bonding between titanium and titanium.
7. The titanium oxide-based supercapacitor electrode material according to claim 1, characterized in that an apparent color of the titanium sub-oxide, the reduced titanium dioxide, or the doped reduced titanium dioxide ranges from yellow to green to brown to blue to gray to black depending on a conductivity.
8. A titanium oxide-based supercapacitor electrode comprising the titanium oxide-based supercapacitor electrode material according to claim 1, characterized in that the titanium oxide-based supercapacitor electrode comprises a conductive substrate, and the titanium sub-oxide, the reduced titanium dioxide or the doped reduced titanium dioxide supported on the conductive substrate, and the conductive substrate includes a metal substrate, a carbon material substrate, and a conductive glass selected from the group consisting of FTO, ITO, AZO, ZnO:B, ZnO:Ga, ZnO:In, Cd.sub.2SnO.sub.4, Zn.sub.2SnO.sub.4, TiO.sub.2:Nb, SrTiO.sub.3:Nb, CuS, CuAlO.sub.2 and CuAlS.sub.2.
9. A titanium oxide-based supercapacitor electrode comprising the titanium oxide-based supercapacitor electrode material according to claim 1, characterized in that the titanium oxide-based supercapacitor electrode is a free-standing titanium oxide-based supercapacitor electrode formed by the titanium sub-oxide, the reduced titanium dioxide, or the doped reduced titanium dioxide.
10. A method for preparing a titanium oxide-based supercapacitor electrode comprising the titanium oxide-based supercapacitor electrode material according to claim 1, comprising: mixing the titanium sub-oxide, the reduced titanium dioxide, or the doped reduced titanium dioxide with a solvent and an aid to obtain a slurry; and a coating method of coating the slurry on a conductive substrate followed by drying to obtain a conductive substrate-supporting titanium oxide-based supercapacitor electrode, or drying the slurry followed by milling and tabletting to obtain a free-standing titanium oxide-based supercapacitor electrode.
11. The method according to claim 10, characterized in that the aid includes a binder, and a conductive agent.
12. The method according to claim 11, characterized in that the conductive agent is one or more agents selected from the group consisting of acetylene black, carbon black, artificial graphite, natural graphite, flake graphite, vapor grown carbon fibers, carbon nanotubes, metal powders, and metal fibers.
13. The method according to claim 11, characterized in that the binder is one or more agents selected from the group consisting of polytetrafluoroethylene, polyvinylidene fluoride, polyethylene, polypropylene, polyacrylamide, ethylene-propylene-diene copolymer resin, styrene-butadiene rubber, polybutadiene, fluorine rubber, polyethylene oxide, polyvinyl pyrrolidone, polyester resins, acrylic resins, phenolic resins, epoxy resins, polyvinyl alcohol, and hydroxypropyl cellulose.
14. The method according to claim 11, characterized in that, in the slurry, a concentration of the titanium sub-oxide, the reduced titanium dioxide, or the doped reduced titanium dioxide is 0.0011 g/mL, a concentration of the binder is 150 mg/mL, and a mass ratio of the conductive agent to the reduced titanium dioxide or the doped reduced titanium dioxide is (0.0510):1.
15. The method according to claim 10, characterized in that the step of performing the high surface reduction treatment on the titanium dioxide to obtain the titanium sub-oxide or the reduced titanium dioxide comprises performing the high surface reduction treatment on titanium dioxide using a highly active metal or under a reducing atmosphere to obtain the titanium sub-oxide or the reduced titanium dioxide; the step of performing the high surface reduction treatment and the doping treatment on titanium dioxide to obtain the doped reduced titanium dioxide comprises: performing the high surface reduction treatment on titanium dioxide using a highly active metal or under a reducing atmosphere followed by performing a metal and/or non-metal doping treatment; or performing the metal and/or non-metal doping treatment on titanium dioxide followed by performing the high surface reduction treatment on the doped titanium dioxide using a highly active metal or under a reducing atmosphere, to obtain the doped reduced titanium dioxide.
16. The method according to claim 10, characterized in that the solvent is one or more solvents selected from the group consisting of water, alcohols, polyols, terpenes, N-methyl-2-pyrrolidone, dimethyl carbonate, diethyl carbonate, ethyl acetate, and methyl propionate.
17. The method according to claim 10, characterized in that the coating method is one or more methods selected from the group consisting of dip-coating, knife coating, spin coating, spray coating, screen printing, and suspended particles dip coating.
18. The method according to claim 10, characterized in that the titanium dioxide has one or more phases selected from the group consisting of amorphous phase, anatase phase, rutile phase, and brookite phase; and the titanium dioxide has one or more morphologies selected from the group consisting of ball, rod, strip, tube and irregular polygons.
19. A method for preparing a titanium oxide-based supercapacitor electrode comprising the titanium oxide-based supercapacitor electrode material according to claim 1, comprising: applying titanium dioxide on a conductive substrate followed by drying to obtain a conductive substrate-supporting titanium dioxide electrode, or drying a slurry containing titanium dioxide followed by milling and tabletting to obtain a free-standing titanium oxide electrode; and performing the high surface reduction treatment or the high surface reduction treatment and the doping treatment on the conductive substrate-supporting titanium dioxide electrode or the free-standing titanium oxide electrode to obtain the supercapacitor electrode.
