CN103855365B - Lithium-air battery positive pole uses the porous carbon materials of N doping - Google Patents
Lithium-air battery positive pole uses the porous carbon materials of N doping Download PDFInfo
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- CN103855365B CN103855365B CN201210496062.7A CN201210496062A CN103855365B CN 103855365 B CN103855365 B CN 103855365B CN 201210496062 A CN201210496062 A CN 201210496062A CN 103855365 B CN103855365 B CN 103855365B
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- 239000003575 carbonaceous material Substances 0.000 title claims abstract description 84
- 239000011148 porous material Substances 0.000 claims abstract description 66
- 238000000034 method Methods 0.000 claims abstract description 44
- 239000002149 hierarchical pore Substances 0.000 claims abstract description 16
- 230000008021 deposition Effects 0.000 claims abstract description 13
- 230000008569 process Effects 0.000 claims abstract description 12
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 claims description 48
- 230000004913 activation Effects 0.000 claims description 36
- 238000003980 solgel method Methods 0.000 claims description 30
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 28
- 239000007787 solid Substances 0.000 claims description 23
- 239000000843 powder Substances 0.000 claims description 22
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- 229910052751 metal Inorganic materials 0.000 claims description 15
- 239000002184 metal Substances 0.000 claims description 15
- 150000003839 salts Chemical class 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid group Chemical group C(CC(O)(C(=O)O)CC(=O)O)(=O)O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 12
- 238000005187 foaming Methods 0.000 claims description 11
- 239000004088 foaming agent Substances 0.000 claims description 11
- 230000003197 catalytic effect Effects 0.000 claims description 10
- 229910000000 metal hydroxide Inorganic materials 0.000 claims description 9
- 150000004692 metal hydroxides Chemical class 0.000 claims description 9
- 239000003513 alkali Substances 0.000 claims description 8
- 239000008367 deionised water Substances 0.000 claims description 8
- 229910021641 deionized water Inorganic materials 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 7
- 239000001099 ammonium carbonate Substances 0.000 claims description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 6
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 6
- 230000003213 activating effect Effects 0.000 claims description 6
- 239000007825 activation reagent Substances 0.000 claims description 6
- 239000003153 chemical reaction reagent Substances 0.000 claims description 6
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 claims description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 4
- 235000012538 ammonium bicarbonate Nutrition 0.000 claims description 4
- 229910052750 molybdenum Inorganic materials 0.000 claims description 4
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 4
- -1 sodium fatty alcohol Chemical class 0.000 claims description 4
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 claims description 3
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims description 3
- 150000001242 acetic acid derivatives Chemical class 0.000 claims description 3
- 235000012501 ammonium carbonate Nutrition 0.000 claims description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 3
- 235000010216 calcium carbonate Nutrition 0.000 claims description 3
- 235000015165 citric acid Nutrition 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 229910052748 manganese Inorganic materials 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- 239000011734 sodium Substances 0.000 claims description 3
- 229910052684 Cerium Inorganic materials 0.000 claims description 2
- 108010082495 Dietary Plant Proteins Proteins 0.000 claims description 2
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims description 2
- 125000005595 acetylacetonate group Chemical group 0.000 claims description 2
- CAMXVZOXBADHNJ-UHFFFAOYSA-N ammonium nitrite Chemical compound [NH4+].[O-]N=O CAMXVZOXBADHNJ-UHFFFAOYSA-N 0.000 claims description 2
- 150000004649 carbonic acid derivatives Chemical class 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 229910052804 chromium Inorganic materials 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 229910052737 gold Inorganic materials 0.000 claims description 2
- 150000004820 halides Chemical class 0.000 claims description 2
- 229910052741 iridium Inorganic materials 0.000 claims description 2
- 229910052746 lanthanum Inorganic materials 0.000 claims description 2
- 150000002678 macrocyclic compounds Chemical class 0.000 claims description 2
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 claims description 2
- 239000001095 magnesium carbonate Substances 0.000 claims description 2
- 229910000021 magnesium carbonate Inorganic materials 0.000 claims description 2
- 235000014380 magnesium carbonate Nutrition 0.000 claims description 2
- 229910052763 palladium Inorganic materials 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 claims description 2
- 229910052697 platinum Inorganic materials 0.000 claims description 2
- 229940051841 polyoxyethylene ether Drugs 0.000 claims description 2
- 229920000056 polyoxyethylene ether Polymers 0.000 claims description 2
- 229910052703 rhodium Inorganic materials 0.000 claims description 2
- 229910052709 silver Inorganic materials 0.000 claims description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 2
- 235000017550 sodium carbonate Nutrition 0.000 claims description 2
- 235000019333 sodium laurylsulphate Nutrition 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 150000003467 sulfuric acid derivatives Chemical class 0.000 claims description 2
- 229910052718 tin Inorganic materials 0.000 claims description 2
- 229910052719 titanium Inorganic materials 0.000 claims description 2
- 229910052721 tungsten Inorganic materials 0.000 claims description 2
- 229910052720 vanadium Inorganic materials 0.000 claims description 2
- 229910052727 yttrium Inorganic materials 0.000 claims description 2
- 229910052725 zinc Inorganic materials 0.000 claims description 2
- 229910052726 zirconium Inorganic materials 0.000 claims description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 9
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims 5
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical group O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims 2
- 229910017604 nitric acid Inorganic materials 0.000 claims 2
- 239000004604 Blowing Agent Substances 0.000 claims 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims 1
- 125000004432 carbon atom Chemical group C* 0.000 claims 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims 1
- 150000004032 porphyrins Chemical class 0.000 claims 1
- 229910052708 sodium Inorganic materials 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 11
- 238000002360 preparation method Methods 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 8
