CN104201438B - A kind of lithium-air battery based on graphene oxide-carbon paper gas catalysis electrode - Google Patents
A kind of lithium-air battery based on graphene oxide-carbon paper gas catalysis electrode Download PDFInfo
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 116
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 62
- 229910021389 graphene Inorganic materials 0.000 title claims abstract description 58
- 238000006555 catalytic reaction Methods 0.000 title 1
- 238000000034 method Methods 0.000 claims abstract description 18
- 239000003792 electrolyte Substances 0.000 claims abstract description 13
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 12
- 230000003197 catalytic effect Effects 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000002360 preparation method Methods 0.000 claims abstract description 7
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 6
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- 239000010439 graphite Substances 0.000 abstract description 4
- 238000011068 loading method Methods 0.000 abstract description 4
- 239000000725 suspension Substances 0.000 abstract description 4
- 239000012153 distilled water Substances 0.000 abstract description 3
- 150000001336 alkenes Chemical class 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 description 18
- 229910052760 oxygen Inorganic materials 0.000 description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 16
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 10
- 229910052744 lithium Inorganic materials 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 8
- 229910018068 Li 2 O Inorganic materials 0.000 description 7
- 229910018071 Li 2 O 2 Inorganic materials 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000003054 catalyst Substances 0.000 description 6
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 5
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 5
- 239000012154 double-distilled water Substances 0.000 description 5
- JBTWLSYIZRCDFO-UHFFFAOYSA-N ethyl methyl carbonate Chemical compound CCOC(=O)OC JBTWLSYIZRCDFO-UHFFFAOYSA-N 0.000 description 5
- 125000000524 functional group Chemical group 0.000 description 5
- 229910001416 lithium ion Inorganic materials 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 4
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 4
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 239000002033 PVDF binder Substances 0.000 description 3
- 230000004913 activation Effects 0.000 description 3
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 3
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- FUJCRWPEOMXPAD-UHFFFAOYSA-N lithium oxide Chemical class [Li+].[Li+].[O-2] FUJCRWPEOMXPAD-UHFFFAOYSA-N 0.000 description 3
- 229910001947 lithium oxide Inorganic materials 0.000 description 3
- 239000011255 nonaqueous electrolyte Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 238000001132 ultrasonic dispersion Methods 0.000 description 3
- 229910013870 LiPF 6 Inorganic materials 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000001237 Raman spectrum Methods 0.000 description 2
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- 230000007797 corrosion Effects 0.000 description 2
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- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- 229910001290 LiPF6 Inorganic materials 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
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- 150000001721 carbon Chemical group 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
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- 238000004070 electrodeposition Methods 0.000 description 1
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- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 1
- 229910052808 lithium carbonate Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011268 mixed slurry Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- -1 oxygen ions Chemical class 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000002161 passivation Methods 0.000 description 1
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- 238000012360 testing method Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
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- 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
- H01M4/88—Processes of manufacture
- H01M4/8825—Methods for deposition of the catalytic active composition
- H01M4/8853—Electrodeposition
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Inert Electrodes (AREA)
- Hybrid Cells (AREA)
Abstract
本发明提供了一种基于氧化石墨烯‑碳纸气体催化电极的锂‑空气电池,该电池的正极为采用以下方法制得的碳纸支撑的氧化石墨烯催化电极,制备方法如下:将氧化石墨烯在磷酸缓冲液中超声分散成悬浮状态,制得电解液;然后以碳纸作正极,铂电极作负极,控制电解池电压为5~20V,在合适的搅拌速度和温度下,电泳‑电解5~30分钟,电解沉积结束后,氧化石墨烯负载在碳纸上;再用二次蒸馏水洗涤碳纸,然后真空干燥,最后用分析天平称重计量碳纸上氧化石墨烯的负载量。本发明制备步骤简单,操作参数易控,电极性能稳定且重现,在0.1mA/cm2电流密度下首次放电容量达11553mAh/g,循环电池运行520小时后性能稳定。
The invention provides a lithium-air battery based on a graphene oxide-carbon paper gas catalytic electrode, the positive electrode of the battery is a graphene oxide catalytic electrode supported by carbon paper prepared by the following method, and the preparation method is as follows: graphite oxide The alkene is ultrasonically dispersed in a phosphate buffer solution into a suspension state to prepare an electrolyte; then, the carbon paper is used as the positive electrode and the platinum electrode is used as the negative electrode, and the voltage of the electrolytic cell is controlled at 5-20V. 5 to 30 minutes, after the electrolytic deposition is completed, the graphene oxide is loaded on the carbon paper; the carbon paper is washed with twice distilled water, then vacuum-dried, and finally the graphene oxide loading on the carbon paper is weighed and measured with an analytical balance. The invention has simple preparation steps, easy control of operating parameters, stable and reproducible electrode performance, the first discharge capacity reaches 11553mAh/g at a current density of 0.1mA/ cm2 , and the performance of the cycle battery is stable after 520 hours of operation.