20. The method according to claim 19, characterized in that the high surface reduction treatment or the high surface reduction treatment and doping treatment is: performing the high surface reduction treatment on the conductive substrate-supporting titanium dioxide electrode or the free-standing titanium oxide electrode using a highly active metal or under a reducing atmosphere; performing the high surface reduction treatment on the conductive substrate-supporting titanium dioxide electrode or the free-standing titanium oxide electrode using a highly active metal or under a reducing atmosphere followed by performing a metal and/or non-metal doping treatment; or performing the metal and/or non-metal doping treatment on the conductive substrate-supporting titanium dioxide electrode or the free-standing titanium oxide electrode followed by performing the high surface reduction treatment using a highly active metal or under a reducing atmosphere.
21. The method according to claim 20, characterized in that the doping treatment is performed at 2001,000 C. for 212 hours.
22. The method according to claim 19, characterized in that the method for applying is one or more methods selected from the group consisting of dip-coating, knife coating, spin coating, spray coating, screen printing method, suspended particles dip coating, anodic electrodeposition, cathodic electrodeposition, electrophoresis, spray pyrolysis, chemical vapor deposition, and physical vapor deposition.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION OF THE EMBODIMENTS
(10) The present invention will be further described with the following embodiments below with reference to the drawings. It should be understood that the drawings and the following embodiments are only used for explaining this invention, and do not limit this invention.
(11) The present invention aims to overcome the problems (such as not taking into account the energy density and power density, high cost, incapability of being made into a symmetric device, the cycle of poor performance, etc.) of the conventional supercapacitor materials, to provide a supercapacitor electrode material with a higher power density, a higher energy density, and a better cyclicity using titanium oxide as the main active substance, a supercapacitor electrode prepared by the material, and a method for preparing the supercapacitor electrode. In the present invention, a reduction treatment and/or a doping treatment are employed to create defects at the surface of the titanium dioxide material which is insulative in the intrinsic state, so that the titanium oxide has a certain conductivity, and thus can be used in a supercapacitor. The titanium oxide-based supercapacitor prepared in the present invention has the advantages of high energy density (20111.8 Wh/kg), high power density (198 kW/kg) and good cyclicity (80%98% retention after 10,000 cycles), and low cost, thus having broad prospective applications.
(12) Firstly, the present invention provides a doped reduced titanium dioxide supercapacitor electrode material, the supercapacitor electrode material including reduced titanium dioxide and doped reduced titanium dioxide, which at their surface have amorphous layers comprising defect-structures and activated Ti.sup.3+, wherein the doping element includes metal and/or non-metal elements, the metal element is one or more elements selected from the group consisting of vanadium, chromium, manganese, iron, cobalt, nickel, copper, niobium, molybdenum, tantalum, ruthenium, silver, platinum, tungsten, cadmium, and rhodium, the non-metal element is one or more elements selected from the group consisting of hydrogen, nitrogen, carbon, boron, sulfur, selenium, phosphorus, fluorine, chlorine, bromine, and iodine. The defect structure includes oxygen vacancies, interstitial titanium, and/or direct bonding between titanium and titanium. The apparent color of the reduced titanium dioxide or the doped reduced titanium dioxide ranges from yellow to green to brown to blue to gray to black depending on the conductivity, and the density of the charge carriers of the powder ranges from 10.sup.18 to 10.sup.22 cm.sup.3. The reduced titanium dioxide or the doped reduced titanium dioxide may be supported on a conductive substrate to form an electrode, or form a free-standing electrode without a supporter by direct tabletting.
(13) As shown in the TEM image of
(14) The conductive substrate includes, but is not limited to, a metal substrate, a carbon material substrate, and a conductive glass selected from the group consisting of FTO, ITO, AZO, ZnO:B, ZnO:Ga, ZnO:In, Cd.sub.2SnO.sub.4, Zn.sub.2SnO.sub.4, TiO.sub.2:Nb, SrTiO.sub.3:Nb, CuS, CuAlO.sub.2, and CuAlS.sub.2.
(15) The present invention further provides two methods for preparing the two supercapacitor electrodes above.
(16) The first preparation method (a) comprises: performing a high surface reduction treatment and/or a doping treatment on titanium dioxide to obtain a reduced titanium dioxide or a doped reduced titanium dioxide; mixing the doped reduced titanium dioxide with aids (such as conductive agent and binder) and solvent to obtain a slurry; and coating the slurry on a conductive substrate followed by drying to obtain a conductive substrate-supporting electrode, or directly drying the slurry followed by tabletting. The high surface reduction treatment may be prior to the doping treatment, for example, titanium dioxide is submitted to a high surface reduction treatment using a highly active metal or under a reducing atmosphere to obtain a reduced titanium dioxide; and the reduced titanium dioxide is submitted to a metal or non-metal doping treatment to obtain a doped reduced titanium dioxide. However, it should be understood that the doping treatment may be prior to the reduction treatment.