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 8
- 229910052799 carbon Inorganic materials 0.000 abstract description 6
- 238000007599 discharging Methods 0.000 abstract 1
- 239000007772 electrode material Substances 0.000 abstract 1
- 208000028659 discharge Diseases 0.000 description 20
- 239000000243 solution Substances 0.000 description 20
- 238000001291 vacuum drying Methods 0.000 description 12
- 230000032683 aging Effects 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 239000003792 electrolyte Substances 0.000 description 4
- 229910001947 lithium oxide Inorganic materials 0.000 description 4
- 239000007774 positive electrode material Substances 0.000 description 4
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 229910052744 lithium Inorganic materials 0.000 description 3
- FUJCRWPEOMXPAD-UHFFFAOYSA-N lithium oxide Chemical compound [Li+].[Li+].[O-2] FUJCRWPEOMXPAD-UHFFFAOYSA-N 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000006722 reduction reaction Methods 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000003487 electrochemical reaction Methods 0.000 description 2
- 238000003411 electrode reaction Methods 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000004088 simulation Methods 0.000 description 2
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- 229920000557 Nafion® Polymers 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 230000010757 Reduction Activity Effects 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- QGUAJWGNOXCYJF-UHFFFAOYSA-N cobalt dinitrate hexahydrate Chemical compound O.O.O.O.O.O.[Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O QGUAJWGNOXCYJF-UHFFFAOYSA-N 0.000 description 1
- 229910000428 cobalt oxide Inorganic materials 0.000 description 1
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical compound [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000012983 electrochemical energy storage Methods 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910021389 graphene Inorganic materials 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011244 liquid electrolyte Substances 0.000 description 1
- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 229910001960 metal nitrate Inorganic materials 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 239000007773 negative electrode material Substances 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- AOPCKOPZYFFEDA-UHFFFAOYSA-N nickel(2+);dinitrate;hexahydrate Chemical compound O.O.O.O.O.O.[Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O AOPCKOPZYFFEDA-UHFFFAOYSA-N 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 125000004433 nitrogen atom Chemical group N* 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- IEQIEDJGQAUEQZ-UHFFFAOYSA-N phthalocyanine Chemical class N1C(N=C2C3=CC=CC=C3C(N=C3C4=CC=CC=C4C(=N4)N3)=N2)=C(C=CC=C2)C2=C1N=C1C2=CC=CC=C2C4=N1 IEQIEDJGQAUEQZ-UHFFFAOYSA-N 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000013341 scale-up Methods 0.000 description 1
- 238000004626 scanning electron microscopy Methods 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8605—Porous electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8605—Porous electrodes
- H01M4/861—Porous electrodes with a gradient in the porosity
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/96—Carbon-based electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M12/00—Hybrid cells; Manufacture thereof
- H01M12/08—Hybrid cells; Manufacture thereof composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M2004/8678—Inert electrodes with catalytic activity, e.g. for fuel cells characterised by the polarity
- H01M2004/8689—Positive electrodes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
本发明涉及锂-空气电池正极用氮掺杂的多孔碳材料,其特征在于:所述氮掺杂的多孔碳材料具有相互贯通的分级孔结构,N均匀地掺杂于C骨架中,其中N占碳材料原子比0.2-15%,分级孔包括传质孔和沉积孔,沉积孔占总孔孔体积的40~95%,传质孔占总孔孔体积的4~55%;将该碳材料用作锂-空气电池电极材料,可最大限度地提高碳材料在充放电过程中的空间利用率,有效提高锂-空气电池的能量密度及功率密度。本发明的优点是:制备工艺简单,材料来源广泛,分级孔碳材料孔结构可调控且调控方式多样,掺氮方式易于实现。The invention relates to a nitrogen-doped porous carbon material for the positive electrode of a lithium-air battery, which is characterized in that: the nitrogen-doped porous carbon material has a hierarchical pore structure interpenetrating, and N is uniformly doped in the C skeleton, wherein N It accounts for 0.2-15% of the atomic ratio of carbon materials. The graded pores include mass transfer pores and deposition pores. The deposition pores account for 40-95% of the total pore volume, and the mass transfer pores account for 4-55% of the total pore volume; the carbon The material is used as an electrode material for lithium-air batteries, which can maximize the space utilization of carbon materials in the process of charging and discharging, and effectively improve the energy density and power density of lithium-air batteries. The invention has the advantages of simple preparation process, wide source of materials, controllable pore structure of the hierarchical pore carbon material in various control modes, and easy realization of nitrogen doping mode.
Description
技术领域technical field
本发明属于储能电池领域,具体涉及一种碳材料,其碳材料掺杂氮,且具有分级孔分布,应用于锂-空气电池正极,具有高的能量密度及功率密度。The invention belongs to the field of energy storage batteries, and in particular relates to a carbon material doped with nitrogen and having hierarchical pore distribution, which is applied to the positive electrode of a lithium-air battery and has high energy density and power density.
背景技术Background technique
电动车和移动电子设备的飞速发展迫切需要开发更高能量密度的电池。目前锂离子电池的实验室比能量虽已达到250Wh/kg,但受正极材料比容量进一步提高的限制,其比能量很难再有较大提高,而且靠提高充电电压以增高比能量的途径将加剧安全问题,因而发展新的电化学储能体系势在必行。在新的储能体系中,锂-空气电池是一种以金属锂为负极,空气电极为正极的二次电池。作为负极材料的金属锂具有最低的理论电压,其理论比容量高达3,862mAh/g,而作为正极活性物质的氧气可直接从空气中获得,因此,锂-空气电池具有极高的比容量及比能量。以锂为标准,其理论比能量密度可达11,140Wh/Kg,在民用及军用领域极具应用前景。The rapid development of electric vehicles and mobile electronic devices urgently requires the development of batteries with higher energy density. At present, although the laboratory specific energy of lithium-ion batteries has reached 250Wh/kg, it is difficult to increase the specific energy due to the limitation of the further improvement of the specific capacity of the positive electrode material, and the way to increase the specific energy by increasing the charging voltage will be Aggravating the safety problem, it is imperative to develop a new electrochemical energy storage system. In the new energy storage system, the lithium-air battery is a secondary battery with metal lithium as the negative electrode and the air electrode as the positive electrode. Metal lithium as the negative electrode material has the lowest theoretical voltage, and its theoretical specific capacity is as high as 3,862mAh/g, while oxygen as the positive electrode active material can be obtained directly from the air. Therefore, lithium-air batteries have extremely high specific capacity and specific capacity. energy. Taking lithium as the standard, its theoretical specific energy density can reach 11,140Wh/Kg, which has great application prospects in civil and military fields.