Description
技术领域technical field
本发明提供了一种锂-空气电池,尤其涉及一种基于氧化石墨烯-碳纸气体催化电极的锂-空气电池,属于锂-空气电池及其制备技术。The invention provides a lithium-air battery, in particular to a lithium-air battery based on a graphene oxide-carbon paper gas catalytic electrode, which belongs to the lithium-air battery and its preparation technology.
背景技术Background technique
锂-空气电池是一种以金属锂为负极,空气为正极的二次电池。它具有与锂离子电池完全不同的设计,其理论比能量为11140Wh/kg(不包括氧气质量),接近汽油的理论比能量值13000Wh/kg。即使考虑氧气的质量,其比能量也是普通锂离子电池的十倍(5210Wh/kg)。1996年,美国马赛诸塞州EIC实验室Abraham博士首次报道了这种新型聚合物电解质体系的锂-空气电池,获得1400Ah/kg的放电比容量,接近于汽油实际可利用比能量1700Wh/kg。该成果在世界范围内得到广泛的认可,从而引发了将其开发成汽车动力电池的研究热潮。锂-空气电池是金属/空气电池的一种,又叫做半燃料电池,是消耗Li的燃料电池,也是正极活性物质为氧气的锂电池。它与锂离子电池和燃料电池有相似之处,也有不同之处。与燃料电池相比,锂-空气电池用金属锂替代氢气,因此不用考虑氢气的储存问题,而且锂-空气电池可实现充/放循环,是一种方便的储能电池;与锂离子电池相比,锂-空气电池可以直接从空气中获取正极活性物质--氧气,而不需将其储存在电池系统内,大幅减轻了电池体系的重量,因此,理论上可实现大容量储能的锂-空气电池的巨大发展价值受到广泛关注。A lithium-air battery is a secondary battery that uses metallic lithium as the negative electrode and air as the positive electrode. It has a completely different design from lithium-ion batteries, and its theoretical specific energy is 11140Wh/kg (excluding oxygen mass), which is close to the theoretical specific energy value of gasoline of 13000Wh/kg. Even considering the quality of oxygen, its specific energy is ten times that of ordinary lithium-ion batteries (5210Wh/kg). In 1996, Dr. Abraham of EIC Laboratory in Massachusetts reported for the first time the lithium-air battery of this new polymer electrolyte system, which obtained a discharge specific capacity of 1400Ah/kg, which is close to the actual available specific energy of gasoline of 1700Wh/kg. This achievement has been widely recognized around the world, which has triggered a research upsurge in developing it into automotive power batteries. Lithium-air battery is a kind of metal/air battery, also known as half fuel cell, it is a fuel cell that consumes Li, and it is also a lithium battery in which the positive active material is oxygen. It has both similarities and differences to lithium-ion batteries and fuel cells. Compared with fuel cells, lithium-air batteries use metallic lithium instead of hydrogen, so there is no need to consider the storage of hydrogen, and lithium-air batteries can achieve charge/discharge cycles, which is a convenient energy storage battery; compared with lithium-ion batteries Compared with lithium-air batteries, the positive electrode active material-oxygen can be obtained directly from the air without storing it in the battery system, which greatly reduces the weight of the battery system. - The huge development value of air batteries has attracted widespread attention.
虽然锂-空气电池展现出很好的应用前景,但是实际上性能受各种因素限制,其能量转换效率距离理论上可到达值相差甚远。目前,锂-空气电池的负极采用金属锂片,为防止金属锂钝化,通常使用较为成熟的碳酸乙烯酯(EC)、碳酸甲乙酯(EMC)、碳酸二甲酯(DMC)混合溶剂配置而成的1mol/dm3LiPF6EC/EMC/DMC(质量比1:1:1)非水电解液(尽管水性电解质和固态电解质也在研究中),空气电极由(碳粉/催化剂/黏结剂)的混合浆料涂覆在泡沫镍上构成。在隔绝空气的环境中组装成电池:Although lithium-air batteries show good application prospects, their performance is actually limited by various factors, and their energy conversion efficiency is far from the theoretically achievable value. At present, the negative electrode of lithium-air batteries uses metal lithium sheets. In order to prevent metal lithium passivation, it is usually configured with a relatively mature mixed solvent of ethylene carbonate (EC), ethyl methyl carbonate (EMC) and dimethyl carbonate (DMC). 1mol/dm 3 LiPF 6 EC/EMC/DMC (mass ratio 1:1:1) non-aqueous electrolyte (although aqueous electrolyte and solid electrolyte are also under study), the air electrode consists of (carbon powder/catalyst/bonded agent) mixed slurry coated on foamed nickel. Assemble batteries in an air-isolated environment:
