High-rate electrochemical energy storage through Li+ intercalation pseudocapacitance

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电化学应用_铅酸蓄电池的发展及其应用_廖斯达

电化学应用_铅酸蓄电池的发展及其应用_廖斯达

易维护或免维护、浮充寿命长、使用安全、单电池电压高等独特优势,长期以来被广泛应用于社会生产和生活 的多种场合。铅酸电池技术发展经历了漫长的历史过程,本文通过回顾铅酸电池的发展历史,从铅酸电池原理 确立和技术演化两个方面进行讨论,从铅酸电池使用到回收的全生命周期过程进行全面评价与分析。在此基础 上,展望铅酸电池的未来发展方向和应用前景,为新型电化学储能技术的提供借鉴。 关键词:铅酸蓄电池;电化学储能;发展史;应用 doi:10.3969/j.issn.2095-4239.2013.05.010 中图分类号: N 092 文献标志码:A 文章编号:2095-4239(2013)05-514-08
不同种类常用电池的性能比较[4] Comparison of different batteries
镍镉、镍氢电池 高功率放电 中 较好 好 中 中 较好 高倍率充放电、 技 术成熟 自放电明显、 镍隔 电池有记忆效应、 镉 污染环境 4.5 >1000 4.5 5~8 — 锂离子电池 能量密度高 好 好 好 较差 好 较差 高倍率充放电、 技术成熟、 能 量密度高、 无记忆效应、 循环寿 命长、自放电小、环保性好 成本高、安全性未完全解决、 高功率放电性能差 6 >1000 6 5~8 — 燃料电池 能量密度极高 好 中 好 差 好 差 能量密度高、能量 转换效率高、低污染
收稿日期:2013-08-15;修改稿日期:2013-08-22。 基金项目:国家自然科学基金项目(21076112,21276134)和国家高技术 研究发展计划(863)项目(2012AA051203) 。 第一作者:廖斯达(1988—) ,男,硕士研究生,主要研究方向为液流电池 储能技术,E-mail:liaostar@;通讯联系人:王保国,博士,教授, 从事膜材料、储能科学与技术研究,E-mail:bgwang@。

太赫兹材料与器件英文

太赫兹材料与器件英文

太赫兹材料与器件英文With the rapid development of science and technology, the demand for high-speed communication and advanced imaging systems has increased in recent years. One of the most promising solutions for these needs is the use of Terahertz (THz) materials and devices.THz waves refer to electromagnetic radiation with frequencies between 0.1 and 10 THz. This frequency range is also known as the THz gap, which is an area in the electromagnetic spectrum that is difficult to access with traditional technologies. With the development of THz technology, it is possible to exploit THz waves for a range of applications, including imaging, sensing, communication, and security.To harness the potential of THz waves, researchers have focused on developing THz materials and devices. These materials and devices have unique properties that make them ideal for THz applications. For example, THz waves can pass through a range of materials, including plastics, wood, and clothing, making them ideal for security applications. THz devices can also detect subtle changes in materials, making them useful for medical imaging and quality control in manufacturing.The development of THz materials and devices has been facilitated by advances in nanotechnology, which allows the creation of new materials with controlled properties. One such material is graphene, which has extraordinary electron transport properties that make it ideal for THz applications.Other materials used for THz devices and components include gallium arsenide (GaAs), indium antimonide (InSb), and indium phosphide (InP).Apart from materials, THz devices also require components such as antennas, sources, and detectors. Antennas are used to generate and receive THz waves, while sources provide the energy required for THz radiation. Detectors, on the other hand, capture and convert the THz radiation into a form that can be analyzed.In summary, THz technology is a promising area of research that has already shown its potential in a range of applications. The development of THz materials and devices is essential to harnessing the potential of THz waves. Nanotechnology has enabled the creation of new materials with controlled properties, while components such as antennas, sources, and detectors are required for THz devices. With continued research and development, THz technology will undoubtedly lead to significant advances in communication, imaging, and sensing.。

长寿命锰酸锂锂离子电池(中英文)

长寿命锰酸锂锂离子电池(中英文)

120
Capacity retention rate / %
5C charge/10C discharge
100
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3000cycles-80%
40
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Cycle number
Cyclic performance of Modified LiMn2O4/C Li-ion batteries (3.0-4.2V)
痕量酸作用下,LiMn2O4发生歧化反应:
The disproportion reaction of LiMn2O4 in trace amount acids
LiMn 2 O 4 + 4H + → Li + + λ MnO 2 + Mn 2+ + 2H 2 O
添加剂 Additives
控制HF含量添加剂: Additives for decreasing HF
与电解质相容性影响因素包括:正极表 面膜的稳定性,电解液组分的氧化分解和 LiMn2O4在电解液中溶解.
电解液组分氧化:Electrolyte oxidation
CH3OCO CH3 (DMC) 3O2 → 3CO2 + 3H2O + 2
LiMn2O4高温分解:
LiMn2O4 decomposition at high temperature
mobile phones Electric bicycles Power tools Electric toys Mining lamps, emergency lamps Vacuum cleaner
LiMn2O4的特点

以核桃壳为碳源微波加热制备介孔活性炭

以核桃壳为碳源微波加热制备介孔活性炭

以核桃壳为碳源微波加热制备介孔活性炭∗王力臻;闻红丽;孙淑敏;张勇【摘要】The mesoporous activated carbon was prepared by microwave radiation process using walnut shell as carbon source.The as-prepared activated carbon was well characterized by XRD,SEM and nitrogen adsorption-desorption.The influences of microwave power and radiation time on the capacitance characteristics of activated carbon for electrochemical capacitors was investigated by glavanostatic charge-discharge,cyclic voltammetry (CV)and AC impedancespectroscopy.Microwave power at 480 W and radiation time for 9 min were regarded as the optimum process.The activated carbon prepared under this process had the average pore size of 4.44 nm and the mesoporous rate of 78.51 %.The specific surface area was 1 530 m2/g and its shape was irregular,porous and amorphous structure.The specific capacitance was 226.4 F/g at the charge-discharge current of 100 mA/g. It kept 192.2 F/g after 1 000 cycles,and the capacity fade of activated carbon was only 0.015 % when cycled at 100 mA/g.%以核桃壳为碳源,微波辐射法制备了介孔活性炭。

电泳沉积法制备高能量密度的非对称平面微型超级电容器

电泳沉积法制备高能量密度的非对称平面微型超级电容器

【电子技术/Electronic Technology】DOI: 10.19289/j.1004-227x.2021.03.001 电泳沉积法制备高能量密度的非对称平面微型超级电容器刘红彬1, *,赵方方2(1.中移(苏州)软件技术有限公司,江苏苏州215000;2.力神电池(苏州)有限公司,江苏苏州215000)摘要:首先采用光刻、蒸镀金的方法制备叉指电极,随后把合成的具有赝电容特性的二维MnO2和Ti3C2纳米片分别电泳沉积到叉指电极上,构建了非对称平面超级电容器。

其中MnO2为正极,Ti3C2为负极,滴涂凝胶为电解质,并利用透明的聚二甲基硅氧烷薄膜封装成器件。

通过能量色散X射线光谱(EDS)、傅里叶变换红外光谱(FT-IR)、扫描电子显微镜(SEM)、光学显微镜等手段证明了电泳沉积后材料的结构没有发生变化以及叉指电极的成功制备,也说明了电泳沉积后材料的形貌为薄膜结构。