目前,锂-空气电池主要采用各种碳材料作为正极材料,通过混入PTFE,PVDF,Nafion等粘结剂制备空气电极。如图1所示,为锂-空气电池正极放电反应过程模拟图。放电反应在液体电解质溶液与碳材料之间构建的固液两相界面上进行,碳材料表面生成固体不溶产物-锂氧化物,随着反应进行,固体产物积累使内部孔道堵塞继而造成放电终止。At present, lithium-air batteries mainly use various carbon materials as positive electrode materials, and prepare air electrodes by mixing PTFE, PVDF, Nafion and other binders. As shown in Figure 1, it is a simulation diagram of the discharge reaction process of the positive electrode of the lithium-air battery. The discharge reaction proceeds on the solid-liquid two-phase interface between the liquid electrolyte solution and the carbon material. The surface of the carbon material generates a solid insoluble product-lithium oxide. As the reaction progresses, the solid product accumulates to block the internal pores and cause the discharge to terminate.
作为电化学反应发生的场所,碳材料孔结构物性参数如:比表面积、孔容、孔径分布对电池性能,尤其是充放电容量具有重要的影响。Tran等研究表明电极的容量由不会影响物质传输的大尺寸孔道内锂氧化物的量所决定。碳材料微孔孔道与部分中孔孔道会被放电起始阶段所形成的锂氧化物堵塞,这部分孔的表面将无法再次通过空气与电解液,因此不再参与电化学反应,造成放电终止。然而,完全由大孔尺寸构成的碳材料在放电过程中,由于锂氧化物导电性差,放电产物在孔壁上的堆积厚度有限,大孔的中心部分得不到利用,也不能充分发挥孔的利用空间。因此如何构造合适孔结构的碳材料,使其利于电解液与空气在多孔结构内的传输,从而加快电极反应速率以及增加孔的有效利用,是目前亟待解决的难题。As the place where the electrochemical reaction occurs, the physical parameters of the carbon material pore structure, such as specific surface area, pore volume, and pore size distribution, have an important impact on battery performance, especially the charge and discharge capacity. Tran et al. showed that the capacity of the electrode is determined by the amount of lithium oxide in the large-sized pores that do not affect the material transport. The micropores and some mesopores of carbon materials will be blocked by the lithium oxide formed at the initial stage of discharge, and the surface of these pores will not be able to pass through air and electrolyte again, so they will no longer participate in the electrochemical reaction, resulting in the termination of discharge. However, during the discharge process of carbon materials composed entirely of macropore sizes, due to the poor conductivity of lithium oxide, the accumulation thickness of discharge products on the pore walls is limited, the central part of the macropores cannot be utilized, and the pores cannot be fully utilized. Use the space. Therefore, how to construct a carbon material with a suitable pore structure to facilitate the transmission of electrolyte and air in the porous structure, thereby accelerating the electrode reaction rate and increasing the effective use of pores is an urgent problem to be solved.
另外,氮掺杂的碳材料在燃料电池中已表现出优异的氧还原活性,可部分替代贵金属Pt/C催化剂。研究显示掺杂氮原子改变了纳米碳材料的微观结构和表面电子态,通过N-O或者C-O“双址(dualsite)吸附”,可削弱氧分子中的O-O键,利于发生还原反应。In addition, nitrogen-doped carbon materials have shown excellent oxygen reduction activity in fuel cells and can partially replace noble metal Pt/C catalysts. Studies have shown that doping nitrogen atoms changes the microstructure and surface electronic state of carbon nanomaterials. Through N-O or C-O "dual site (dualsite) adsorption", it can weaken the O-O bond in oxygen molecules, which is conducive to the reduction reaction.
目前有关氮掺杂的碳纳米管、氮掺杂的石墨烯材料在锂-空气电池中的应用有少量报道,结果显示氮掺杂可造成碳边缘缺陷,有效地增加这部分活性位暴露,以促进氧还原反应,有效提高锂-空气电池的放电容量及放电电压。但上述材料由于其制备方法复杂,成本较高,且实验条件要求较高,不利于大规模商业化制备应用,仍不能满足锂空气电池对材料的要求。At present, there are a few reports on the application of nitrogen-doped carbon nanotubes and nitrogen-doped graphene materials in lithium-air batteries. The results show that nitrogen doping can cause carbon edge defects, effectively increasing the exposure of this part of the active site, and Promote the oxygen reduction reaction and effectively improve the discharge capacity and discharge voltage of the lithium-air battery. However, the above-mentioned materials are not conducive to large-scale commercial preparation and application due to their complicated preparation methods, high cost, and high experimental conditions, and still cannot meet the material requirements of lithium-air batteries.
发明内容Contents of the invention
本发明的目的在于提供一种锂-空气电池用电极碳材料及其制备方法。The object of the present invention is to provide an electrode carbon material for a lithium-air battery and a preparation method thereof.
为实现上述目的,本发明采用的技术方案如下,In order to achieve the above object, the technical scheme adopted in the present invention is as follows,
锂-空气电池正极用氮掺杂的多孔碳材料,所述氮掺杂的多孔碳材料具有相互贯通的分级孔结构,N均匀地掺杂于C骨架中,其中N占碳材料原子比0.2-15%,分级孔包括传质孔和沉积孔,沉积孔占总孔孔体积的40~95%,传质孔占总孔孔体积的4~55%,其余为孔径小于5nm的孔,沉积孔孔径为5~90nm,传质孔孔径为0.1~6um,传质孔间相互间距为0.1~8um,传质孔通过沉积孔相互连通,碳材料总孔容为0.5~5cm3/g。A nitrogen-doped porous carbon material for the positive electrode of a lithium-air battery, the nitrogen-doped porous carbon material has a hierarchical pore structure interpenetrating, N is uniformly doped in the C skeleton, and the atomic ratio of N to the carbon material is 0.2- 15%, graded pores include mass transfer pores and deposition pores, deposition pores account for 40-95% of the total pore volume, mass transfer pores account for 4-55% of the total pore volume, and the rest are pores with a diameter less than 5nm, deposition pores The pore diameter is 5~90nm, the mass transfer hole diameter is 0.1~6um, the distance between the mass transfer holes is 0.1~8um, the mass transfer holes are connected to each other through the deposition holes, and the total pore volume of the carbon material is 0.5~5cm 3 /g.