(-)锂片|有机电解液-隔膜|气体扩散电极(+)(-)Lithium sheet|Organic electrolyte-diaphragm|Gas diffusion electrode(+)
非水体系的锂-空气电池中,电池放电时负极锂片氧化产生的Li+通过电解液迁移到正极,与氧气还原产生的过氧离子(或进一步反应产生的氧离子O2-)形成锂的氧化物。而充电过程与放电过程相反,充电时锂的氧化物分解产生氧气和锂离子。放电产物Li2O2的生成不需要O-O键的断裂,因此反应不需要很高的活化能,在不使用催化剂的条件下也能顺利进行,见附图1。而充电过程是将形成的锂的氧化物分解,锂的氧化物是离子晶体,将其分解需要较高的活化能,而且当有电解液或粘结剂分解造成放电产物变为碳酸锂或含锂的有机物时,充电所需的活化能更高,因此充电过程中析氧催化剂的使用必不可少。相关证据显示,放电产物Li2O2或Li2O在非水电解液中不溶解,经过一次放电后,电极的空气一侧有大量放电产物无序堆积,而隔膜一侧则基本上没有放电产物,从而造成氧气传输通道堵塞,致使放电终止。而且,固态的Li2O2或Li2O离子晶体几乎是绝缘体,一旦生成并无序堆积而造成电极导电性破坏,使充电无法进行。可见实现电池反应产物在正极的有序化分布,保证充电过程中电极导电性不间断,加速或O2-→O2的转化速率,是有机电解液系锂-空气电池正极必须解决的关键问题,这也是近些年来人们不懈地在新型碳材料研究、多功能高效催化剂研究、电极空间结构设计与尝试等方面展开大规模探索的目标。In a lithium-air battery in a non-aqueous system, the Li + produced by the oxidation of the negative lithium sheet migrates to the positive electrode through the electrolyte when the battery is discharged, and the peroxide ion produced by the reduction of oxygen (or oxygen ions O 2- generated by further reactions) to form lithium oxides. The charging process is opposite to the discharging process. During charging, lithium oxides decompose to produce oxygen and lithium ions. The formation of the discharge product Li 2 O 2 does not require the cleavage of the OO bond, so the reaction does not require a high activation energy, and can proceed smoothly without using a catalyst, see Figure 1. The charging process is to decompose the formed lithium oxide, which is an ionic crystal, and its decomposition requires a high activation energy, and when the electrolyte or binder is decomposed, the discharge product becomes lithium carbonate or contains When lithium is an organic compound, the activation energy required for charging is higher, so the use of an oxygen evolution catalyst is essential during charging. Relevant evidence shows that the discharge product Li 2 O 2 or Li 2 O is insoluble in the non-aqueous electrolyte. After a discharge, a large amount of discharge products accumulate disorderly on the air side of the electrode, while there is basically no discharge on the diaphragm side. products, thereby causing the blockage of the oxygen transport channel, resulting in the termination of the discharge. Moreover, solid Li 2 O 2 or Li 2 O ion crystals are almost insulators, once formed and piled up in disorder, the conductivity of the electrode will be destroyed, making charging impossible. It can be seen that the orderly distribution of battery reaction products on the positive electrode can be realized to ensure the uninterrupted conductivity of the electrode during the charging process and accelerate the charging process. Or the conversion rate of O 2- → O 2 is the key problem that must be solved for the positive electrode of the organic electrolyte lithium-air battery. The goal of large-scale exploration in terms of design and experimentation.
发明内容Contents of the invention
本发明提供了一种基于氧化石墨烯-碳纸气体催化电极的锂-空气电池,该电池比现有的锂-空气电池具有更高的容量和充放循环性能;本发明还提供了一种电泳-电解沉积法制备氧化石墨烯-碳纸电极的方法。The invention provides a lithium-air battery based on graphene oxide-carbon paper gas catalytic electrode, which has higher capacity and charge-discharge cycle performance than existing lithium-air batteries; the invention also provides a A method for preparing graphene oxide-carbon paper electrodes by electrophoresis-electrodeposition.