最后通过二电极系统测试了器件的电化学性能,结果显示该器件具有高倍率性能和高能量密度,同时保持着高功率密度和优异的机械柔韧性,其容量在各种弯曲角度下基本没有衰减。

关键词:二氧化锰;碳化钛;电泳沉积;赝电容;二维材料;叉指电极;非对称平面微型超级电容器中图分类号:TQ174 文献标志码:A 文章编号:1004 – 227X (2021) 03 – 0171 – 06 Preparation of high-energy-density asymmetric planar microsupercapacitors by electrophoretic depositionLIU Hongbin 1, *, ZHAO Fangfang 2( 1. China Mobile (SuZhou) Software Technology Co., Ltd., Suzhou 215000, China;2. Lishen Battery (Suzhou) Joint-Stock Co., Ltd., Suzhou 215000, China)Abstract:The interdigitated electrodes were first prepared by photolithography and gold evaporation. Subsequently, the synthesized two-dimensional MnO2 and Ti3C2 nanosheets with pseudocapacitive properties were electrodeposited onto the interdigitated electrodes to fabricate asymmetric planar supercapacitors with gel electrolyte encapsulated with a transparent polydimethylsiloxane film, where MnO2 was the positive electrode and Ti3C2 was the negative electrode. The results of energy-dispersive X-ray spectroscopy, Fourier-transform infrared spectroscopy (FT-IR), scanning electron microscopy (SEM), and optical microscopy proved that the microstructures of MnO2 and Ti3C2 after electrophoretic deposition were unchanged and the interdigitated electrodes were prepared successfully, and also showed that the electrophoretically deposited materials were of a thin film structure. The electrochemical performance of the fabricated device was tested by a two-electrode system, which showed that it not only had high rate capability and high energy density, but also maintained high power density and good mechanical flexibility. There was basically no attenuation in capability for the device when being bended at various angles.Keywords:manganese dioxide; titanium carbide; electrophoretic deposition; pseudocapacitance; two-dimensional material; interdigitated electrode; asymmetric planar microsupercapacitor随着现代可穿戴电子设备的持续快速发展,对特征尺寸在微米范围内器件的制备开始成为人们比较感兴趣的问题[1-3]。

耦合光热发电储热-有机朗肯循环的先进绝热压缩空气储能系统热力学分析

耦合光热发电储热-有机朗肯循环的先进绝热压缩空气储能系统热力学分析

第 12 卷第 12 期2023 年 12 月Vol.12 No.12Dec. 2023储能科学与技术Energy Storage Science and Technology耦合光热发电储热-有机朗肯循环的先进绝热压缩空气储能系统热力学分析尹航1,王强1,朱佳华2,廖志荣2,张子楠1,徐二树2,徐超2(1中国广核新能源控股有限公司,北京100160;2华北电力大学能源动力与机械工程学院,北京102206)摘要:先进绝热压缩空气储能是一种储能规模大、对环境无污染的储能方式。

为了提高储能系统效率,本工作提出了一种耦合光热发电储热-有机朗肯循环的先进绝热压缩空气储能系统(AA-CAES+CSP+ORC)。

该系统中光热发电储热用来解决先进绝热压缩空气储能系统压缩热有限的问题,而有机朗肯循环发电系统中的中低温余热发电来进一步提升储能效率。

本工作首先在Aspen Plus软件上搭建了该耦合系统的热力学仿真模型,随后本工作研究并对比两种聚光太阳能储热介质对系统性能的影响,研究结果表明,导热油和太阳盐相比,使用太阳盐为聚光太阳能储热介质的系统性能更好,储能效率达到了115.9%,往返效率达到了68.2%,㶲效率达到了76.8%,储电折合转化系数达到了92.8%,储能密度达到了5.53 kWh/m3。

此外,本研究还发现低环境温度、高空气汽轮机入口温度及高空气汽轮机入口压力有利于系统储能性能的提高。

关键词:先进绝热压缩空气储能;聚光太阳能辅热;有机朗肯循环;热力学模型;㶲分析doi: 10.19799/ki.2095-4239.2023.0548中图分类号:TK 02 文献标志码:A 文章编号:2095-4239(2023)12-3749-12 Thermodynamic analysis of an advanced adiabatic compressed-air energy storage system coupled with molten salt heat and storage-organic Rankine cycleYIN Hang1, WANG Qiang1, ZHU Jiahua2, LIAO Zhirong2, ZHANG Zinan1, XU Ershu2, XU Chao2(1CGN New Energy Holding Co., Ltd., Beijing 100160, China; 2School of Energy Power and Mechanical Engineering,North China Electric Power University, Beijing 102206, China)Abstract:Advanced adiabatic compressed-air energy storage is a method for storing energy at a large scale and with no environmental pollution. To improve its efficiency, an advanced adiabatic compressed-air energy storage system (AA-CAES+CSP+ORC) coupled with the thermal storage-organic Rankine cycle for photothermal power generation is proposed in this report. In this system, the storage of heat from photothermal power generation is used to solve the problem of limited compression heat in the AA-CAES+CSP+ORC, while the medium- and low-temperature waste heat generation in the organic Rankine cycle power收稿日期:2023-08-18;修改稿日期:2023-09-18。

化工专业英语例句摘录(2)-电极材料

化工专业英语例句摘录(2)-电极材料

期刊文献中的英文句子摘录(3)原文:This small-sized molecule is incapable to be carbonized into 2D carbonnanosheets since it could escape from the gallery of HNTO during the processes of thermal polymerization and carbonization.翻译:由于这种小分子无法在热聚合和碳化过程中从HNTO通道中逸出,因此无法碳化成2D碳纳米片。

出处:DOI: 10.1021/acsami.0c03775原文:Metal sulfides as promising SIB anode material s have merits of hightheoretical capacities, better reversibility, and relatively higher electronic conductivity than metal oxides counterparts.翻译:金属硫化物作为有希望的SIB负极材料,具有比金属氧化物对应物更高的理论容量,更好的可逆性和相对更高的电子电导率的优点。

出处:10.1007/s40820-020-0367-9原文:Carbon materials have been investigated as electrode materials forelectrochemical energy storage and capture owing to their large surface area, electrical conductivity, electrochemical, thermal, and mechanical stabilities, diverse morphologies and chemistries.翻译:碳已经成为研究电化学能量捕获存储的电极材料,这是由于其表面积大,导电性,电化学,热和机械的稳定性以及不同的形态具有的化学性质。

山东圣泉新能源科技有限公司钛酸锂电池规格书说明书

山东圣泉新能源科技有限公司钛酸锂电池规格书说明书
山东圣泉新能源科技有限公司
文件名称:SQT-32145H-6Ah 圆柱钛酸锂电池规格书 SPECIFICATIONS of SQT-32145H-6Ah LTO BATTERY
电池型号: SQT-32145H/6Ah Battery Model: SQT-32145H/6Ah
Document No. 文件编号
编制人 Editor
修订页次 Pages
修订日期 Date
全部页次 2019.06.10 All Pages
增加了第 10 条:模组 焊接注意
事项
Precautions for Module
Welding
2020.05.12
审核批准 Check/Approval
审核意见 Suggestion
审核人签名 Signature
文件名称 SQ- LTO32145H-6Ah 圆柱电池规格

文件编号 版本号
SQNTX-Ⅱ-16-JL11-06A
A/0 页码 1/15
1. 适用范围 Scope
本规格书描述纳米钛酸锂电池之基本参数、电化学特性、可靠性及其试验和判定标准、使用说明、安 全规程、质量评定及包装、贮存和运输等,适用于山东圣泉新能源科技有限公司制造的 LTO32145H/6Ah 纳 米钛酸锂电池。
This specification describes the titanate lithium cell’s basic parameters, electrochemical characteristics, reliability and its test method, decision criteria, instructions, safety procedures, quality evaluation, packaging, storage, and transportation, and etc. The specification is applied to the LTO32145H/6Ah lithium ion cell manufactured by Shandong Shengquan New Energy Technology Co. Ltd..