所述碳材料采用溶胶凝胶法结合活化法或溶胶凝胶法结合发泡法制备而成。The carbon material is prepared by a sol-gel method combined with an activation method or a sol-gel method combined with a foaming method.
优选溶胶凝胶法结合活化法。The sol-gel method combined with the activation method is preferred.
具体制备方法如下:The specific preparation method is as follows:
A溶胶凝胶法结合活化法A sol-gel method combined with activation method
所述溶胶凝胶法结合活化法包括在碳化过程中催化活化,或对溶胶凝胶法制得的碳材料进行后活化,二者中的一种或二种结合使用。The sol-gel method combined with the activation method includes catalytic activation during the carbonization process, or post-activation of the carbon material prepared by the sol-gel method, one or both of which are used in combination.
优选溶胶凝胶法碳化过程中催化活化和后活化中的NH3热处理活化法。The catalytic activation in the sol-gel carbonization process and the NH3 heat treatment activation method in the post-activation are preferred.
所述溶胶凝胶法在碳化过程中催化活化按如下过程制备而成,将间苯二酚分散于溶剂中,然后添加金属盐或金属氢氧化物继续溶解分散,然后滴加甲醛溶液,30~80℃下搅拌混合均匀直至反应形成凝胶;将凝胶60~100℃下真空干燥老化3~10天处理,取出后粉碎研磨,得到固体粉末;经高温NH3气氛下碳化后用酸或碱除去金属盐或金属氢氧化物,经过滤、干燥,即得多孔碳材料,其中NH3进气流量控制在2~100ml/min。The sol-gel method is prepared by catalytic activation in the carbonization process as follows: disperse resorcinol in a solvent, then add metal salt or metal hydroxide to continue dissolving and dispersing, then add formaldehyde solution dropwise, 30~ Stir and mix evenly at 80°C until the reaction forms a gel; vacuum dry and age the gel at 60-100°C for 3-10 days, take it out and grind it to obtain a solid powder; Remove metal salts or metal hydroxides, filter and dry to obtain porous carbon materials, in which the NH 3 intake flow rate is controlled at 2~100ml/min.
所述金属盐或金属氢氧化物为含Fe、Co、Ni、Cu、Ag、Pt、Pd、Au、Ir、Ru、Nb、Y、Rh、Cr、Zr、Ce、Ti、Mo、Mn、Zn、W、Sn、La及V的一种或二种以上金属盐或金属氢氧化物;金属盐为金属的硝酸盐、碳酸盐、硫酸盐、醋酸盐、卤化物、二亚硝基二胺盐、乙酰丙酮化物、或大环络合物及卟啉化物、酞箐化物中的一种或二种以上。优选Fe、Co、Ni、Cu、Mo、Mn、Mo的硝酸盐、醋酸盐。The metal salt or metal hydroxide contains Fe, Co, Ni, Cu, Ag, Pt, Pd, Au, Ir, Ru, Nb, Y, Rh, Cr, Zr, Ce, Ti, Mo, Mn, Zn , W, Sn, La and V of one or more metal salts or metal hydroxides; metal salts are metal nitrates, carbonates, sulfates, acetates, halides, dinitroso di One or more of amine salts, acetylacetonates, or macrocyclic complexes, porphyrin compounds, and phthalocyanine compounds. Nitrates and acetates of Fe, Co, Ni, Cu, Mo, Mn, and Mo are preferred.
所述溶胶凝胶法制得的碳材料进行后活化,包括以下一种或两种以上方法结合制备而成:The carbon material prepared by the sol-gel method is post-activated, including one or more of the following methods:
(1)物理活化法:将间苯二酚分散于溶剂中,然后滴加甲醛溶液,30~80℃下搅拌混合均匀直至反应形成凝胶;将凝胶60~100℃下真空干燥老化3~10天处理,取出后粉碎研磨,得到固体粉末;经高温NH3气氛下碳化后,通入水蒸气、CO2、及可产生上述两种气体之一的化合物中的一种或几种进行活化;活化温度控制在400~1300℃,活化时间控制在10min~5h,NH3、水蒸气或CO2进气流量控制在2~100ml/min;(1) Physical activation method: disperse resorcinol in a solvent, then add formaldehyde solution dropwise, stir and mix evenly at 30~80°C until the reaction forms a gel; vacuum dry and age the gel at 60~100°C for 3~ After 10 days of treatment, take it out, crush and grind it to obtain solid powder; after carbonization under high-temperature NH 3 atmosphere, pass in water vapor, CO 2 , and one or more of the compounds that can generate one of the above two gases to activate; The activation temperature is controlled at 400~1300°C, the activation time is controlled at 10min~5h, and the intake flow of NH 3 , water vapor or CO 2 is controlled at 2~100ml/min;
(2)NH3热处理活化法:将间苯二酚分散于溶剂中,然后滴加甲醛溶液,30~80℃下搅拌混合均匀直至反应形成凝胶;将凝胶60~100℃下真空干燥老化3~10天处理,取出后粉碎研磨,得到固体粉末;经高温N2或Ar碳化后,得到的碳材料在NH3气氛下进行热处理活化。热处理温度控制在400~1300℃,时间控制在10min~6h,N2或Ar、NH3进气流量控制在2~100ml/min;(2) NH 3 heat treatment activation method: disperse resorcinol in the solvent, then add formaldehyde solution dropwise, stir and mix evenly at 30~80°C until the reaction forms a gel; vacuum dry and age the gel at 60~100°C After 3-10 days of treatment, take it out, crush and grind it to obtain solid powder; after carbonization by high temperature N 2 or Ar, the obtained carbon material is activated by heat treatment in NH 3 atmosphere. The heat treatment temperature is controlled at 400~1300°C, the time is controlled at 10min~6h, and the intake flow of N2 or Ar, NH3 is controlled at 2~100ml/min;