(17) The second preparation method (b) comprises: applying titanium oxide on a conductive substrate followed by drying to obtain an electrode provided with titanium oxide, or drying a slurry containing titanium oxide followed by tabletting to obtain a free-standing electrode; and performing a high surface reduction treatment and a doping treatment on the electrode provided with titanium oxide or the free-standing titanium oxide electrode to obtain the titanium oxide-based supercapacitor electrode material. The high surface reduction treatment may be prior to the doping treatment, for example, the electrode provided with titanium oxide is submitted to a high surface reduction treatment using a highly active metal or under a reducing atmosphere to obtain an electrode provided with reduced titanium dioxide; and the electrode provided with reduced titanium dioxide is submitted to a metal or non-metal doping treatment to obtain a doped reduced titanium dioxide supercapacitor electrode material. However, it should be understood that the doping treatment may be prior to the reduction treatment.
(18) In the first preparation method (a) and/or the second preparation method (b), the titanium dioxide as the raw material includes, but is not limited to, one or more phases selected from the group consisting of amorphous phase, anatase phase, rutile phase, and brookite phase. The morphology thereof includes, but is not limited to, one or more morphologies selected from the group consisting of ball, rod, strip, tube, and irregular polygons. The titanium dioxide may be commercial or self-made, for example, be prepared through hydrolysis of titanium tetrachloride.
(19) The highly active metal used includes, but is not limited to, one or more metals selected from the group consisting of lithium, magnesium, aluminum, calcium, gallium, strontium, indium, and barium. The reducing atmosphere includes, but is not limited to, a mixture of hydrogen and argon, wherein the ratio of argon to hydrogen may be (020):1.
(20) Hereinafter, a process according to the first preparation method (a) will be described as an example.
(21) (a-1) The high surface reduction treatment on titanium dioxide.
(22) Titanium dioxide is submitted to a high surface reduction treatment using a highly active metal or under a reducing atmosphere to obtain reduced titanium dioxide.
(23) The reduction method using a highly active metal includes, but is not limited to, one of or a combination of a dual-temperature-zone metal-aided reduction method and a metal-mixed with-titanium dioxide vacuum annealing method.
(24) Taking the dual-temperature-zone metal-aided reduction method as an example, it may comprise the following steps.
(25) 1) A highly active metal and a titanium dioxide power are placed in different heating sections in a sealed container, respectively, and the container is vacuumized to a specified negative pressure. The container may be a sealable and heatable tube furnace. The titanium dioxide and the highly active metal (e.g., aluminum) are placed in different positions spaced apart from each other in a sealed system so as to receive different heating environments. The specified negative pressure may be less than 30 Pa, preferably less than 1 Pa, for example, less than 0.1 Pa.
(26) 2) The section in which the highly active metal is placed and the section in which the titanium dioxide is placed are heated to different temperatures. Specifically, the highly active metal is placed in a section with a higher temperature (a first temperature, e.g., 5001500 C., preferably 7001,000 C.), and the titanium dioxide is placed in a section with a lower temperature (a second temperature, e.g., 100600 C., preferably 300500 C.), such that a dual-temperature-zone reduction system is realized by a simple device. Under the negative pressure, the highly active metal is heated to react with the oxygen in the system, thus lowering the oxygen partial pressure of the whole system. Once the oxygen partial pressure is lower than the equilibrium oxygen partial pressure of titanium dioxide, the titanium dioxide is reduced, and thus, a reduced titanium dioxide is obtained.
(27) 3) After a treatment for 212 h, the heating power is turned off. The sample cools down, and a reduced titanium dioxide powder is obtained.
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(29) The metal-mixed with-titanium dioxide vacuum annealing method may comprise the following process: a highly active metal is mixed with a titanium dioxide powder, and the resulting mixture is heated to 2001,000 C. (preferably 300500 C.) so that the titanium dioxide is reduced.
(30) The method of performing a reduction treatment on titanium dioxide under a reducing atmosphere includes, but is not limited to, one or more methods selected from the group consisting of a high-temperature annealing method, a high-pressure annealing method, and a plasma-assisted method.
(31) Taking the plasma-assisted method as an example, it may comprise the following steps.
(32) 1) A titanium dioxide powder is placed in a sealed container, and the system is vacuumized to a base pressure lower than 30 Pa, preferably lower than 1 Pa, for example lower than 0.1 Pa. The sealed system used may, for example, be a sealable and heatable tube furnace.
(33) 2) RF gas (hydrogen or a mixture of argon and hydrogen (with a molar ratio of 020):1)) is supplied to the sealed container as vacuumized in step 1). Herein, the sealed system may be supplied with hydrogen or a mixture of argon and hydrogen at the same time of vacuumizing in advance, so as to expel the residual oxygen from the sealed system, before being supplied with the gas above.
(34) 3) The sealed container after step (b) is heated to 100600 C., preferably 300500 C.
(35) 4) Once the sealed container is heated to a target temperature as mentioned in step 3), the gas flow is regulated in such a manner that the pressure inside the container is maintained at 50500 Pa, preferably 100300 pa, and the RF power is turned on, with the power thereof being 50500 W, preferably 100300 W, so that the gas in the container is ionized to generate plasma. Such treatment lasts for 212 h.