新能源材料与器件英语

新能源材料与器件英语

新能源材料与器件英语New Energy Materials and Devices.New energy materials and devices are key components of the emerging clean energy economy, enabling the development of sustainable energy sources and efficient energy storage and conversion technologies. These materials and devices encompass a wide range of electrochemical, photovoltaic, and thermal energy applications, offering promising solutions for addressing global energy challenges.Electrochemical Energy Storage.Electrochemical energy storage systems, such as batteries and supercapacitors, play a crucial role in storing electricity from renewable energy sources and providing backup power. The development of new energy materials and devices for electrochemical energy storage is critical for improving energy density, power density, cycle life, and safety.Batteries: Batteries are electrochemical devices that store chemical energy and convert it into electrical energy through electrochemical reactions. Advancements in battery materials, including cathode materials (e.g., lithium-ion, lithium-sulfur), anode materials (e.g., graphite, silicon), and electrolytes, aim to enhance energy density, reduce charging time, and improve stability.Supercapacitors: Supercapacitors are electrochemical devices that store energy electrostatically at theinterface between two conductive materials separated by an electrolyte. New materials and device architectures are being explored to increase capacitance, power density, and energy density, making supercapacitors suitable for applications requiring high-rate energy delivery.Photovoltaic Energy Conversion.Photovoltaic devices, such as solar cells and solar panels, convert sunlight into electricity through the photovoltaic effect. The efficiency of photovoltaic energyconversion is determined by the optical and electrical properties of the semiconductor materials used.Solar Cells: Solar cells are the fundamental building blocks of photovoltaic systems, generating electricity when exposed to sunlight. New materials and device structuresare being developed to improve light absorption, reduce carrier recombination, and enhance energy conversion efficiency.Solar Panels: Solar panels consist of multiple solar cells connected together to increase the total power output. Advancements in module design, packaging, andinterconnection technologies focus on improving durability, reducing costs, and maximizing energy yield.Thermal Energy Conversion.Thermal energy conversion technologies involve the conversion of heat into electricity. New energy materials and devices for thermal energy conversion include thermoelectric materials and thermophotovoltaic devices.Thermoelectric Materials: Thermoelectric materials generate electricity from a temperature gradient, enabling waste heat recovery and power generation from low-gradeheat sources. Research efforts are directed towards developing materials with high thermoelectric figure of merit, which quantifies the efficiency of thermal energy conversion.Thermophotovoltaic Devices: Thermophotovoltaic devices convert thermal radiation directly into electricity through the photovoltaic effect. New materials and device designs aim to improve absorption efficiency, reduce thermal losses, and enhance overall performance.Materials for New Energy Applications.The development of new energy materials and devices requires advanced materials with specific properties and functionalities. These materials include:Electrodes: Electrodes are essential components ofelectrochemical energy storage and conversion devices, responsible for charge transfer and electrochemical reactions. New materials with high electrical conductivity, electrochemical stability, and specific surface area are being explored.Semiconductors: Semiconductors are the active materials in photovoltaic devices, responsible for light absorption and charge separation. New semiconductors with optimized bandgaps, carrier mobilities, and light absorption properties are being developed.Dielectrics: Dielectrics are insulating materials used in capacitors and transistors, enabling charge storage and electronic switching. New dielectric materials with high permittivity and electrical stability are being explored.Superconductors: Superconductors are materials that exhibit zero electrical resistance below a critical temperature. Superconducting materials are being investigated for use in high-efficiency energy transmission and storage.Summary.New energy materials and devices are essential for the transition towards a sustainable energy future. The development of these materials and devices requires a multidisciplinary approach, combining materials science, electrochemistry, photovoltaic physics, and thermal engineering. By pushing the boundaries of materials science and engineering, new energy materials and devices will enable efficient and reliable energy storage, conversion, and utilization, paving the way for a cleaner and more sustainable energy landscape.。

电化学脱合金的英文

电化学脱合金的英文

电化学脱合金的英文Electrochemical Dealloying: Principles, Applications, and Challenges.Introduction.Electrochemical dealloying is a process that involves the selective removal of one or more constituent metalsfrom a multicomponent metallic alloy by electrochemical means. This process, often referred to as "dealuminization" in the context of aluminum-based alloys, has found widespread applications in materials science, nanotechnology, and energy conversion and storage systems. The primary advantage of electrochemical dealloying lies in its ability to create nanostructured materials with unique physical and chemical properties, such as high surface area, porosity, and conductivity.Principles of Electrochemical Dealloying.The electrochemical dealloying process occurs when an alloy is immersed in an electrolyte solution and apotential is applied between the alloy and a counter-electrode. The applied potential drives the electrochemical reactions at the alloy surface, resulting in thedissolution of one or more constituent metals. The dissolution rate of each metal depends on its electrochemical properties, such as the redox potential and electrochemical activity in the given electrolyte.During the dealloying process, the alloy is typically the anode, and the counter-electrode is the cathode. The anode is connected to the positive terminal of the power source, while the cathode is connected to the negative terminal. When the potential is applied, the alloy begins to dissolve, and the dissolved metal ions migrate towards the cathode. At the cathode, the metal ions are reduced and deposited on the surface, forming a new metal layer.The rate of metal dissolution during electrochemical dealloying is controlled by several factors, including the electrolyte composition, applied potential, temperature,and alloy composition. By optimizing these parameters, researchers can precisely control the morphology, porosity, and composition of the resulting nanostructured materials.Applications of Electrochemical Dealloying.Electrochemical dealloying has found numerous applications in materials science and engineering. Some of the key applications are discussed below:1. Nanoporous Metals: Electrochemical dealloying is widely used to create nanoporous metals with high surface area and porosity. These materials exhibit unique physical and chemical properties that are beneficial in various applications, such as catalysis, sensors, and energy storage.2. Battery Materials: Nanoporous metals produced by electrochemical dealloying have been explored as anode materials for lithium-ion batteries. The high porosity and surface area of these materials enhance the lithium storage capacity and improve the battery's performance.3. Fuel Cells: Electrochemical dealloying has also been used to create nanostructured catalysts for fuel cells. These catalysts exhibit enhanced activity and durability, which are crucial for efficient fuel cell operation.4. Biomedical Applications: Nanoporous metals produced by electrochemical dealloying have potential applicationsin biomedicine, such as drug delivery, tissue engineering, and implant materials. The porous structure of these materials allows for controlled drug release and improved cell adhesion and growth.Challenges and Future Directions.Despite the significant progress made inelectrochemical dealloying, several challenges remain to be addressed. One of the primary challenges is the control of the dealloying process at the nanoscale, as it is crucialfor achieving the desired material properties. Additionally, the development of new electrolytes and optimization of dealloying parameters are ongoing research efforts.Future research in electrochemical dealloying could focus on exploring new alloy systems, optimizing the dealloying process for specific applications, and understanding the fundamental mechanisms underlying metal dissolution and nanostructure formation. Furthermore, the integration of electrochemical dealloying with other nanotechnology approaches, such as lithography and templating, could lead to the development of even more advanced materials with tailored properties.Conclusion.Electrochemical dealloying is a powerful technique for creating nanostructured materials with unique physical and chemical properties. Its applications span multiple fields, including materials science, energy conversion and storage, and biomedicine. While significant progress has been madein this field, there are still numerous challenges and opportunities for further research and development. With the advancement of nanotechnology and materials science, electrochemical dealloying holds promise for enabling thecreation of next-generation materials with improved performance and functionality.。

Electrochemical energy storage systems

Electrochemical energy storage systems

Electrochemical energy storage systems 电化学储能系统As the world moves towards renewable energy sources, the need for energy storage systems has become increasingly important. One of the most promising energy storage technologies is electrochemical energy storage systems. In this article, we will explore the basics of electrochemical energy storage systems and their applications.随着世界向可再生能源的方向发展,储能系统的需求变得越来越重要。