(3)化学活化法:将间苯二酚分散于溶剂中,然后滴加甲醛溶液,30~80℃下搅拌混合均匀直至反应形成凝胶;将凝胶60~100℃下真空干燥老化3~10天处理,取出后粉碎研磨,得到固体粉末;经高温NH3气氛下碳化后,将活化试剂与溶胶凝胶法制备的碳材料研磨混合均匀,活化试剂为碳材料质量的10~300%,活化温度控制在300~900℃,活化时间控制在10min~5h;活化后碳材料用去离子水洗涤并干燥;其中NH3进气流量控制在2~100ml/min;所述的活化试剂包括碱类活化试剂KOH,酸类活化试剂H3PO4,盐类活化试剂为ZnCl2、K2CO3或Na2CO3。(3) Chemical activation method: disperse resorcinol in a solvent, then add formaldehyde solution dropwise, stir and mix evenly at 30~80°C until the reaction forms a gel; vacuum dry and age the gel at 60~100°C for 3~ After 10 days of treatment, take it out, crush and grind to obtain solid powder; after carbonization under high-temperature NH3 atmosphere, grind and mix the activation reagent and the carbon material prepared by the sol-gel method evenly. The activation reagent is 10-300% of the mass of the carbon material. The activation temperature is controlled at 300-900°C, and the activation time is controlled at 10min-5h; after activation, the carbon material is washed with deionized water and dried; the NH 3 intake flow is controlled at 2-100ml/min; the activation reagent includes alkali The activating reagent KOH, the acid activating reagent H 3 PO 4 , and the salt activating reagent are ZnCl 2 , K 2 CO 3 or Na 2 CO 3 .
B溶胶凝胶法结合发泡法B sol-gel method combined with foaming method
所述碳材料采用溶胶凝胶法结合发泡法按如下过程制备而成:将间苯二酚和发泡剂分散于溶剂中,然后滴加甲醛溶液,30~80℃下搅拌混合均匀直至反应形成凝胶;将凝胶60~100℃下真空干燥老化3~10天处理,取出后粉碎研磨,得到固体粉末;经高温NH3气氛下碳化后,用酸或碱除去发泡剂,经过滤、干燥,即得多孔碳材料;其中NH3进气流量控制在2~100ml/min。The carbon material is prepared by the sol-gel method combined with the foaming method as follows: disperse resorcinol and foaming agent in a solvent, then add formaldehyde solution dropwise, stir and mix evenly at 30-80°C until the reaction Form a gel; vacuum dry and age the gel at 60-100°C for 3-10 days, take it out, crush and grind it to obtain a solid powder; after carbonization in a high-temperature NH 3 atmosphere, remove the foaming agent with acid or alkali, and filter , drying, that is, porous carbon materials; wherein the NH 3 intake flow is controlled at 2~100ml/min.
所述发泡剂为柠檬酸、碳酸钙、碳酸镁、碳酸氢钠、碳酸钠、碳酸铵、碳酸氢胺、亚硝酸铵、十二烷基硫酸钠、十六烷基三甲基溴化铵、脂肪醇聚氧乙烯醚硫酸钠、正戊烷、正己烷、正庚烷、石油醚、动植物蛋白类发泡剂的一种或两种以上发泡剂。优选柠檬酸、碳酸铵、碳酸氢铵、碳酸氢钠、碳酸钙。The whipping agent is citric acid, calcium carbonate, magnesium carbonate, sodium bicarbonate, sodium carbonate, ammonium carbonate, ammonium bicarbonate, ammonium nitrite, sodium lauryl sulfate, cetyltrimethylammonium bromide , one or more foaming agents of fatty alcohol polyoxyethylene ether sodium sulfate, n-pentane, n-hexane, n-heptane, petroleum ether, animal and vegetable protein foaming agents. Citric acid, ammonium carbonate, ammonium bicarbonate, sodium bicarbonate, calcium carbonate are preferred.
本发明有益效果:Beneficial effects of the present invention:
1.碳材料制备过程中即构造掺杂氮的分级孔结构,分别用于放电产物的沉积及氧、电解液的传质,将该碳材料用作锂-空气电池电极,可最大限度地提高碳材料孔的利用率,另外,氮的引入使碳边缘造成缺陷,引入更多氧还原反应的活性位。综合考虑,此新型碳材料,大大提高电极的空间利用率,使各孔径尺寸的孔各司其职,同时掺杂氮具有催化活性,有效提高电池的放电比容量、电压平台及倍率放电能力,提高电池的能量密度及功率密度。1. During the preparation of carbon materials, a hierarchical pore structure doped with nitrogen is constructed, which are used for the deposition of discharge products and the mass transfer of oxygen and electrolyte. The carbon materials can be used as lithium-air battery electrodes to maximize the In addition, the introduction of nitrogen causes defects on the carbon edge and introduces more active sites for oxygen reduction reactions. Considering comprehensively, this new type of carbon material can greatly improve the space utilization of the electrode, so that the pores of each pore size can perform their duties. At the same time, nitrogen doping has catalytic activity, which can effectively improve the discharge specific capacity, voltage platform and rate discharge capacity of the battery. Improve the energy density and power density of the battery.
2.氮掺杂的分级孔碳材料制备方法简单易行,原材料来源广泛且价格低廉,制备过程较温和环保、无强酸强碱,且易于放大实现产品的大批量制备,满足锂空气电池对正极材料的要求,推进锂空气电池的商业化应用。2. The preparation method of nitrogen-doped hierarchical pore carbon material is simple and easy, the source of raw materials is wide and the price is low, the preparation process is mild and environmentally friendly, there is no strong acid and strong alkali, and it is easy to scale up to realize the mass preparation of the product, which meets the requirements of lithium-air batteries for positive electrodes. Material requirements to promote the commercial application of lithium-air batteries.