(36) 5) After the treatment, the RF power and the heating power are turned off successively. After the sample cools down, the gas flow is cut off. Thus, a reduced titanium dioxide powder is obtained.
(37) (a-2) The doping treatment for the reduced titanium dioxide powder.
(38) The reduced titanium dioxide powder is submitted to a non-metal (hydrogen, nitrogen, carbon, boron, sulfur, selenium, phosphorus, fluorine, chlorine, bromine, iodine, etc.) doping and/or a metal (vanadium, chromium, manganese, iron, cobalt, nickel, copper, niobium, molybdenum, tantalum, ruthenium, silver, platinum, tungsten, cadmium, rhodium, etc.) doping to give a doped reduced titanium dioxide. Taking nitrogen-doping as an example, the process may comprise the following steps: the reduced titanium dioxide powder is placed in a sealed container, and the sealed container is supplied with ammonia gas, and heated to 2001,000 C. (preferably 400600 C.) and kept thereat for 212 h (preferably 48 h) to give a nitrogen-doped reduced titanium dioxide powder. Doping of other non-metal elements and/or metal elements can be conducted using a corresponding dopant referring to the method above or by other methods. For example, in the case of sulfur doping, hydrogen sulfide can be supplied to the sealed container which is heated to 2001,000 C. (preferably 400600 C.) and kept thereat for 212 h (preferably 48 h) to give a sulfur-doped reduced titanium dioxide powder.
(39) (a-3) The doped reduced titanium dioxide powder and a conductive agent are added to a solvent in which a binder is dispersed, and uniformly stirred to get a slurry in which the concentration of the doped reduced titanium dioxide powder is 0.11 g/mL, and the concentration of the binder is 1050 mg/mL. The conductive agent used includes, but is not limited to, one or more conductive agents selected from the group consisting of acetylene black, carbon black, artificial graphite, natural graphite, flake graphite, vapor grown carbon fibers, carbon nanotubes, metal powders, and metal fibers. The binder used includes, but is not limited to, one or more binders selected from the group consisting of polytetrafluoroethylene, polyvinylidene fluoride, polyethylene, polypropylene, polyacrylamide, ethylene-propylene-diene copolymer resin, styrene-butadiene rubber, poly butadiene, fluorine rubber, polyethylene oxide, polyvinyl pyrrolidone, polyester resins, acrylic resins, phenolic resins, epoxy resins, polyvinyl alcohol, and hydroxypropyl cellulose. The solvent used includes, but is not limited to, one or more solvents selected from the group consisting of water, alcohols, polyols, terpenes, N-methyl-2-pyrrolidone, dimethyl carbonate, diethyl carbonate, ethyl acetate, and methyl propionate carbonate.
(40) (a-4) The slurry is uniformly coated on a conductive substrate, and the solvent is dried, to give the doped reduction titanium dioxide supercapacitor electrode of the present invention. The method for coating includes, but is not limited to, one or more methods selected from the group consisting of dip-coating, knife coating, spin coating, spray coating, screen printing, suspended particles dip coating. Alternatively, the powder obtained by drying the slurry is submitted to tabletting to give the free-standing doped reduction titanium dioxide supercapacitor electrode of the present invention.
(41) Hereinafter, a process according to the second preparation method (b) will be described as an example.
(42) (b-1) Titanium dioxide is uniformly applied to a conductive substrate to give an electrode provided with titanium dioxide. The method for applying includes, but is not limited to, one or more methods selected from the group consisting of dip-coating, knife coating, spin coating, spray coating, screen printing method, suspended particles dip coating, anodic electrodeposition, cathodic electrodeposition, electrophoresis, spray pyrolysis, chemical vapor deposition, and physical vapor deposition. Alternatively, the powder obtained by drying the slurry is submitted to tabletting to give the free-standing titanium dioxide supercapacitor electrode.
(43) (b-2) The titanium dioxide electrode is submitted to a high surface reduction treatment. This treatment may refer to step (a-1), except that the titanium dioxide in step (a-1) is replaced by the titanium dioxide electrode. After this step, a reduced titanium dioxide electrode is obtained.
(44) (b-3) The reduced titanium dioxide electrode is submitted to a doping treatment. This treatment may refer to step (a-2), except that the reduced titanium dioxide in step (a-2) is replaced by the reduced titanium dioxide electrode. After this step, a doped reduced titanium dioxide electrode material of the present invention is obtained.
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(63) Hereinafter, the present invention will be better described with the following representative examples. It is should be understood that the following examples are only used to explain this invention and do not limit the scope of this invention, and any non-essential improvements and modifications made by a person skilled in the art based on this invention all fall into the protection scope of this invention. The specific parameters below such as temperature and time are only exemplary, and a person skilled in the art can choose proper values within an appropriate range according to the description of this article, and are not restricted to the specific values cited below.
Example 1
(64) A commercial titanium oxide powder (P25) as the raw material, and an aluminum metal as the highly active reducing metal are placed in different heating sections in a sealed tube furnace, respectively, and the whole system is vacuumized to 0.1 Pa. Then the aluminum and the titanium oxide are heated to 800 C. and 300500 C., respectively. After a reaction of 8 hours, the heating power is turned off, and the sample cools down. To 3 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the reduced P25 powder. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The titanium dioxide slurry is uniformly coated on a nickel net by knife coating, then dried under vacuum at 100 C. for 8 h.