最有前途的储能技术之一是电化学储能系统。

在本文中,我们将探讨电化学储能系统的基础知识和应用。

Basics of Electrochemical Energy Storage Systems电化学储能系统的基础知识Electrochemical energy storage systems convert electrical energy into chemical energy and store it. The energy can be released when needed by reversing the process. The most common type of electrochemical energy storage system is the battery. A battery consists of one or more electrochemical cells, which convert chemical energy into electrical energy.电化学储能系统将电能转换为化学能并储存。

nature铝离子电池英文原文An ultrafast rechargeable aluminium-ion battery

nature铝离子电池英文原文An ultrafast rechargeable aluminium-ion battery

An ultrafast rechargeable aluminium-ion batteryMeng-Chang Lin 1,2*,Ming Gong 1*,Bingan Lu 1,3*,Yingpeng Wu 1*,Di-Yan W ang 1,4,5,Mingyun Guan 1,Michael Angell 1,Changxin Chen 1,Jiang Yang 1,Bing-Joe Hwang 6&Hongjie Dai 1The development of new rechargeable battery systems could fuel var-ious energy applications,from personal electronics to grid storage 1,2.Rechargeable aluminium-based batteries offer the possibilities of low cost and low flammability,together with three-electron-redox properties leading to high capacity 3.However,research efforts over the past 30years have encountered numerous problems,such as cathode material disintegration 4,low cell discharge voltage (about 0.55volts;ref.5),capacitive behaviour without discharge voltage plateaus (1.1–0.2volts 6or 1.8–0.8volts 7)and insufficient cycle life (less than 100cycles)with rapid capacity decay (by 26–85per cent over 100cycles)4–7.Here we present a rechargeable aluminium bat-tery with high-rate capability that uses an aluminium metal anode and a three-dimensional graphitic-foam cathode.The battery oper-ates through the electrochemical deposition and dissolution of alu-minium at the anode,and intercalation/de-intercalation of chloroaluminate anions in the graphite,using a non-flammable ionic liquid electrolyte.The cell exhibits well-defined discharge voltage plateaus near 2volts,a specific capacity of about 70mA h g –1and a Coulombic efficiency of approximately 98per cent.The cathode was found to enable fast anion diffusion and intercalation,affording charging times of around one minute with a current densityof 4,000mA g –1(equivalent to 3,000W kg –1),and to withstand more than 7,500cycles without capacity decay.Owing to the low-cost,low-flammability and three-electron redox properties of aluminium (Al),rechargeable Al-based batteries could in principle offer cost-effectiveness,high capacity and safety,which wouldlead to a substantial advance in energy storage technology 3,8.However,research into rechargeable Al batteries over the past 30years has failed to compete with research in other battery systems.This has been due to problems such as cathode material disintegration 4,low cell discharge voltage (,0.55V;ref.5),capacitive behaviour without discharge voltage plateaus (1.1–0.2V,or 1.8–0.8V;refs 6and 7,respectively),and insuf-ficient cycle life (,100cycles)with rapid capacity decay (by 26–85%over 100cycles)4–7.Here we report novel graphitic cathode materials that afford unprecedented discharge voltage profiles,cycling stabilities and rate capabilities for Al batteries.We constructed Al/graphite cells (see diagram in Fig.1a)in Swagelok or pouch cells,using an aluminium foil (thickness ,15–250m m)anode,a graphitic cathode,and an ionic liquid electrolyte made from vacuum dried AlCl 3/1-ethyl-3-methylimidazolium chloride ([EMIm]Cl;see Methods,residual water ,500p.p.m.).The cathode was made from either pyrolytic graphite (PG)foil (,17m m)or a three-dimensional graphitic foam 9,10.Both the PG foil and the graphitic-foam materials exhibited typical graphite structure,with a sharp (002)X-ray diffraction (XRD)graphite peak at 2h <26.55u (d spacing,3.35A˚;Extended Data Fig.1).The cell was first optimized in a Swagelok cell operating at 25u C with a PG foil cathode.The optimal ratio of AlCl 3/[EMIm]Cl was found to be ,1.3–1.5(Extended Data Fig.2a),affording a specific discharging capacity of 60–66mA h g 21(based on graphitic cathode mass)with a Coulombic efficiency of 95–98%.Raman spectroscopy revealed that with an AlCl 3/[EMIm]Cl ratio of ,1.3,both AlCl 42and Al 2Cl 72anions were present (Extended Data Fig.2b)at a ratio [AlCl 42]/[Al 2Cl 72]<2.33*These authors contributed equally to this work.1Department of Chemistry,Stanford University,Stanford,California 94305,USA.2Green Energy and Environment Research Laboratories,Industrial Technology Research Institute,Hsinchu 31040,Taiwan.3School of Physics and Electronics,Hunan University,Changsha 410082,China.4Department of Chemistry,National Taiwan Normal University,Taipei 11677,Taiwan.5Institute of Atomic and Molecular Sciences,Academia Sinica,Taipei 10617,Taiwan.6Department of Chemical Engineering,National Taiwan University of Science and Technology,Taipei 10607,Taiwan.V o l t a g e(V)Time (h)Cycle numberSpecific capacity (mA h g –1)e –4Battery discharging ab c(aluminium)(graphite)C n [AlCl 4] + eC n + AlCl 4EMI +Al 2Cl 74Al 2Cl 7 + 3eAlCl 3/[EMIm]Cl Ionic liquidAl + 7AlCl 43060901201500.00.51.01.52.02.5Charging DischargingV o l t a g e (V )S p e c i fi c c a p a c i t y (m A h g –1)Coulombic efficiency (%)–––––––Figure 1|Rechargeable Al/graphite cell.a ,Schematic drawing of the Al/graphite cell during discharge,using the optimal composition of the AlCl 3/[EMIm]Cl ionic liquid electrolyte.On the anode side,metallic Al and AlCl 4–were transformed into Al 2Cl 7–during discharging,and the reverse reaction took place during charging.On the cathode side,predominantly AlCl 4–wasintercalated and de-intercalated between graphite layers during charge and discharge reactions,respectively.b ,Galvanostatic charge and discharge curves of an Al/pyrolytic graphite (PG)Swagelok cell at a current density of66mA g 21.Inset,charge and discharge cycles.c ,Long-term stability test of an Al/PG cell at 66mA g 21.00M O N T H 2015|V O L 000|N A T U R E |1Macmillan Publishers Limited. All rights reserved©2015(ref.11).The cathode specific discharging capacity was found to be independent of graphite mass (Extended Data Fig.3),suggesting that the entirety of the graphite foil participated in the cathode reaction.The Al/PG cell exhibited clear discharge voltage plateaus in the ranges 2.25–2.0V and 1.9–1.5V (Fig.1b).The relatively high discharge voltage plateaus are unprecedented among all past Al-ion charge-storage sys-tems 4–7.Similar cell operation was observed with the amount of elec-trolyte lowered to ,0.02ml per mg of cathode material (Extended Data Fig.4).Charge–discharge cycling at a current density of 66mA g 21(1C charging rate)demonstrated the high stability of the Al/PG cell,which nearly perfectly maintained its specific capacity over .200cycles with a 98.160.4%Coulombic efficiency (Fig.1c).This was consistent with the high reversibility of Al dissolution/deposition,with Coulombic efficiencies of 98.6–99.8%in ionic liquid electrolytes 12–15.No dendrite formation was observed on the Al electrode after cycling (Extended Data Fig.5).To maintain a Coulombic efficiency .96%,the cut-off voltage of the Al/PG cell (that is,the voltage at which charging was stopped)was set at 2.45V,above which reduced efficiencies were observed (see Extended Data Fig.6a),probably due to side reactions (especially above ,2.6V)involving the electrolyte,as probed by cyclic voltamme-try with a glassy carbon electrode against Al (Extended Data Fig.6b).We observed lowered Coulombic efficiency and cycling stability of the Al/graphite cell when using electrolytes with higher water contents,up to ,7,500p.p.m.