实现本发明上述目的所采用的技术方案为:The technical scheme adopted to realize the above-mentioned purpose of the present invention is:
一种基于氧化石墨烯-碳纸气体催化电极的锂-空气电池,该电池的正极为采用以下方法制得的碳纸支撑的氧化石墨烯催化电极,制备方法如下:将氧化石墨烯在pH值为5~9的磷酸缓冲液中超声分散成悬浮状态,制得电解液;然后以碳纸作正极,铂电极作负极,组装成电泳-电解池,采用直流稳压电源控制电泳-电解池电压为5~20V,电解液的温度控制在20~50℃,电泳-电解时间为5~30分钟;在电解过程中,为使氧化石墨烯在碳纸表面均匀附着沉积,采用了匀速搅拌装置,搅拌速率为1000~4000r/min,电解沉积结束后,氧化石墨烯沉积在碳纸上;然后用二次蒸馏水洗涤负载有氧化石墨烯的碳纸,洗涤后在80~120℃下真空干燥,最后用分析天平称重计量碳纸上氧化石墨烯的负载量,所述的碳纸上氧化石墨烯的负载量为0.1~1.0mg/cm2。A lithium-air battery based on a graphene oxide-carbon paper gas catalytic electrode, the positive electrode of the battery is a graphene oxide catalytic electrode supported by carbon paper prepared by the following method, and the preparation method is as follows: graphene oxide is mixed at a pH value The electrophoresis-electrolysis cell is assembled by using carbon paper as the positive electrode and the platinum electrode as the negative electrode, and using a DC stabilized power supply to control the voltage of the electrophoresis-electrolysis cell. The temperature of the electrolyte is 5-20V, the temperature of the electrolyte is controlled at 20-50°C, and the electrophoresis-electrolysis time is 5-30 minutes; during the electrolysis process, in order to make the graphene oxide adhere and deposit evenly on the surface of the carbon paper, a uniform stirring device is used. The stirring rate is 1000-4000r/min. After the electrolytic deposition, the graphene oxide is deposited on the carbon paper; then the carbon paper loaded with graphene oxide is washed with twice distilled water, and after washing, it is vacuum-dried at 80-120°C, and finally An analytical balance is used to weigh and measure the loading amount of graphene oxide on the carbon paper, and the loading amount of graphene oxide on the carbon paper is 0.1-1.0 mg/cm 2 .
所述的碳纸为经过疏水和平整化处理后的碳纸,其厚度为25~34μm,与水的接触角为90~140°。The carbon paper is a carbon paper after hydrophobic and flattening treatment, its thickness is 25-34 μm, and its contact angle with water is 90-140°.
所述的电解液中氧化石墨烯的浓度为0.5~3.0mg/cm3。The graphene oxide concentration in the electrolyte is 0.5-3.0 mg/cm 3 .
当制备锂-空气电池时,将上述负载氧化石墨烯的碳纸剪裁成所需面积作正极,用锂片作负极,注入1mol/dm3LiPF6EC/EMC/DMC(质量比1:1:1)非水电解液,在隔绝空气下组装成扣式电池,在开路电压下静置3-24小时,采取恒电流自由放电模式和控制放电深度模式进行放电试验,记录电压-时间曲线和电压-比容量曲线。When preparing a lithium-air battery, the above-mentioned carbon paper loaded with graphene oxide is cut into the required area as the positive electrode, and the lithium sheet is used as the negative electrode, and injected with 1mol/dm LiPF 6 EC/EMC/DMC (mass ratio 1 :1: 1) Non-aqueous electrolyte, assembled into a button battery under the isolation of air, let it stand for 3-24 hours under the open circuit voltage, adopt constant current free discharge mode and control discharge depth mode for discharge test, record voltage-time curve and voltage - Specific capacity curve.
在本发明中,由于氧化石墨烯是片状剥离石墨经过氧化处理后的衍生物,仍保持石墨的层状结构,每个碳原子以sp2杂化轨道共价相连,但在每一层的石墨烯单片上引入了含氧基功能团。现阶段人们普遍接受的结构模型是在氧化石墨烯二维平面上随机分布着羟基和环氧基,而在单片的边缘则引入了羰基和羧基,见附图2。尽管这些含氧基团的数量和分布会因制备方法而异,但可以肯定的是,含氧基功能团的引入使得氧化石墨烯具有两亲性,从石墨烯薄片边缘到中央呈现亲水至疏水的性质,因而使之能悬浮于水溶液中。因此在本发明中考虑了以下因素:1、氧化石墨烯的羰基能通过电解氧化方法打开双键,在碳纸上形成氧化石墨烯表面;2、氧化石墨烯的羟基、羧基所含-OH基团在电极表面能看作是一种广义的“水”,提供给电池反应产物由Li2O2或Li2O向LiOH转变;3、由于氧化石墨烯仍保持石墨的层状结构,垂直于sp2碳环平面的离域大π键可增强碳纸的电子导电性;4、氧化石墨烯的含氧基功能团有较强的吸电子能力,电池充电时能诱导或O2-,或OH-趋向正极放电,实际起到对氧还原反应(放电,ORR)和析氧转化反应(充电,OER)催化剂的效果。In the present invention, since graphene oxide is a derivative of flaky exfoliated graphite after oxidation treatment, it still maintains the layered structure of graphite, and each carbon atom is covalently connected with sp 2 hybrid orbitals, but in each layer Oxygen-containing functional groups were introduced into graphene monoliths. The structure model generally accepted by people at this stage is that hydroxyl groups and epoxy groups are randomly distributed on the two-dimensional plane of graphene oxide, while carbonyl and carboxyl groups are introduced at the edge of the monolith, see Figure 2. Although the number and distribution of these oxygen-containing groups will vary depending on the preparation method, it is certain that the introduction of oxygen-containing functional groups makes graphene oxide amphiphilic, from the edge to the center of the graphene sheet, it is hydrophilic to the center. Hydrophobic properties, thus enabling it to be suspended in aqueous solutions. Therefore consider following factor in the present invention: 1, the carbonyl group of graphene oxide can open double bond by electrolytic oxidation method, forms graphene oxide surface on carbon paper; The group on the electrode surface can be regarded as a kind of "water" in a broad sense, which is provided to the battery reaction product to change from Li 2 O 2 or Li 2 O to LiOH; 3. Since graphene oxide still maintains the layered structure of graphite, it is perpendicular to The delocalized large π bond of the sp 2 carbon ring plane can enhance the electronic conductivity of carbon paper; 4. The oxygen-containing functional group of graphene oxide has a strong electron-absorbing ability, which can induce Or O 2- , or OH - tends to discharge toward the positive electrode, and actually acts as a catalyst for oxygen reduction reaction (discharge, ORR) and oxygen evolution conversion reaction (charge, OER).