(65) The picture of the reduced titanium dioxide (TiO.sub.2-x) powder is shown in
(66) The density of charge carrier of the reduced titanium dioxide powder is 8.3*10.sup.20 cm.sup.3.
(67) The TEM and SEM images of the nano titanium dioxide on the nickel net are shown in
(68) As shown in
(69) The electrode coated with the reduced titanium dioxide powder is submitted to a constant current charge-discharge test, and the result is shown in
Example 2
(70) An amorphous titanium dioxide made by hydrolysis of titanium tetrachloride as the raw material, and an aluminum metal as the highly active reducing metal are uniformly mixed together and placed in a sealed tube furnace, and the whole system is vacuumized to 0.1 Pa. Then the sample is heated to 300500 C. After a reaction for 8 hours, the heating power is turned off, and the sample cools down. Then, an ammonia gas is filled into the sealed system, and the titanium dioxide is heated to 600 C. to undergo a nitriding treatment for 4 h. The sample is taken out after cooling down. To 3 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the reduced black powder. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The titanium dioxide slurry is uniformly coated on a nickel net by knife coating, then dried under vacuum at 100 C. for 8 h.
(71) As shown in TiO.sub.2N of
(72) Amorphous layers with a thickness of 215 nm are formed at the surface of the reduced and nitrided amorphous titanium dioxide powder.
(73) A CV test shows that, as compared with electrode by coating the untreated amorphous powder on the nickel net, the supercapacitor electrode obtained by coating the reduced and nitrided amorphous titanium dioxide powder on the nickel net has a significantly increased capacitance, which is 197 F/g at a scan rate of 100 mV/s by calculating. A constant current charge-discharge test is performed on the supercapacitor electrode obtained by coating the reduced and nitrided amorphous titanium dioxide powder on the nickel net, and the calculation result shows that the capacitance of the reduced and nitrided powder is 273 F/g under a charge-discharge current of 1 A/g.
Example 3
(74) An amorphous titanium dioxide made by hydrolysis of titanium tetrachloride (same as that in Example 2) as the raw material, and an aluminum metal as the highly active reducing metal are uniformly mixed together and placed in a sealed tube furnace, and the whole system is vacuumized to 0.1 Pa. Then the sample is heated to 500 C. After a reaction for 8 hours, the heating power is turned off, and the sample cools down. Then, a hydrogen sulfide gas is filled into the sealed system, and the titanium dioxide is heated to 600 C. to undergo a sulfuration treatment for 4 h. The sample is taken out after cooling down. To 1.5 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the reduced and sulfurized amorphous powder. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The titanium dioxide slurry is uniformly coated on a nickel net by knife coating, then dried under vacuum at 100 C. for 8 h.
(75) As shown in TiO.sub.2S of
(76) The capacitance of the supercapacitor electrode obtained by coating the reduced and sulfurized amorphous titanium dioxide powder on the nickel net significantly increases, which is 157 F/g, as calculated from the CV curves at a scan rate of 100 mV/s.
(77) A constant current charge-discharge test is performed on the supercapacitor electrode obtained by coating the reduced and sulfurized amorphous titanium dioxide powder on the nickel net, and the calculation result shows that the capacitance of the electrode is 211 F/g under a charge-discharge current of 1 A/g.
Example 4
(78) An amorphous titanium dioxide made by a titanium tetrachloride and nickel chloride co-precipitation method is used as the raw material, and an aluminum metal is used as the highly active reducing metal. The aluminum metal and the nickel-doped titanium dioxide are uniformly mixed together and placed in a sealed tube furnace, and the whole system is vacuumized to 0.1 Pa. Then the sample is heated to 500 C. After a reaction for 8 hours, the heating power is turned off, and the sample cools down. The sample is taken out after cooling down. To 1.5 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the reduced nickel-doped titanium dioxide. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The titanium dioxide slurry is uniformly coated on a nickel net by knife coating, then dried under vacuum at 100 C. for 8 h.
(79) The nickel-doped titanium dioxide powder made through co-precipitation is pale green, and turns deep dark green after reduction. The density of charge carrier of the nickel-doped reduced titanium dioxide is 9.3*10.sup.18 cm.sup.3.
(80) The capacitance of supercapacitor electrode obtained by coating the reduced and nickel-doped titanium dioxide powder on the nickel net significantly increases, which is 271 F/g, as calculated from the CV curves at a scan rate of 100 mV/s.
(81) A constant current charge-discharge test is performed on the supercapacitor electrode obtained by coating the reduced nickel-doped titanium dioxide powder on the nickel net, and the calculation result shows that the capacitance of the electrode is 326 F/g under a charge-discharge current of 1 A/g.