(Extended data Fig.6c,d),accompanied by obvious H 2gas evolution measured by gas chromatography (Extended Data Fig.6e).This suggested side reactions triggered by the presence of resi-dual water in the electrolyte,with H 2evolution under reducing poten-tial on the Al side during charging.Further lowering the water contentof the ionic liquid electrolyte could be important when maximizing the Coulombic efficiency of the Al/graphite cells.The Al/PG cell showed limited rate capability with much lower specific capacity when charged and discharged at a rate higher than 1C (Extended Data Fig.7).It was determined that cathode reactions in the Al/PG cell involve intercalation and de-intercalation of relatively large chloroa-luminate (Al x Cl y 2)anions in the graphite (see below for XRD evidence of intercalation),and the rate capability is limited by slow diffusion of anions through the graphitic layers 16.When PG was replaced by nat-ural graphite,intercalation was evident during charging owing to dra-matic expansion (,50-fold)of the cathode into loosely stacked flakes visible to the naked eye (Extended Data Fig.8a).In contrast,expansion of PG foil upon charging the Al/PG cell was not observable by eye (Extended Data Fig.8b),despite the similar specific charging capacity of the two materials (Extended Data Fig.8c).This superior structural integrity of PG over natural graphite during charging was attributed to the existence of covalent bonding between adjacent graphene sheets in PG 17,which was not present in natural ing PG,which has an open,three-dimensionally-bound graphitic structure,we prevented excessive electrode expansion that would lead to electrode disinteg-ration,while maintaining the efficient anion intercalation necessary for high performance.Because high-rate and high-power batteries are highly desirable for applications such as electrical grid storage,the next step in the investi-gation was to develop a cathode material that would have reduced ener-getic barriers to intercalation during charging 16.We investigated a flexible graphitic foam (Fig.2a),which was made on a nickel foam template by chemical vapour deposition 9,10(see Methods),as a possible material fordcbCycle numberSpecific capacity (mA h g –1)a3060901201500.00.51.01.52.02.5Charging DischargingV o l t a g e (V )223.5223.6223.7223.80.00.51.01.52.02.5V o l t a g e (V )Time (h)Cycle numberCoulombic efficiency (%)Coulombic efficiency (%)S p e c i fi c c a p a c i t y (m A h g –1)S p e c i fi c c a p a c i t y (m A h g –1)Figure 2|An ultrafast and stable rechargeable Al/graphite cell.a ,Ascanning electron microscopy image showing a graphitic foam with an open frame structure;scale bar,300m m.Inset,photograph of graphitic foam;scale bar,1cm.b ,Galvanostatic charge and discharge curves of an Al/graphitic-foam pouch cell ata current density of 4,000mA g 21.c ,Long-term stability test of an Al/graphitic-foam pouch cell over 7,500charging and discharging cycles at a current density of 4,000mA g 21.d ,An Al/graphitic-foam pouch cell charging at 5,000mA g 21and discharging at current densities ranging from 100to 5,000mA g 21.LETTER2|N A T U R E |V O L 000|00M O N T H 2015Macmillan Publishers Limited. All rights reserved©2015ultrafast Al batteries.The graphite whiskers in the foam were 100m m in width (Fig.2a),with large spaces in between,which greatly decreased the diffusion length for the intercalating electrolyte anions and facili-tated more rapid battery operation.Remarkably,the Al/graphitic-foam cell (in a pouch cell configuration)could be charged and discharged at a current density up to 5,000mA g 21,about 75times higher (that is,at a 75C rate,,1min charge/discharge time)than the Al/PG cell while maintaining a similar voltage profile and discharge capacity (,60mA h g 21)(Figs 1b and 2b).An impres-sive cycling stability with ,100%capacity retention was observed over 7,500cycles with a Coulombic efficiency of 9762.3%(Fig.2c).This is the first time an ultrafast Al-ion battery has been constructed with stability over thousands of cycles.The Al/graphitic-foam cell retained similar capacity and excellent cycling stability over a range of charge–discharge rates (1,000–6,000mA g 21)with 85299%Coulombic effi-ciency (Extended Data Fig.9a).It was also found that this cell could be rapidly charged (at 5,000mA g 21,in ,1min)and gradually discharged (down to 100mA g 21,Fig.2d and Extended Data Fig.9b)over ,34min while maintaining a high capacity (,60mA h g 21).Such a rapid char-ging/variable discharging rate could be appealing in many real-world applications.We propose that simplified Al/graphite cell redox reactions during charging and discharging can be written as:4Al 2Cl {7z 3e {'Al z 7AlCl {4ð1ÞC n z AlCl {4'C n AlCl 4½ z e{ð2Þwhere n is the molar ratio of carbon atoms to intercalated anions in thegraphite.The balanced AlCl 4–and Al 2Cl 7–concentrations in the electro-lyte allowed for an optimal charging capacity at the cathode,with abun-dant AlCl 4–for charging/intercalation in graphite (equation (2)),and sufficient Al 2Cl 7–concentration for charging/electrodeposition at the anode (equation (1).Ex situ XRD measurement of graphite foil (Fig.3a)confirmed graphite intercalation/de-intercalation by chloroaluminate anions during charging/discharging.The sharp pristine graphite foil (002)peak at2h 526.55u (d spacing 53.35A˚)(Fig.3a)vanished on charging to a specific capacity of ,30mA h g –1,while two new peaks appeared at,28.25u (d <3.15A˚)and ,23.56u (d <3.77A ˚)(Fig.3a),with peak intensities further increasing on fully charging to ,62mA h g –1.The doublet XRD peak suggested highly strained graphene stacks formed on anion intercalation 18.Analysis of the peak separation (see Methods)suggested a stage 4graphite intercalation compound with an interca-lant gallery height (spacing between adjacent graphitic host layers)of,5.7A˚,indicating that the AlCl 4–anions (size ,5.28A ˚;ref.19)were intercalated between graphene layers in a distorted state.Full dischar-ging led to the recovery of the graphite peak but with a broad shoulder (Fig.3a),probably caused by irreversible changes in the stacking between the graphene layers or a small amount of trapped species.In situ Raman spectroscopy was also performed to probe chloroalu-minate anion intercalation/de-intercalation from graphite during cell charge/discharge (Fig.3b).The graphite G band (,1,584cm –1)diminished and split into a doublet (1,587cm –1for the E 2g2(i)mode and ,1,608cm –1for the E 2g2(b)mode)upon anion intercalation (Fig.3b)20,and then evolved into a sharp new peak (,1,636cm –1,the G2band of the E 2g2(b)mode,spectrum 2.41V,Fig.3b)once fully charged.The spectral changes were then reversed upon discharging (Fig.3b),as the typical graphite Raman G band (1584cm –1)was recovered when fully discharged (spectrum 0.03V,Fig.3b).Similar Raman spectra and XRD data were obtained with a graphitic-foam cathode (Extended Data Fig.10a,b).Interestingly,calcination of a fully charged PG foil at 850u C in air (Fig.3c)yielded a white aluminium oxide foam (Extended Data Fig.10c),confirming the intercalation of chloroaluminate anions into the carbon network,which had been evi-dently removed oxidatively.Lastly,X-ray photoelectron spectra (XPS)and Auger electron spec-troscopy (AES)were performed to probe the chemical nature of the intercalated species in our graphitic cathodes (see Methods for details).To minimize the amount of trapped electrolyte,graphitic foam was used and the electrode was thoroughly washed with anhydrous methanol.XPS revealed that upon charging pristine graphite,the 284.8eV C 1s peak developed a shoulder at higher energy (,285.9eV,Fig.4a),con-firming electrochemical oxidation of graphitic carbon by intercalation of AlCl 4–anions (equation (2)).Chloroaluminate intercalation was evi-dent from the appearance of Al 2p and Cl 2p peaks (Fig.4b,c).UponFully charged PG850°C in aircba20253035discharged chargedcharged 30 mA h g 24 mA h g I n t e n s i t y (a .u .)62 mA h g Pristinedischarged 60 mA h g 3.77 Å3.35 Å3.15 ÅSecond cycleI n t e n s i t y (a .u .)Raman shift (cm –1)2q (degrees)Figure 3|Al/graphite cell reaction mechanisms.a ,Ex situ X-ray diffraction patterns of PG in various charging and discharging states through the second cycle.b ,In situ Raman spectra recorded for the PG cathode through a charge–discharge cycle,showing chloroaluminate anion intercalation/de-intercalation into graphite.c ,After calcination of a fully charged(62mA h g 21)PG electrode at 850u C in air,the sample completely transformed into a white foam made of aluminium oxide.Scale bar,1cm.I n t e n s i t y (a .u .)Binding energy (eV)4008001,2001,6002,000–2.0–1.00.01.02.0C l OC d N (E )/d E (×104)d N (E )/d E (×104)Kinetic energy (eV)AlDischarged cathodeCharged cathodeC+Al+Clf edgcKinetic energy (eV)Figure 4|Chemical probing of a graphitic cathode by XPS and AES.a ,XPS data of the C 1s peak of a graphitic-foam electrode:pristine,fully charged and fully discharged.b ,c ,XPS data of Al 2p and Cl 2p peaks observed with a graphitic-foam electrode:pristine,fully charged and fully discharged.d–g ,AES mapping images for C,Al and Cl (d ,f ),and the AES spectrum of the boxed regions (e ,g )obtained with a fully charged graphitic-foam sample (d ,e )and a fully discharged graphitic-foam sample (f ,g ).Scale bars:d ,25m m;f ,10m m.LETTER 00M O N T H 2015|V