本发明提供的锂-空气电池中,其正极巧妙地将氧化石墨烯与碳纸进行了结合,其优点在于:其一,利用碳纸的多孔性、导电性、稳定性,避免了充电电压在4.2V以后集流体的腐蚀,由于不需要任何影响电极电子导电性和孔容积的碳粉和催化剂材料,也不需要N-甲基吡咯烷酮分散剂(NMP)和PVDF粘合剂,大大降低了正极的欧姆电压降,见图4;其二,碳纸和氧化石墨烯皆为碳材料,通过电解氧化法使氧化石墨烯与碳纸键合,在正极引入-OH和COOH功能团,能促进Li2O2或Li2O向LiOH的转变,可由原来的充电反应Li2O2→2Li++O2+2e或Li2O→2Li+O2+4e转变为OH-在电极上的放电:4OH-→O2+H2O+4e,随着Li2O2或Li2O固态晶体在电极广义“水”作用下的转型及流态化,克服了电池反应产物在电极孔隙无序堆积所造成的电极导电性间断,使充电无法持续的问题;其三,氧化石墨烯的羰基、羧基等含氧基功能团具有吸引电子能力,充电时能诱导电极活性物质(Li2O2或Li2O,进而是OH-)在电极表面吸附并放电,实际上起到催化剂的作用,达到充电反应顺利进行的目的,大大提高了锂-空气电池的稳定性、循环性和实用性;最后,本发明的锂-空气电池组装后轻便稳定,电压平台高,放电容量大,在一定的放电制度下实现了稳定的充/放循环,而且,本发明制备工艺及操作参数简单易控,易于实现规模化生产,便于产业化推广。In the lithium-air battery provided by the present invention, the positive electrode skillfully combines graphene oxide and carbon paper. Corrosion of the current collector after 4.2V, because no carbon powder and catalyst material that affects the electronic conductivity and pore volume of the electrode, nor N-methylpyrrolidone dispersant (NMP) and PVDF binder, greatly reduces the corrosion rate of the positive electrode. ohmic voltage drop, see Figure 4; second, both carbon paper and graphene oxide are carbon materials, graphene oxide is bonded to carbon paper by electrolytic oxidation, and -OH and COOH functional groups are introduced into the positive electrode, which can promote Li The conversion of 2 O 2 or Li 2 O to LiOH can be transformed into OH by the original charging reaction Li 2 O 2 → 2Li + + O 2 +2e or Li 2 O → 2Li+O 2 +4e - discharge on the electrode: 4OH - →O 2 +H 2 O+4e, with the transformation and fluidization of Li 2 O 2 or Li 2 O solid crystals under the action of generalized "water" in the electrode, it overcomes the disordered accumulation of battery reaction products in the electrode pores The resulting electrode conductivity is interrupted, making charging unsustainable; third, the carbonyl, carboxyl and other oxygen-containing functional groups of graphene oxide have the ability to attract electrons, and can induce electrode active materials (Li 2 O 2 or Li 2 O, and then OH - ) is adsorbed and discharged on the electrode surface, which actually acts as a catalyst to achieve the purpose of smooth charging reaction, which greatly improves the stability, cycleability and practicability of lithium-air batteries; finally, The lithium-air battery of the present invention is light and stable after assembly, has a high voltage platform, and a large discharge capacity, and realizes a stable charge/discharge cycle under a certain discharge system. Moreover, the preparation process and operating parameters of the present invention are simple and easy to control, and are easy to implement Large-scale production is convenient for industrial promotion.