Example 5
(82) An amorphous titanium dioxide made by hydrolysis of titanium tetrachloride (same as that in Example 2) is used as the raw material. To 1.5 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the amorphous titanium dioxide powder. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The titanium dioxide slurry is uniformly coated on a nickel net by knife coating, then dried under vacuum at 100 C. for 8 h. An aluminum metal and the nickel net electrode coated with the amorphous titanium dioxide are uniformly mixed together and placed in a sealed tube furnace, and the whole system is vacuumized to 0.1 Pa. Then the sample is heated to 500 C. After a reaction for 8 hours, the heating power is turned off. Then, an ammonia gas is filled into the sealed system, and the nickel net electrode coated with the amorphous titanium dioxide is heated to 600 C. to be nitrided for 4 h. The electrode is taken out after cooling down. Two reduced and nitrided electrodes are assembled into a symmetric supercapacitor device, wherein the two pieces of the electrodes are separated by a diaphragm, and the electrolyte is a solution of tetraethyl ammonium tetrafluoroborate in acetonitrile.
(83) The pictures of the nickel net electrodes coated with amorphous titanium dioxide before and after reduction and nitriding are shown in
(84) The capacitance of the nickel net electrode coated with amorphous titanium dioxide increases significantly after the reduction and nitriding treatment, and is much larger than that of the electrode prepared by the method of Example 2. As shown in
(85) The capacitance of the nickel net electrode coated with amorphous titanium dioxide increases significantly after the reduction and nitriding treatment, and is much larger than that of the electrode prepared by the method of Example 2. As shown in
(86) The nickel net electrodes coated with amorphous titanium dioxide after reduction and nitriding are assembled into a symmetric device. As shown in
(87) The nickel net electrodes coated with amorphous titanium dioxide after reduction and nitriding are assembled into a symmetric device, which is submitted to a charge-discharge test under a current of 0.5 A/g. The test result is shown in
(88) A 5,000-cycle CV test is performed on the nickel net electrode coated with amorphous titanium dioxide after reduction and nitriding. As shown in
Example 6
(89) An amorphous titanium dioxide made by hydrolysis of titanium tetrachloride (same as that in Example 2) is used as the raw material. To 1.5 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the amorphous titanium dioxide powder. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The titanium dioxide slurry is uniformly coated on a nickel net by knife coating, then dried under vacuum at 100 C. for 8 h. An aluminum metal and the nickel net electrode coated with the amorphous titanium dioxide are uniformly mixed together and placed in a sealed tube furnace, and the whole system is vacuumized to 0.1 Pa. Then the sample is heated to 500 C. After a reaction for 8 hours, the heating power is turned off. Then, a hydrogen sulfide gas is filled into the sealed system, and the nickel net electrode coated with the amorphous titanium dioxide is heated to 600 C. to be sulfurized for 4 h. The electrode cools down then is taken out.
(90) The electrode turns deep yellow after reduction and sulfuration treatments.
(91) The capacitance of the nickel net electrode coated with amorphous titanium dioxide after reduction and sulfuration significantly increases, which is 174 F/g, as calculated from the CV curve at a scan rate of 100 mV/s.
(92) A constant current charge-discharge test is performed on the nickel net electrode coated with amorphous titanium dioxide after reduction and sulfuration, and the calculation result shows that the capacitance of the electrode is 259 F/g under a charge-discharge current of 1 A/g.
Example 7
(93) An amorphous titanium dioxide made by hydrolysis of titanium tetrachloride (same as that in Example 2) is used as the raw material. To 1.5 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the amorphous titanium dioxide powder. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The titanium dioxide slurry is uniformly coated on an FTO by knife coating, then dried under vacuum at 100 C. for 8 h. An aluminum metal and the FTO electrode coated with the amorphous titanium dioxide are uniformly mixed together and placed in a sealed tube furnace, and the whole system is vacuumized to 0.1 Pa. Then the sample is heated to 500 C. After a reaction for 8 hours, the heating power is turned off. Then, an ammonia gas is filled into the sealed system, and the FTO electrode coated with the amorphous titanium dioxide is heated to 600 C. to be nitrided for 4 h. The electrode cools down then is taken out.
(94) The FTO electrode coated with amorphous titanium dioxide is white before treatment, and turns dark after reduction and nitriding.
(95) The capacitance of the FTO electrode coated with amorphous titanium dioxide after reduction and nitriding significantly increases, which is 174 F/g, as calculated from the CV curve at a scan rate of 100 mV/s.
(96) A constant current charge-discharge test is performed on the FTO electrode coated with amorphous titanium dioxide after reduction and nitriding, and the calculation result shows that the capacitance of the electrode is 470 F/g under a charge-discharge current of 1 A/g.
Example 8
(97) An amorphous titanium dioxide made by hydrolysis of titanium tetrachloride (same as that in Example 2) is used as the raw material. To 1.5 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the amorphous titanium dioxide powder. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The titanium dioxide slurry is uniformly coated on a nickel net by knife coating, then dried under vacuum at 100 C. for 8 h. The nickel net electrode coated with the amorphous titanium dioxide is placed in a sealed tube furnace. The whole system is vacuumized to 0.1 Pa, and filled with hydrogen gas. The sample is heated to 500 C. After a reaction for 8 hours, the heating power is turned off and the electrode is taken out. Then, an ammonia gas is filled into the sealed system, and the nickel net electrode coated with the amorphous titanium dioxide is heated to 600 C. to be nitrided for 4 h. The electrode is taken out after cooling down.