O L 000|N A T U R E |3Macmillan Publishers Limited. All rights reserved©2015discharging,the C1s XPS spectrum of the cathode reverted to that of the pristine graphite due to anion de-intercalation and carbon reduc-tion(Fig.4a).Also,a substantial reduction in the Al2p and Cl2p signals was recorded over the graphite sample(see Fig.4b,c).The remaining Al and Cl signals observed were attributed to trapped/adsorbed species in the graphite sample,which was probed by XPS over a large area.Fur-thermore,high spatial resolution AES elemental mapping of a single graphite whisker in the fully charged graphitic foam clearly revealed Al and Cl Auger signals uniformly distributed over the whisker(Fig.4d,e), again confirming chloroaluminate anion intercalation.When fully dis-charged,AES mapping revealed anion de-intercalation from graphite with much lower Al and Cl Auger signals observed(Fig.4f,g).These spectroscopic results clearly revealed chloroaluminate ion intercala-tion/de-intercalation in the graphite redox reactions involved in our rechargeable Al cell.The Al battery pouch cell is mechanically bendable and foldable(Sup-plementary Video1)owing to the flexibility of the electrode and sepa-rator materials.Further,we drilled through Al battery pouch cells during battery operation and observed no safety hazard,owing to the lack of flammability of the ionic liquid electrolyte in air(see Supplementary Video2).We have developed a new Al-ion battery using novel graphitic cath-ode materials with a stable cycling life up to7,500charge/discharge cycles without decay at ultrahigh current densities.The present Al/graphite battery can afford an energy density of,40W h kg–1(comparable to lead–acid and Ni–MH batteries,with room for improvement by opti-mizing the graphitic electrodes and by developing other novel cathode materials)and a high power density,up to3,000W kg–1(similar to super-capacitors).We note that the energy/power densities were calculated on the basis of the measured,65mA h g–1cathode capacity and the mass of active materials in electrodes and electrolyte.Such recharge-able Al ion batteries have the potential to be cost effective and safe,and to have high power density.Online Content Methods,along with any additional Extended Data display items and Source Data,are available in the online version of the paper;references unique to these sections appear only in the online paper.Received12March2014;accepted6February2015.Published online6April2015.1.Yang,Z.et al.Electrochemical energy storage for green grid.Chem.Rev.111,3577–3613(2011).2.Huskinson,B.et al.A metal-free organic-inorganic aqueous flow battery.Nature505,195–198(2014).3.Li,Q.&Bjerrum,N.J.Aluminum as anode for energy storage and conversion:areview.J.Power Sources110,1–10(2002).4.Gifford,P.R.&Palmisano,J.B.An aluminum/chlorine rechargeable cellemploying a room temperature molten salt electrolyte.J.Electrochem.Soc.135, 650–654(1988).5.Jayaprakash,N.,Das,S.K.&Archer,L.A.The rechargeable aluminum-ion 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and its cycling efficiencies.J.Electrochem.Soc.132, 598–601(1985).13.Wilkes,J.S.,Levisky,J.A.,Wilson,R.A.&Hussey,C.L.Dialkylimidazoliumchloroaluminate melts:a new class of room-temperature ionic liquids forelectrochemistry,spectroscopy and synthesis.Inorg.Chem.21,1263–1264(1982).i,P.K.&Skyllas-Kazacos,M.Electrodeposition of aluminium in aluminiumchloride/1-methyl-3-ethylimidazolium chloride.J.Electroanal.Chem.Interfacial Electrochem.248,431–440(1988).15.Jiang,T.,Chollier Brym,M.J.,Dube´,G.,Lasia,A.&Brisard,G.M.Electrodeposition ofaluminium from ionic liquids:Part I—electrodeposition and surface morphology of aluminium from aluminium chloride(AlCl3)–1-ethyl-3-methylimidazolium chloride([EMIm]Cl)ionic liquids.Surf.Coat.Tech.201,1–9(2006).16.Borg,R.J.&Dienes,G.J.An Introduction to Solid State Diffusion(Academic,1988).17.Zhu,Y.-J.,Hansen,T.A.,Ammermann,S.,McBride,J.D.&Beebe,T.P.Nanometer-size monolayer and multilayer molecule corrals on HOPG:a depth-resolvedmechanistic study by 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Acknowledgements We thank M.D.Fayer for discussions.We also thank Y.Cui’s group for use of an argon-filled glove box and a vacuum oven.M.-C.L thanks the Bureau of Energy,Ministry of Economic Affairs,Taiwan,for supporting international cooperation between Stanford University and ITRI.B.L.acknowledges support from the National Natural Science Foundation of China(grant no.21303046),the China Scholarship Council(no.201308430178),and the Hunan University Fund for Multidisciplinary Developing(no.531107040762).We also acknowledge support from the US Department of Energy for novel carbon materials development and electrical characterization work(DOE DE-SC0008684),Stanford GCEP,the Precourt Institute of Energy,and the Global Networking Talent3.0plan(NTUST104DI005)from the Ministry of Education of Taiwan.Author Contributions M.-C.L.,M.G.,B.L.and Y.W.contributed equally to this work. M.-C.L.and H.D.conceived the idea for the project.B.L.prepared the graphitic foam. M.-C.L.,M.G.,B.L.,Y.W.,D.-Y.W.,M.A.and M.Guan performed electrochemical experiments.M.-C.L.,C.C.and J.Y conducted in situ Raman spectroscopy measurements.M.-C.L.,M.G.,B.L.and Y.W.performed ex situ X-ray diffraction measurements.M.G.,M.-C.L.,B.L.and Y.W.performed X-ray photoelectron spectroscopy and Auger electron spectroscopy measurements.M.-C.L.,M.G.,B.L.,Y.W., D.-Y.W.,M.A.,B.-J.H.and H.D.discussed the results,analysed the data and drafted the manuscript.Author Information Reprints and permissions information is available at/reprints.The authors declare no competing financial interests. Readers are welcome to comment on the online version of the paper.Correspondence and requests for materials should be addressed to H.D.(hdai@).LETTER4|N A T U R E|V O L000|00M O N T H2015Macmillan Publishers Limited. All rights reserved©2015METHODSPreparation of ionic liquid electrolytes.A room temperature ionic liquid electro-lyte was made by mixing1-ethyl-3-methylimidazolium chloride([EMIm]Cl,97%, Acros Chemicals)and anhydrous aluminium chloride(AlCl3,99.999%,Sigma Aldrich).[EMIm]Cl was baked at130u C under vacuum for16–32h to remove residual water.([EMIm]Al x Cl y)ionic liquid electrolytes were prepared in an argon-atmosphere glove box(both[EMIm]Cl and AlCl3are highly hygroscopic)by mix-ing anhydrous AlCl3with[EMIm]Cl,and the resulting light-yellow,transparent liquid was stirred at room temperature for10min.The mole ratio of AlCl3to[EMIm]Cl was varied from1.1to1.8.The water content of the ionic liquid was determined (500–700p.p.m.)using a coulometric Karl Fischer titrator,DL39(Mettler Toledo). The predominant anions in basic melts(AlCl3/[EMIm]Cl mole ratio,1)are Cl2 and AlCl42,while in acidic melts(AlCl3/[EMIm]Cl mole ratio.1)chloroalumi-nate anions such as Al2Cl72,Al3Cl102,and Al4Cl132are formed11.The ratio of anions to cations in the AlCl3/[EMIm]Cl electrolyte was determined using a glass fibre filter paper(Whatman GF/D)loaded with a4–8m m Au-coated SiO2beads21in a cuvette cell(0.35ml,Starna Cells)with random orientation quartz windows.Then,in the glove box,the cuvette cell was filled with AlCl3/[EMIm]Cl51.3(by mole).Raman spectra(200–650cm-1)were obtained using a785-nm laser with2cm–1resolution. Raman data were collected from the surface of the Au-coated SiO2bead so as to benefit from surface enhanced Raman21,22(Extended Data Fig.2b). Preparation of graphitic foam.Nickel(Ni)foams(Alantum Advanced Technology Materials,Shenyang,China),were used as3D scaffold templates for the CVD growth of graphitic foam,following the process reported previously9,10. The Ni foams were heated to1,000u C in a horizontal tube furnace(Lindberg Blue M,TF55030C)under Ar(500standard cubic centimetres per minute or s.c.c.m.)and H2(200s.c.c.m.)and annealed for10min to clean their surfaces and to eliminate a thin surface oxide layer.Then,methane(CH4)was introduced into the reaction tube at ambient pressure at a flow rate of10s.c.c.m.,corresponding to a concen-tration of1.4vol.