附图说明Description of drawings
图1为本发明中碳纸正极(CP)与氧化石墨烯-碳纸正极(GO-CP)的首次放电曲线对比图;Fig. 1 is the first discharge curve contrast figure of carbon paper positive pole (CP) and graphene oxide-carbon paper positive pole (GO-CP) in the present invention;
图2为本发明中氧化石墨烯结构示意图;Fig. 2 is a schematic diagram of graphene oxide structure in the present invention;
图3为本发明中通过电解负载了氧化石墨烯的碳纸SEM图及局部放大图;Fig. 3 is the carbon paper SEM figure and local enlarged figure of graphene oxide loaded by electrolysis in the present invention;
图4为本发明中对比例1和实施例1的首次放电曲线对比图;Fig. 4 is the comparison chart of the first discharge curve of comparative example 1 and embodiment 1 in the present invention;
图5为对比例3中以纯碳纸作正极的锂-空气电池的充放电循环曲线;Fig. 5 is the charge-discharge cycle curve of the lithium-air battery using pure carbon paper as the positive electrode in Comparative Example 3;
图6为本发明中负载氧化石墨烯-碳纸电极(GO-CP)与所使用的碳纸(CP)的拉曼光谱;Fig. 6 is the Raman spectrum of the graphene oxide-carbon paper electrode (GO-CP) and the carbon paper (CP) used in the present invention;
图7为本发明实施例1中在0.05mA/cm2和0.1mA/cm2的电流密度下的首次放电曲线;Fig. 7 is the discharge curve for the first time under the current density of 0.05mA/cm 2 and 0.1mA/cm 2 in the embodiment 1 of the present invention;
图8为本发明实施例2中截取的81-100次循环的充放循环图;Fig. 8 is a charge-discharge cycle diagram of 81-100 cycles intercepted in Example 2 of the present invention;
图9为本发明中实施例3的充放循环图。Fig. 9 is a charge-discharge cycle diagram of Example 3 of the present invention.
具体实施方式detailed description
为了较好地阐述本发明的内容、实质特点和显著进步,下面结合相关的对比例和实施例对本发明作进一步说明。在此需要说明的是,对于具体对比例和实施例的列举,是用于帮助理解本发明,但本发明并不局限于以下实施例。以下实施例中所述的碳纸为经过疏水和平整化处理后的碳纸,其厚度为25~34μm,与水的接触角为90~140°。In order to better illustrate the content, essential features and remarkable progress of the present invention, the present invention will be further described below in conjunction with relevant comparative examples and examples. It should be noted here that the enumeration of specific comparative examples and examples is to help understand the present invention, but the present invention is not limited to the following examples. The carbon paper described in the following examples is carbon paper after hydrophobic and planarization treatment, its thickness is 25-34 μm, and its contact angle with water is 90-140°.
对比例1Comparative example 1
将购买的石墨烯和聚偏氟乙烯(PVDF)按90:10的质量比在N-甲基吡咯烷酮(NMP)介质中调制成一定粘度的浆料,采用类似于丝网印刷的方法将浆料均匀地涂覆到碳纸上,然后放入真空烘箱,在80℃下烘12h,烘干后称重,并将涂好的碳纸铳成直径为8mm的圆片,由此制成正极片备用。The purchased graphene and polyvinylidene fluoride (PVDF) are modulated into a slurry of a certain viscosity in N-methylpyrrolidone (NMP) medium at a mass ratio of 90:10, and the slurry is coated by a method similar to screen printing. Evenly coated on carbon paper, then placed in a vacuum oven, baked at 80 ° C for 12 hours, weighed after drying, and the coated carbon paper was shot into a disc with a diameter of 8 mm, thus making a positive electrode sheet spare.
在氩气保护的手套箱中,采用CR2032电池壳(正极壳表面已打孔以保证氧气的传输通道)作为电池封装体,依次将金属锂片(Φ15.6×0.45mm)、隔膜Celgard 2325、正极片逐层装好,并滴加适量商业的1M LiPF6(EC:EMC:DMC=1:1:1)电解液使电极和隔膜被浸润,将电池在封装机上封口,即完成电池组装。In an argon-protected glove box, a CR2032 battery case (the surface of the positive electrode case has been perforated to ensure the transmission channel of oxygen) was used as the battery package, and the metal lithium sheet (Φ15.6×0.45mm), the separator Celgard 2325, The positive electrode sheet is installed layer by layer, and an appropriate amount of commercial 1M LiPF6 (EC:EMC:DMC=1:1:1) electrolyte is added dropwise to infiltrate the electrode and separator, and the battery is sealed on the packaging machine to complete the battery assembly.
电池的整个运行过程在干燥的氧气中进行,在0.05mA/cm2的电流密度下,首次放电容量为6022mAh/g,放电平台在2.7V左右,见附图4。The whole operation process of the battery is carried out in dry oxygen. Under the current density of 0.05mA/cm 2 , the initial discharge capacity is 6022mAh/g, and the discharge platform is around 2.7V, see Figure 4.