3.氮掺杂的分级孔碳材料孔结构可调控且调控方式多样;掺N方式多样且易于实现。在碳载体表面导入或产生含N结构使用方法有:原位掺杂N,包括在NH3气氛下碳化;以及后掺N,如多孔碳材料碳化后在NH3中热处理。3. The pore structure of nitrogen-doped hierarchical pore carbon materials can be adjusted and adjusted in various ways; the ways of N doping are diverse and easy to realize. The methods of introducing or generating N-containing structures on the surface of the carbon support include: in-situ doping of N, including carbonization under NH 3 atmosphere; and post-doping of N, such as heat treatment in NH 3 after carbonization of porous carbon materials.
4.氮掺杂的分级孔碳材料孔结构可调控,从微米到纳米范围且调控范围广且方式多样;4. The pore structure of nitrogen-doped hierarchically porous carbon materials can be adjusted, ranging from micron to nanometer, in a wide range and in various ways;
5.溶胶凝胶法结合活化法的优点是:利用溶胶凝胶法形成的三维网络结构,可形成导电性能优异且具有微孔和较小介孔的碳材料,且通过活化的方式,可对网络结构的孔进一步扩孔,形成较大孔径的孔,最终形成介孔到大孔范围的分级孔结构的含N碳材料,满足电池放电过程需要。其中催化活化方法制备过程中可易于同时实现金属/金属氧化物的掺杂,应用于锂空气电池可对充放电过程起到催化作用,降低充放电极化,提高电池能量效率。5. The advantages of the sol-gel method combined with the activation method are: using the three-dimensional network structure formed by the sol-gel method, carbon materials with excellent electrical conductivity and micropores and small mesoporous properties can be formed, and the network structure can be modified by activation. The pores are further expanded to form pores with larger pore diameters, and finally form a N-containing carbon material with a hierarchical pore structure ranging from mesopores to macropores, which meets the needs of the battery discharge process. Among them, the catalytic activation method can easily realize the doping of metal/metal oxide at the same time during the preparation process, and it can play a catalytic role in the charge and discharge process when applied to lithium-air batteries, reduce charge and discharge polarization, and improve battery energy efficiency.
6.溶胶凝胶法结合发泡法的优点是:利用溶胶凝胶法形成的三维网络结构,可形成导电性能优异且具有微孔和较小介孔的碳材料,且通过加入发泡剂方式,可发泡形成较大孔径的孔,且加入的发泡剂在碳化过程中分解,不需要酸洗或碱洗处理。最终形成介孔到大孔范围的分级孔结构的含N碳材料,满足电池放电过程需要。6. The advantages of the sol-gel method combined with the foaming method are: the three-dimensional network structure formed by the sol-gel method can be used to form a carbon material with excellent electrical conductivity and micropores and small mesopores, and by adding a foaming agent, it can be Foaming forms pores with a larger pore size, and the added foaming agent decomposes during the carbonization process, and does not require pickling or alkali cleaning. Finally, a N-containing carbon material with a hierarchical pore structure ranging from mesopores to macropores is formed to meet the needs of the battery discharge process.
附图说明Description of drawings
图1为电极反应过程模拟图;Fig. 1 is the simulation diagram of electrode reaction process;
图2为实施例1采用以溶胶凝胶法结合催化活化法制备的分级多孔碳材料与商业化碳粉材料表面形貌的对比,A为掺杂N的分级多孔碳材料(HPC-N),B为商业化KB600碳粉。Fig. 2 is the comparison of the surface morphology of the hierarchical porous carbon material prepared by the sol-gel method combined with the catalytic activation method and the commercial carbon powder material in Example 1, A is the hierarchical porous carbon material (HPC-N) doped with N, B is commercialized KB600 toner.
具体实施方式detailed description
实施例1Example 1
采用溶胶凝胶法结合催化活化法制备氮掺杂的分级孔结构多孔碳材料。将6.16g间苯二酚溶于10mL去离子水,形成透明溶液;取0.29g六水合硝酸镍添加到上述透明溶液中,混合溶解均匀得到溶液;向上述搅拌中的溶液中滴加9.08g甲醛溶液,进一步搅拌混合均匀,在20℃环境中持续搅拌,直至反应形成凝胶;将凝胶转移至真空干燥箱在70℃下真空干燥老化处理7d,取出后粉碎研磨,得到固体粉末;将固体粉末在NH3中900℃碳化处理3h,用适量1MHCl洗除氧化镍,过滤干燥,即得所述碳材料。Nitrogen-doped porous carbon materials with hierarchical pore structure were prepared by sol-gel method combined with catalytic activation method. Dissolve 6.16g of resorcinol in 10mL of deionized water to form a transparent solution; add 0.29g of nickel nitrate hexahydrate to the above transparent solution, mix and dissolve evenly to obtain a solution; add dropwise 9.08g of formaldehyde to the above stirring solution The solution was further stirred and mixed evenly, and continuously stirred in an environment of 20°C until the reaction formed a gel; the gel was transferred to a vacuum drying oven for 7 days of vacuum drying and aging treatment at 70°C, and then crushed and ground to obtain a solid powder; the solid The powder was carbonized in NH 3 at 900°C for 3 hours, washed with an appropriate amount of 1M HCl to remove nickel oxide, filtered and dried to obtain the carbon material.