%in the total gas flow.After10min of reaction gas mixture flow, the samples were rapidly cooled to room temperature at a rate of300u C min21 under Ar(500s.c.c.m.)and H2(200s.c.c.m.).The Ni foams covered with graphite were drop-coated with a poly(methyl methacrylate)(PMMA)solution(4.5%in ethyl acetate),and then baked at110u C for0.5h.The PMMA/graphene/Ni foam structure was obtained after solidification.Afterwards,these samples were put into a3M HCl solution for3h to completely dissolve the Ni foam to obtain the PMMA/graphite at80u C.Finally,the pure graphitic foam was obtained by removing PMMA in hot acetone at55u C and annealing in NH3(80s.c.c.m.)at 600u C for2h,and then annealing in air at450u C for2h.The microstructure of the graphitic foam was examined by SEM analysis using a FEI XL30Sirion scanning electron microscope(Fig.2a in the main text).Preparation of glassy carbon.Glassy carbon(GC)was used as the current collector in the Swagelok-type cell.72g phenol(Sigma-Aldrich)and4.5ml ammonium hydroxide(30%,Fisher Scientific)were dissolved in100ml formaldehyde solution (37%,Fisher Scientific)under reflux while stirring rapidly.The solution was stirred at90u C until the solution turned a milk-white colour.Rotary evaporation was used to remove the water and get the phenolic resin.The phenolic resin was solidified at 100u C in a mould(1/2-inch glass tube),and then carbonized at850u C under an Ar atmosphere for four hours to obtain the GC rod.The resulting GC rod contributed negligible capacity to the cathode(Extended Data Fig.6b).Electrochemical measurements.Prior to assembling the Al/graphite cell in the glove box,all components were heated under vacuum at60u C for more than12h to remove residual water.All electrochemical tests were performed at2561u C.A Swagelok-type cell(1/2inch diameter)was constructed using a,4mg PG foil(0.017mm,Suzhou Dasen Electronics Materials)cathode and a90mg Al foil (0.25mm,Alfa Aesar)anode.A1/2inch GC rod(10mm)was used as the current collector for the PG cathode,and a1/2inch graphite rod(10mm)was used for the Al anode.Six layers of1/2inch glass fibre filter paper(Whatman934-AH)were placed between the anode and cathode.Then,,1.0ml of ionic liquid electrolyte (prepared with AlCl3/[EMIm]Cl mole ratios of1.1,1.3,1.5and1.8)was injected and the cell sealed.The Al/PG cell was then charged(to2.45V)and discharged(to 0.01V)at a current density of66mA g–1with a MTI battery analyser(BST8-WA) to identify the ideal AlCl3/[EMIm]Cl mole ratio(Extended Data Fig.2a).To investigate the Coulombic efficiency of the Al/PG cell in AlCl3/[EMIm]Cl<1.3 (by mole)electrolyte,the cell was charged to2.45,2.50,2.55and2.60V,respectively, and discharged to0.4V at a current density of66mA g–1(Extended Data Fig.6a). For long-term cycling stability tests,an Al/PG cell using electrolyte AlCl3/ [EMIm]Cl<1.3by mole was charged/discharged at a current density of 66mA g21(Fig.1b,c in the main text).To study the rate capability of the Al/ PG cell,the current densities were varied from66to264mA g21(Extended Data Fig.7).Note that we lowered the electrolyte amount to,0.02ml per mg of cathode material and observed similar cell operation(Extended Data Fig.4). Further decrease in the electrolyte ratio is possible through battery engineering.PG foil was synthesized by pyrolysis of polyimide at high temperature,in which some covalent bonding is inevitably generated due to imperfections.Natural graphite foil was produced by compressing expanded graphite flakes,leading to stacking of natural graphite flakes by Van der Waals bonding between them.Similar battery characteristics were observed with PG and graphite foil electrodes,indicating that the battery behaviour was derived from the graphitic property of the electrodes (Extended Data Fig.8c).However,since the natural graphite foils are synthesized by compressing expanded natural graphite powders without the covalent linkage between them,these foils suffered from drastic electrode expansion obvious to the naked eye,whereas pyrolytic graphite foils showed no obvious electrode expan-sion due to covalency(Extended Data Fig.8a,b).Pouch cells were assembled in the glove box using a graphitic-foam(,3mg) cathode and an Al foil(,70mg)anode,which were separated by two layers of glass fibre filter paper to prevent shorting.Polymer(0.1mm34mm35mm)coated Ni foils(0.09mm33mm360mm in size;MTI corporation)were used as current collectors for both anode and cathode.The electrolyte(,2ml prepared using AlCl3/[EMIm]Cl51.3by mole)was injected and the cell was closed using a heat sealer.The cell was removed from the glove box for long-term cycling stability tests,in which the cell was charged/discharged at a current density of4,000mA g21 (Fig.2b,c).To determine the rate capability and fast-charge/slow-discharge beha-viours of the Al/graphitic-foam cell,various current densities from100to 5,000mA g21were used(Extended Data Fig.9and Fig.2d).The pouch cell was charged to2.42V and discharged to a cut-off voltage of0.5V to prevent the dissolution reaction of Ni foil in the ionic liquid electrolyte.Cyclic voltammetry measurements were performed using a potentiostat/galva-nostat model CHI760D(CH Instruments)in either three-electrode or two-electrode mode.The working electrode was an Al foil or a PG foil,the auxiliary electrode consisted of an Al foil,and an Al foil was used as the reference electrode.Copper tape(3M)was attached to these electrodes as the current collector.The copper tape was covered by poly-tetrafluoroethylene(PTFE)tape to prevent contact with the ionic liquid electrolyte and the part of the copper tape covered by PTFE was not immersed in the ionic liquid electrolyte.This prevented corrosion of the copper tape during cyclic voltammetry measurements.All three electrodes were placed in a plastic(1.5ml)cuvette cell(containing electrolyte AlCl3/ [EMIm]Cl51.3by mole)in the glove box,and then sealed with a rubber cap using a clamp.The scanning voltage range was set from–1.0to1.0V(versus Al) for Al foil and0to2.5V(versus Al)for graphitic material,and the scan rate was 10mV s–1(Extended Data Fig.10d).To investigate the working voltage range of the electrolyte without involving cathode intercalation,two-electrode measurement was performed by using a GC rod cathode against an Al anode in a Swagelok cell in AlCl3/[EMIm]Cl(,1.3by mole)electrolyte.The scanning voltage range was set from0to2.9V at a scan rate of10mV s–1(Extended Data Fig.6b).We investigated the Al ion cell operation mechanism and electrode reactions in the ionic liquid electrolyte,using the optimal mole ratio of AlCl3/[EMIm]Cl51.3. Using CV(Extended Data Fig.10d),a reduction wave from–1.0to–0.08V(versus Al)and an oxidation wave from20.08to0.80V(versus Al)for the anode were observed(Extended Data Fig.10d,left plot),corresponding to Al reduction/elec-trodeposition and oxidation/dissolution13,15,23–25during charging and discharging, respectively.This was consistent with Al redox electrochemistry in chloroalumi-nate ionic liquids13,15,23–25via equation(1)in the main text,and consistent with our Raman measurements,which showed both AlCl42and Al2Cl72in the electrolyte (Extended Data Fig.2b).On the graphitic cathode side,an oxidation wave of1.83 to2.50V(versus Al)and a reduction wave of1.16to2.36V(versus Al)were observed (Extended Data Fig.10d,right plot)and attributed to graphite oxidation and reduc-tion through intercalation and de-intercalation of anions(predominantly AlCl42 due to its smaller size),respectively.The oxidation voltage range of1.83to2.50V (versus Al,Extended Data Fig.10d,right plot)was close to the anodic voltage range (1.8to2.2V versus Al)of a previously reported dual-graphite cell26attributed to AlCl42intercalation in graphite.The reduction wave range of1.16to2.36V(versus Al)was assigned to the AlCl42de-intercalation26.The nature of the shoulder in the reduction curve of graphite ranging from2.36to1.9V(Extended Data Fig.10d, right plot)and a higher discharge plateau(2.25to2.0V)of an Al/PG cell upon charging(Fig.1b in the main text)remained unclear,but could be due to different stages of anion–graphite intercalation27.XRD and Raman studies of graphite cathodes during charge and discharge. For ex situ X-ray diffraction(XRD)study,an Al/PG cell(in a Swagelok configu-ration)was charged and discharged at a constant current density of66mA g–1.The reactions were stopped after30mA h g–1charged,fully charged(62mA h g–1)and 40mA h g–1discharged after charge/discharge capacities were in a stable state.Fully charged(62mA h g–1)graphitic foam was also prepared.After either the charge or the discharge reaction,the graphitic cathode was removed from the cell in the glove box.To avoid reaction between the cathode and air/moisture in the ambient atmo-sphere,the cathode was placed onto a glass slide and then wrapped in a Scotch tape.LETTERMacmillan Publishers Limited. All rights reserved ©2015。