对比例2Comparative example 2
将烘干的纯碳纸作为正极,按对比例1中的方法制作锂-空气电池,得到如附图1中的放电曲线,首次放电容量为13830.7mAh/g(纯碳纸),放电平台平均值在2.7V左右。The pure carbon paper that dries is used as positive electrode, makes lithium-air battery by the method in comparative example 1, obtains the discharge curve as in accompanying drawing 1, and first discharge capacity is 13830.7mAh/g (pure carbon paper), and discharge platform average The value is around 2.7V.
对比例3Comparative example 3
将烘干的纯碳纸作为正极,假设与实施例1中的负载量相同,控制放电深度,即控制放电容量为1000mAh/g,得到附图5中的循环曲线,纯碳纸电极经过20次充放后放电终止。The pure carbon paper of drying is used as the positive electrode, assuming that the loading capacity in Example 1 is the same, the depth of discharge is controlled, that is, the discharge capacity is controlled to be 1000mAh/g, and the cycle curve in the accompanying drawing 5 is obtained. The pure carbon paper electrode passes through 20 times Discharge terminates after charging and discharging.
实施例1Example 1
将氧化石墨烯以1.0mg/cm3的浓度超声分散于二次蒸馏水中,加入KH2PO4和K2HPO4,配制成pH9.0的磷酸缓冲溶液,继续超声分散6h,使之成均匀分散的悬浮液。以铂电极为负极,碳纸为正极,组装成电泳-电解池,稳压电源控制电解池电压在20V,电解液的温度控制在45℃,在电解过程中,为使氧化石墨烯在碳纸表面均匀附着沉积,采用了匀速搅拌装置,搅拌速率为2000r/min,电解反应时间为5min。将负载氧化石墨烯的碳纸电极用二次蒸馏水清洗,其拉曼图谱见附图6。将清洗后的负载氧化石墨烯的碳纸电极在真空烘箱中80℃下烘12h,称重,铳成直径为8mm的圆片组装电池。分别在0.05mA/cm2和0.1mA/cm2的电流密度下恒流放电,其首次放电曲线如附图7。电源为两电极直流电源。Ultrasonic disperse graphene oxide at a concentration of 1.0 mg/cm 3 in double distilled water, add KH 2 PO 4 and K 2 HPO 4 to prepare a phosphate buffer solution with pH 9.0, and continue ultrasonic dispersion for 6 hours to make it uniform Dispersed suspension. The electrophoresis-electrolytic cell is assembled with a platinum electrode as the negative electrode and carbon paper as the positive electrode. The voltage of the electrolytic cell is controlled at 20V by the stabilized power supply, and the temperature of the electrolyte is controlled at 45°C. The surface is evenly attached and deposited, using a uniform stirring device, the stirring rate is 2000r/min, and the electrolysis reaction time is 5min. The carbon paper electrode loaded with graphene oxide was washed with double distilled water, and its Raman spectrum is shown in Figure 6. The cleaned carbon paper electrodes loaded with graphene oxide were baked in a vacuum oven at 80°C for 12 hours, weighed, and punched into discs with a diameter of 8 mm to assemble batteries. The discharge curves for the first time are shown in Figure 7 when the constant current discharges are performed at the current densities of 0.05mA/cm 2 and 0.1mA/cm 2 respectively. The power supply is a two-pole DC power supply.
实施例2Example 2
将氧化石墨烯以2.0mg/cm3的浓度超声分散于二次蒸馏水中,加入KH2PO4和K2HPO4,配制成pH8.0的磷酸缓冲溶液,继续超声分散6h,使之成均匀分散的悬浮液。以铂电极为负极,碳纸为正极,组装成电泳-电解池,稳压电源控制电解池电压在15V,电解液的温度控制在35℃,在电解过程中,为使氧化石墨烯在碳纸表面均匀附着沉积,采用了匀速搅拌装置,搅拌速率为3000r/min,电解反应时间为15min。将负载氧化石墨烯的碳纸电极用二次蒸馏水清洗,将清洗后的负载氧化石墨烯的碳纸电极在真空烘箱中100℃下烘10h,称重,铳成直径为8mm的圆片组装电池。Ultrasonic disperse graphene oxide at a concentration of 2.0 mg/cm 3 in twice distilled water, add KH 2 PO 4 and K 2 HPO 4 to prepare a pH 8.0 phosphate buffer solution, and continue ultrasonic dispersion for 6 hours to make it uniform Dispersed suspension. The electrophoresis-electrolytic cell is assembled with a platinum electrode as the negative electrode and carbon paper as the positive electrode. The voltage of the electrolytic cell is controlled at 15V by the stabilized power supply, and the temperature of the electrolyte is controlled at 35°C. During the electrolysis process, in order to make the graphene oxide on the carbon paper The surface is uniformly attached and deposited, using a uniform stirring device, the stirring rate is 3000r/min, and the electrolysis reaction time is 15min. The carbon paper electrode loaded with graphene oxide was cleaned with double distilled water, and the cleaned carbon paper electrode loaded with graphene oxide was dried in a vacuum oven at 100°C for 10 h, weighed, and assembled into a disc with a diameter of 8 mm. .