(98) The electrode turns dark after hydrogen reduction and nitrogen doping.
(99) The capacitance of the nickel net electrode coated with amorphous titanium dioxide after hydrogenation reduction and nitriding significantly increases to 376 F/g, as calculated from the CV curve at a scan rate of 100 mV/s.
(100) A constant current charge-discharge test is performed on the nickel net electrode coated with amorphous titanium dioxide after reduction and sulfuration, and the calculation result shows that the capacitance of the electrode is 460 F/g under a charge-discharge current of 1 A/g.
Example 9
(101) An amorphous titanium dioxide made by hydrolysis of titanium tetrachloride (same as that in Example 2) is used as the raw material, and an aluminum metal is used as the highly active reducing metal. The aluminum metal and the titanium dioxide are placed in different heating sections in a dual-temperature-zone furnace, respectively, and the whole system is vacuumized to 0.1 Pa. Then the electrode sheet is heated to 500 C. and the aluminum powder is heated to 850 C. After a reaction for 8 hours, the heating power is turned off, and the sample cools down. An ammonia gas is filled into the sealed system, and the titanium dioxide is heated to 600 C. to be nitrided for 4 h. The sample is taken out after cooling down. To 3 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the reduced and nitrided black titanium dioxide powder, and 0.04 g of acetylene black. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The slurry is dried and milled to give a powder. The powder is tableted to give a free-standing titanium dioxide electrode.
(102) As shown in
(103) As shown in
(104) The free-standing electrodes are assembled into a symmetric device, which can stably extend the voltage window to 1.4 V at a scan rate of 2 mV/s as shown in
(105) The free-standing electrodes are assembled into a symmetric device, which is submitted to a charge-discharge test under a current of 0.5 A/g. The test result is shown in
Example 10
(106) An amorphous titanium dioxide made by hydrolysis of titanium tetrachloride (same as that in Example 2) is used as the raw material. To 3 mL solution of polyvinylidene fluoride in N-methyl-2-pyrrolidone (20 mg/mL) is added 0.4 g of the amorphous titanium dioxide powder and 0.04 g of acetylene black. The mixture is stirred for 8 h to give a uniformly dispersed titanium dioxide slurry. The slurry is dried and milled to give a powder. The powder is tableted to give a free-standing amorphous titanium dioxide electrode sheet. An aluminum metal as the highly active reducing metal and the amorphous titanium dioxide electrode sheet are placed in different heating sections in a dual-temperature-zone furnace, respectively, and the whole system is vacuumized to 0.1 Pa. Then the electrode sheet is heated to 500 C. and the aluminum powder is heated to 850 C. After a reaction for 8 hours, the heating power is turned off, and the sample cools down. An ammonia gas is filled into the sealed system, and the electrode sheet is heated to 600 C. to be nitrided for 4 h. The sample is taken out after cooling down to give a free-standing reduced and nitrided titanium dioxide electrode.
(107) The calculated capacitance of the supercapacitor electrode is 1,872 F/g at a scan rate of 2 mV/s.
(108) It is calculated from the charge-discharge curve under a charge-discharge current of 1 A/g that the capacitance of the supercapacitor electrode calculated is 1,740 F/g [93% capacitance retention after 10,000 cycles].
Example 11
(109) A titanium sheet is anodized to grow titanium nanotube arrays at the surface. Specifically, a copper is used as the cathode, a solution of glycol in water (volume ratio of ethylene glycol:water=97:3) containing 0.4 wt % NH.sub.4F is used as the electrolytic solution, and the titanium sheet is oxidized by application of a 100V DC power supply for 25 min, followed by application of an ultrasound to remove the nanotubes as formed, leaving bowl pits at the surface of the titanium sheet; then, the titanium sheet is oxidized by application of a 100V DC power supply for 25 min again, to give high-quality nanotubes. The resulting titanium sheet is dried and annealed at 500 C. for 8 h in an air atmosphere. Subsequently, the titanium sheet with titanium dioxide nanotubes grown therein as the raw material and an aluminum metal as the highly active reducing metal are placed in different heating sections in a dual-temperature-zone furnace, respectively, and the whole system is vacuumized to 0.1 Pa. Then the electrode sheet is heated to 500 C. and the aluminum powder is heated to 850 C. After a reaction for 8 hours, the heating power is turned off, and the sample is taken out after cooling down.
(110) A CV test is conducted at a scan rate of 100 mV/s. As shown in
(111) The charge-discharge curve of the supercapacitor electrode under a charge-discharge current of 0.5 mA/cm.sup.2 is shown in
(112) The capacitances of the supercapacitor electrode at various scan rates in a range of 5 mV/s200 mV/s are shown in
(113) A change in the capacitance of the supercapacitor electrode under a 2,000-cycle test is shown in
Example 12
(114) A titanium sheet electrode with titanium dioxide nanotubes grown therein as the raw material, and an aluminum metal as the highly active metal are placed in different heating sections in a dual-temperature-zone furnace, respectively, and the whole system is vacuumized to 0.1 Pa. Then the electrode sheet is heated to 500 C. and the aluminum powder is heated to 850 C. After a reaction for 8 hours, the heating power is turned off. After the sample cools down, an ammonia gas is filled into the sealed system, and the electrode sheet is heated to 600 C. to be nitrided for 4 h, then cools down and is taken out to give a reduced and nitrided electrode.