实施例1所制备的正极材料结构具有大量的10~40纳米孔径沉积孔,具有0.1~0.5微米级传质孔的分级孔,传质孔间相互间距为1um左右,传质孔贯通于沉积孔;碳材料呈蜂窝状网络孔结构(扫描电镜结果图2显示)。另外BET结果表明,所制备的碳材料在20nm左右有集中的孔分布,碳材料的总孔容为0.9cm3/g,沉积孔占总孔孔体积的85%。其中HPC-N中经X射线光电子能谱分析,氮占碳材料原子比为1.8%。The positive electrode material structure prepared in Example 1 has a large number of deposition pores with a diameter of 10 to 40 nanometers, and graded pores with mass transfer pores of 0.1 to 0.5 microns. The distance between the mass transfer pores is about 1 μm, and the mass transfer pores penetrate the deposition pores. ; The carbon material has a honeycomb network pore structure (Scanning electron microscopy results shown in Figure 2). In addition, the BET results show that the prepared carbon material has a concentrated pore distribution around 20nm, the total pore volume of the carbon material is 0.9cm 3 /g, and the deposited pores account for 85% of the total pore volume. Among them, the X-ray photoelectron spectroscopy analysis in HPC-N shows that nitrogen accounts for 1.8% of the carbon material atomic ratio.
实施例1所制备的掺杂N的分级多孔碳材料用作锂空气电池正极,其电极担量为3mg/cm2 carbon,在三氟甲基磺酰亚胺锂电解质盐和四甘醇二甲醚溶剂构成的电解液下,室温以0.1mA/cm2电流密度下,1atm下99.99%纯度的O2条件下测试,首圈放电容量达6500mAh/g。The N-doped hierarchical porous carbon material prepared in Example 1 is used as the positive electrode of a lithium-air battery, and its electrode load is 3 mg/cm 2 carbon . In the electrolyte composed of ether solvent, tested under the condition of 0.1mA/cm 2 current density at room temperature and 99.99% purity O 2 at 1 atm, the first cycle discharge capacity reached 6500mAh/g.
对比例:Comparative example:
采用商业化KB-600碳粉作为锂空气电池正极,相同条件下,其首圈放电容量仅为3000mAh/g,实施例1所制备的掺杂N的分级多孔碳材料容量较商业化碳粉KB-600提高了116%,且放电电压平台提高。Commercialized KB-600 carbon powder is used as the positive electrode of lithium-air battery. Under the same conditions, its first-cycle discharge capacity is only 3000mAh/g. The capacity of the hierarchical porous carbon material doped with N prepared in Example 1 is higher than that of commercial carbon powder KB -600 has been increased by 116%, and the discharge voltage platform has been increased.
实施例2Example 2
采用溶胶凝胶法结合活化法制备氮掺杂的分级孔结构多孔碳材料。将6.16g间苯二酚溶于10mL去离子水,形成透明溶液;取0.808g硝酸铁添加到上述透明溶液中,混合溶解均匀得到溶液;向上述搅拌中的溶液中滴加9.08g甲醛溶液,进一步搅拌混合均匀,在20℃环境中持续搅拌,直至反应形成凝胶;将凝胶转移至真空干燥箱在70℃下真空干燥老化处理3d,取出后粉碎研磨,得到固体粉末;将固体粉末在NH3中1000℃碳化处理5h,用适量1MHCl洗除氧化铁,过滤干燥,即得所述碳材料。Nitrogen-doped porous carbon materials with hierarchical pore structure were prepared by sol-gel method combined with activation method. Dissolve 6.16g of resorcinol in 10mL of deionized water to form a transparent solution; add 0.808g of ferric nitrate to the above-mentioned transparent solution, mix and dissolve to obtain a uniform solution; add 9.08g of formaldehyde solution dropwise to the above-mentioned stirring solution, Stir and mix evenly, and continue to stir in an environment of 20°C until the reaction forms a gel; transfer the gel to a vacuum drying oven for 3 days of vacuum drying and aging treatment at 70°C, take it out, crush and grind to obtain a solid powder; put the solid powder in Carbonization treatment in NH 3 at 1000° C. for 5 h, washing away iron oxide with an appropriate amount of 1M HCl, filtering and drying to obtain the carbon material.
实施例3Example 3
采用溶胶凝胶法结合活化法制备氮掺杂的分级孔结构多孔碳材料。将6.16g间苯二酚溶于10mL去离子水,形成透明溶液;取0.2716g六水合硝酸钴添加到上述透明溶液中,混合溶解均匀得到溶液;向上述搅拌中的溶液中滴加9.08g甲醛溶液,进一步搅拌混合均匀,在20℃环境中持续搅拌,直至反应形成凝胶;将凝胶转移至真空干燥箱在70℃下真空干燥老化处理7d,取出后粉碎研磨,得到固体粉末;将固体粉末在NH3中900℃碳化处理3h,用适量1MHCl洗除氧化钴,过滤干燥,即得所述碳材料。Nitrogen-doped porous carbon materials with hierarchical pore structure were prepared by sol-gel method combined with activation method. Dissolve 6.16g of resorcinol in 10mL of deionized water to form a transparent solution; add 0.2716g of cobalt nitrate hexahydrate to the above transparent solution, mix and dissolve to obtain a solution; add dropwise 9.08g of formaldehyde to the above stirring solution The solution was further stirred and mixed evenly, and continuously stirred in an environment of 20°C until the reaction formed a gel; the gel was transferred to a vacuum drying oven for 7 days of vacuum drying and aging treatment at 70°C, and then crushed and ground to obtain a solid powder; the solid The powder was carbonized in NH 3 at 900°C for 3 hours, washed with an appropriate amount of 1M HCl to remove cobalt oxide, filtered and dried to obtain the carbon material.
实施例4Example 4
采用溶胶凝胶法结合发泡法制备氮掺杂的分级孔结构多孔碳材料。将6.16g间苯二酚溶于10mL去离子水,形成透明溶液;向上述搅拌中的溶液中加入9.08g甲醛溶液及1g碳酸氢铵,进一步搅拌混合均匀,在20℃环境中持续搅拌,直至反应形成凝胶;将凝胶转移至真空干燥箱在70℃下真空干燥老化处理7d,取出后粉碎研磨,得到固体粉末;将固体粉末在NH3中850℃处理2h,即得所述碳材料。Nitrogen-doped porous carbon materials with hierarchical pore structure were prepared by sol-gel method combined with foaming method. Dissolve 6.16g of resorcinol in 10mL of deionized water to form a transparent solution; add 9.08g of formaldehyde solution and 1g of ammonium bicarbonate to the stirring solution, stir and mix evenly, and continue to stir at 20°C until React to form a gel; transfer the gel to a vacuum drying oven for 7 days of vacuum drying and aging treatment at 70°C, take it out and grind it to obtain a solid powder; treat the solid powder in NH 3 at 850°C for 2 hours to obtain the carbon material .