采用本实施例中制备的正极片,在0.05mA/cm2的电流密度下,控制放电容量为500mAh/g(按负载氧化石墨烯的量计算),其充放循环曲线如附图8。Using the positive electrode sheet prepared in this example, at a current density of 0.05 mA/cm 2 , the discharge capacity is controlled to be 500 mAh/g (calculated based on the amount of supported graphene oxide), and its charge-discharge cycle curve is shown in Figure 8.
实施例3Example 3
将氧化石墨烯以3.0mg/cm3的浓度超声分散于二次蒸馏水中,加入KH2PO4和K2HPO4,配制成pH7.0的磷酸缓冲溶液,继续超声分散6h,使之成均匀分散的悬浮液。以铂电极为负极,碳纸为正极,组装成电泳-电解池,稳压电源控制电解池电压在8V,电解液的温度控制在25℃,在电解过程中,为使氧化石墨烯在碳纸表面均匀附着沉积,采用了匀速搅拌装置,搅拌速率为4000r/min,电解反应时间为25min。将负载氧化石墨烯的碳纸电极用二次蒸馏水清洗,将清洗后的负载氧化石墨烯的碳纸电极在真空烘箱中120℃下烘8h,称重,铳成直径为8mm的圆片组装电池。Ultrasonic disperse graphene oxide at a concentration of 3.0 mg/cm 3 in double distilled water, add KH 2 PO 4 and K 2 HPO 4 to prepare a pH 7.0 phosphate buffer solution, and continue ultrasonic dispersion for 6 hours to make it uniform Dispersed suspension. The electrophoresis-electrolytic cell is assembled with a platinum electrode as the negative electrode and carbon paper as the positive electrode. The voltage of the electrolytic cell is controlled at 8V by the stabilized power supply, and the temperature of the electrolyte is controlled at 25°C. During the electrolysis process, in order to make the graphene oxide on the carbon paper The surface is uniformly attached and deposited, using a uniform stirring device, the stirring rate is 4000r/min, and the electrolysis reaction time is 25min. The carbon paper electrode loaded with graphene oxide was cleaned with double distilled water, and the cleaned carbon paper electrode loaded with graphene oxide was dried in a vacuum oven at 120°C for 8 hours, weighed, and formed into a disc with a diameter of 8 mm to assemble the battery .
采用本实施例中制备的正极片,在0.05mA/cm2的电流密度下,控制放电容量为1000mAh/g(按负载氧化石墨烯的量计算),其充放循环曲线如附图9。Using the positive electrode sheet prepared in this example, at a current density of 0.05mA/cm 2 , the discharge capacity is controlled to be 1000mAh/g (calculated based on the amount of graphene oxide supported), and its charge-discharge cycle curve is shown in Figure 9.
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AU2012378149B2 (en) | 2011-12-21 | 2016-10-20 | The Regents Of The University Of California | Interconnected corrugated carbon-based network |
US9779884B2 (en) | 2012-03-05 | 2017-10-03 | The Regents Of The University Of California | Capacitor with electrodes made of an interconnected corrugated carbon-based network |
JP2018501644A (en) | 2014-11-18 | 2018-01-18 | ザ リージェンツ オブ ザ ユニバーシティ オブ カリフォルニア | Porous interconnected corrugated carbon based network (ICCN) composites |
CN105037763B (en) * | 2015-07-31 | 2017-07-11 | 中国地质大学(北京) | The preparation method of modified graphene oxide piezopolymer energy storage thin-film device |
AU2016378400B2 (en) | 2015-12-22 | 2021-08-12 | The Regents Of The University Of California | Cellular graphene films |
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WO2017165548A1 (en) | 2016-03-23 | 2017-09-28 | The Regents Of The University Of California | Devices and methods for high voltage and solar applications |
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CN106637327B (en) * | 2016-11-09 | 2019-04-19 | 中国科学院生态环境研究中心 | Cathode material for electrocatalytic reduction of oxygen, preparation method and use thereof |
CN107026274B (en) * | 2017-05-16 | 2020-05-22 | 中国地质大学(武汉) | Preparation method and application of graphene/carbon paper gas electrode in borax buffer system |
CN107342428B (en) * | 2017-06-08 | 2020-02-07 | 中国科学技术大学 | Method for enhancing microbial extracellular electron transfer in microbial electrochemical system |
CN107768688B (en) * | 2017-10-24 | 2020-09-04 | 昆明纳太科技有限公司 | Gas diffusion catalytic electrode, preparation method thereof and application thereof in rechargeable zinc-air battery |
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