(115) The capacitance of electrode is 185 mF/cm.sup.2, as calculated from the CV curve at a scan rate of 5 mV/s.
(116) The capacitance of electrode is 336 mF/cm.sup.2, as calculated from the charge-discharge curve under a charge-discharge current of 0.5 mA/cm.sup.2.
Example 13
(117) A processing method which is the same as that of Example 2 is adopted, with a rutile titanium dioxide having a particle size of 1 micron being used as the raw material, to obtain a micron-sized nitrogen-doped titanium oxide, which has a capacitance of 103 F/g as calculated from the CV curve at a scan rate of 2 mV/s.
(118) The capacitance of the electrode is 112 F/g, as calculated from the charge-discharge curve under a charge-discharge current of 1 A/g [96% capacitance retention after 10,000 cycles].
Example 14
(119) A processing method which is the same as that of Example 2 is adopted, with an anatase titanium dioxide having a particle size of 2.3 micron being used as the raw material, to obtain a micron-sized nitrogen-doped titanium oxide, which has a capacitance of 55 F/g as calculated from the CV curve at a scan rate of 2 mV/s.
(120) The capacitance of electrode is 58 F/g, as calculated from the charge-discharge curve under a charge-discharge current of 1 A/g [97% capacitance retention after 10,000 cycles].
(121) The micron-sized nitrogen-doped titanium oxide is made into a symmetric device by means of a processing method which is the same as that of Example 9, which has a capacitance of 42 F/g [94% capacitance retention after 10,000 cycles].
Example 15
(122) A conductive nitrogen-doped titanium oxide (same as that in Example 2) is used as a synergist, and MnO.sub.2 active substances are added by an electrochemical deposition method, to obtain a nitrogen-doped titanium oxide/MnO.sub.2 composite electrode, which has a capacitance of 624 F/g as calculated from the CV curve at a scan rate of 2 mV/s, and 90% capacitance retention after 10,000 cycles.
Comparative Example 1
(123) MnO.sub.2 active substances are prepared on a current collector by means of an electrochemical deposition method (same as that in Example 15), to give a pure MnO.sub.2 electrode, which has a capacitance of 432 F/g as calculated from the CV curve at a scan rate of 2 mV/s, and 32% capacitance retention after 10,000 cycles.
Example 16
(124) A conductive nitrogen-doped titanium oxide (same as that in Example 2) is used as a synergist, and NiO active substances are added by a mechanical ball milling method, to obtain a nitrogen-doped titanium oxide/NiO composite electrode, which has a capacitance of 927 F/g as calculated from the CV curve at a scan rate of 2 mV/s, and 87% capacitance retention after 10,000 cycles.
Comparative Example 2
(125) NiO active substances (same as that in Example 2) are coated on a current collector to give a pure NiO electrode, which has a capacitance of 798 F/g as calculated from the CV curve at a scan rate of 2 mV/s, and 27% capacitance retention after 10,000 cycles.
Example 17
(126) A conductive nitrogen-doped titanium oxide (same as that in Example 2) is used as a synergist, and polyaniline active substances are added by an electrochemical deposition method, to obtain a nitrogen-doped titanium oxide/polyaniline composite electrode, which has a capacitance of 1,200 F/g as calculated from the CV curve at a scan rate of 2 mV/s, and 92% capacitance retention after 10,000 cycles.
Comparative Example 3
(127) Polyaniline active substances are prepared on a current collector by means of an electrochemical deposition method (same as that in Example 17), to give a pure polyaniline electrode, which has a capacitance of 967 F/g as calculated from the CV curve at a scan rate of 2 mV/s, and 17% capacitance retention after 10,000 cycles.
Example 18
(128) A conductive nitrogen-doped titanium oxide (same as that in Example 2) is used as a synergist, and activated carbon is added as the active substance by a mechanical ball milling method, to obtain a nitrogen-doped titanium oxide/activated carbon composite electrode, which has a capacitance of 312 F/g as calculated from the CV curve at a scan rate of 2 mV/s, and 98% capacitance retention after 10,000 cycles.
Comparative Example 4
(129) Activated carbon active substances (same as that in Example 18) are coated on a current collector to give a pure activated carbon electrode, which has a capacitance of 180 F/g as calculated from the CV curve at a scan rate of 2 mV/s, and 97% capacitance retention after 10,000 cycles.
INDUSTRIAL APPLICABILITY
(130) The present invention provides a supercapacitor electrode material with conductive titanium oxide as the active substance, and relates to a method which requires little equipment, has a short preparation period, is low in cost, and is capable of preparing a capacitor with good performance. As compared with conventional capacitors, the supercapacitor prepared herein has advantages of high energy density, high power density, and good cycle stability, and has broad prospective applications in areas of electric vehicles, energy storage, etc.