实施例5Example 5
采用溶胶凝胶法结合发泡法制备氮掺杂的分级孔结构多孔碳材料。将6.16g间苯二酚溶于10mL去离子水,形成透明溶液;向上述搅拌中的溶液中加入9.08g甲醛溶液及1g柠檬酸,进一步搅拌混合均匀,在20℃环境中持续搅拌,直至反应形成凝胶;将凝胶转移至真空干燥箱在70℃下真空干燥老化处理7d,取出后粉碎研磨,得到固体粉末;将固体粉末在NH3中850℃处理2h,即得所述碳材料。Nitrogen-doped porous carbon materials with hierarchical pore structure were prepared by sol-gel method combined with foaming method. Dissolve 6.16g of resorcinol in 10mL of deionized water to form a transparent solution; add 9.08g of formaldehyde solution and 1g of citric acid to the stirring solution, stir and mix evenly, and continue stirring at 20°C until the reaction Form a gel; transfer the gel to a vacuum drying oven for 7 days of vacuum drying and aging treatment at 70°C, take it out and grind it to obtain a solid powder; treat the solid powder in NH 3 at 850°C for 2 hours to obtain the carbon material.
实施例6Example 6
采用溶胶凝胶法结合发泡法制备氮掺杂的分级孔结构多孔碳材料。将6.16g间苯二酚溶于10mL去离子水,形成透明溶液;向上述搅拌中的溶液中加入9.08g甲醛溶液及1g十六烷基三甲基溴化铵,进一步搅拌混合均匀,在20℃环境中持续搅拌,直至反应形成凝胶;将凝胶转移至真空干燥箱在70℃下真空干燥老化处理3d,取出后粉碎研磨,得到固体粉末;将固体粉末在NH3中1050℃处理2h,即得所述碳材料。Nitrogen-doped porous carbon materials with hierarchical pore structure were prepared by sol-gel method combined with foaming method. 6.16g of resorcinol was dissolved in 10mL of deionized water to form a transparent solution; 9.08g of formaldehyde solution and 1g of cetyltrimethylammonium bromide were added to the above stirring solution, and further stirred and mixed evenly, at 20 Stir continuously in an environment of ℃ until the reaction forms a gel; transfer the gel to a vacuum drying oven for 3 days of vacuum drying and aging treatment at 70 ℃, take it out and grind it to obtain a solid powder; treat the solid powder in NH 3 at 1050 ℃ for 2 hours , to obtain the carbon material.
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CN108172792A (en) * | 2017-12-26 | 2018-06-15 | 刘春丽 | A kind of composite cathode material for lithium ion cell and preparation method thereof |
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CN110690423B (en) * | 2019-09-27 | 2021-06-29 | 中国电子科技集团公司第十八研究所 | Heteroatom doped carbon material and preparation method and application thereof |
CN112038604A (en) * | 2020-09-03 | 2020-12-04 | 青海凯金新能源材料有限公司 | Battery negative electrode material with good conductivity and preparation method thereof |
CN116031383B (en) * | 2023-01-09 | 2024-10-29 | 南京航空航天大学 | Carbon composite material, preparation method and application thereof, and lithium ion thermal battery |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101284223A (en) * | 2007-04-13 | 2008-10-15 | 中国科学院金属研究所 | A kind of magnetic porous carbon adsorbent and preparation method thereof |
CN101454243A (en) * | 2006-05-31 | 2009-06-10 | 促进科学E.V.麦克斯-普朗克公司 | Porous carbon electrode with conductive polymer coating |
CN102104157A (en) * | 2009-12-16 | 2011-06-22 | 中国科学院大连化学物理研究所 | Preparation method for carbon dry gel |
CN102294255A (en) * | 2010-06-25 | 2011-12-28 | 中国科学院大连化学物理研究所 | Carbon gel catalyst and application thereof |
CN102299347A (en) * | 2010-06-25 | 2011-12-28 | 中国科学院大连化学物理研究所 | Application of catalyst in alkaline fuel cell |
WO2012111169A1 (en) * | 2011-02-16 | 2012-08-23 | Toyota Jidosha Kabushiki Kaisha | Method for producing cathode material for rechargeable lithium-air batteries, cathode material for rechargeable lithium-air batteries and rechargeable lithium-air battery |
-
2012
- 2012-11-28 CN CN201210496062.7A patent/CN103855365B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101454243A (en) * | 2006-05-31 | 2009-06-10 | 促进科学E.V.麦克斯-普朗克公司 | Porous carbon electrode with conductive polymer coating |
CN101284223A (en) * | 2007-04-13 | 2008-10-15 | 中国科学院金属研究所 | A kind of magnetic porous carbon adsorbent and preparation method thereof |
CN102104157A (en) * | 2009-12-16 | 2011-06-22 | 中国科学院大连化学物理研究所 | Preparation method for carbon dry gel |
CN102294255A (en) * | 2010-06-25 | 2011-12-28 | 中国科学院大连化学物理研究所 | Carbon gel catalyst and application thereof |
CN102299347A (en) * | 2010-06-25 | 2011-12-28 | 中国科学院大连化学物理研究所 | Application of catalyst in alkaline fuel cell |
WO2012111169A1 (en) * | 2011-02-16 | 2012-08-23 | Toyota Jidosha Kabushiki Kaisha | Method for producing cathode material for rechargeable lithium-air batteries, cathode material for rechargeable lithium-air batteries and rechargeable lithium-air battery |
Non-Patent Citations (1)
Title |
---|
"Ivestigation of the gas-diffusion-electrode used as lithium/air cathode in non-aqueous electrolyte and the importance of carbon material porosity";Chris Tran et al.;《Journal of Power Sources》;20091013;第195卷(第7期);第2057-2063页 * |
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