高充放电深度锌负极

高充放电深度锌负极

高充放电深度锌负极英文回答:Deep-discharge high-rate zinc anodes are a promising technology for next-generation energy storage systems due to their high theoretical capacity (820 mAh g-1), low redox potential (-0.76 V vs. SHE), and long cycle life. However, the practical application of zinc anodes is limited bytheir poor cycling stability and low Coulombic efficiency, which are mainly attributed to the formation of zinc dendrites and side reactions with the electrolyte.Several strategies have been developed to address these challenges. One effective approach is to use a stable and conductive substrate to support the zinc deposition. Carbon-based materials, such as graphene, carbon nanotubes, and porous carbon, have been widely used as substrates for zinc anodes due to their high electrical conductivity, large surface area, and mechanical flexibility. These substrates can provide a uniform and homogeneous depositionof zinc, which can effectively suppress the formation ofzinc dendrites.Another promising strategy is to use electrolyte additives to stabilize the zinc deposition. Additives such as chloride ions, fluoride ions, and organic compounds can be added to the electrolyte to modify the surface chemistry of the zinc anode and inhibit side reactions. Chloride ions, for example, can form a stable passivation layer on thezinc surface, which can prevent the dissolution of zinc and the formation of zinc dendrites.In addition to the substrate and electrolyte design,the electrochemical deposition conditions also play acrucial role in the cycling stability and Coulombic efficiency of zinc anodes. Optimizing the deposition potential, current density, and temperature can help to achieve a more uniform and stable zinc deposition.中文回答:高充放电深度锌负极是下一代储能系统中的一种有前途的技术,它们具有高理论容量(820 mAh g-1)、低氧化还原电位(-0.76 V vs. SHE)和长的循环寿命。

规模化钠离子电池正极指标

规模化钠离子电池正极指标

规模化钠离子电池正极指标Sodium-ion batteries (SIBs) have emerged as a promising alternative to lithium-ion batteries (LIBs) due to the abundance and low cost of sodium resources. However, the development of high-performance SIBs with scalable positive electrode materials remains a significant challenge. Inthis essay, I will discuss the key requirements for achieving scalable positive electrode materials for SIBs from multiple perspectives.Firstly, one of the primary requirements for scalable positive electrode materials in SIBs is high energy density. Energy density determines the amount of energy that can be stored in a given volume or mass of the battery. To achieve high energy density, the positive electrode material should have a high specific capacity, which refers to the amountof charge that can be stored per unit mass or volume. Additionally, the positive electrode material should have a high operating voltage to maximize the energy output of the battery. Researchers are actively exploring variousmaterials, such as transition metal oxides, polyanionic compounds, and organic compounds, to achieve high energy density in SIBs.Secondly, another crucial requirement for scalable positive electrode materials in SIBs is good cycling stability. Cycling stability refers to the ability of the battery to maintain its performance over repeated charge-discharge cycles. The positive electrode material should exhibit minimal capacity decay and voltage hysteresis during cycling. This is particularly important for applications that require long battery lifetimes, such as electric vehicles and grid energy storage. Researchers are investigating strategies to improve the cycling stability of SIBs, including the design of nanostructured materials, surface modification techniques, and the use of stable electrolyte systems.Furthermore, the scalability of positive electrode materials is essential for their practical implementation in large-scale energy storage systems. Scalability refers to the ability to produce the material in large quantitiesand at a reasonable cost. The positive electrode material should be easily synthesized using low-cost and abundantraw materials, and the synthesis process should be scalable to meet the demand for large-scale production. Additionally, the positive electrode material should exhibit good electrochemical performance not only at the laboratoryscale but also when fabricated into practical electrode configurations, such as thick electrodes or electrode films.In addition to high energy density, cycling stability, and scalability, another requirement for scalable positive electrode materials in SIBs is good rate capability. Rate capability refers to the ability of the battery to deliver and accept charge at high current densities. This iscrucial for applications that require rapid charging and discharging, such as portable electronics. The positive electrode material should have a high electronic and ionic conductivity to facilitate fast charge transfer kinetics. Moreover, the material should have a well-defined and accessible sodium storage mechanism to enable rapid sodium insertion and extraction during cycling.Furthermore, the safety of positive electrode materials is of utmost importance for the widespread adoption of SIBs. The positive electrode material should be stable and non-reactive towards the electrolyte, minimizing the risk of thermal runaway and battery failure. Additionally, the material should have a high thermal stability to withstand elevated temperatures during battery operation or in the case of external thermal abuse. Researchers are exploring the use of novel materials and protective coatings to enhance the safety of SIBs and mitigate the risk of electrode degradation or thermal runaway.Lastly, the environmental impact of positive electrode materials should also be considered. Sustainable and eco-friendly materials should be prioritized to minimize the environmental footprint of SIBs. This includes the use of non-toxic and abundant raw materials, as well as the development of recycling processes for spent electrode materials. By considering the environmental impact, SIBscan be developed as a more sustainable energy storage solution compared to LIBs.In conclusion, achieving scalable positive electrode materials for SIBs requires addressing several key requirements such as high energy density, cycling stability, scalability, rate capability, safety, and environmental impact. These requirements are crucial for the practical implementation of SIBs in various applications, rangingfrom portable electronics to large-scale energy storage systems. Continued research and development efforts are needed to overcome the current challenges and unlock thefull potential of sodium-ion batteries as a viable alternative to lithium-ion batteries.。

峰值放电电流英语

峰值放电电流英语

峰值放电电流英语Peak discharge current, often referred to as peak current, is a crucial parameter in the evaluation of batteries, capacitors, and other energy storage devices. It represents the maximum amount of current that can be safely discharged from a device in a short duration, typically measured in amperes (A). Understanding peak discharge current is essential for ensuring the reliability, efficiency, and safety of these devices across various applications.In batteries, peak discharge current is a measure of how quickly energy can be released. It is particularly important in high-drain applications such as flashlights, power tools, and electric vehicles where a rapid burst of power is required. A battery with a high peak discharge current rating can deliver more power in a shorter time, thus enabling devices to perform better under demanding conditions.Capacitors, on the other hand, are known for their ability to store and release energy quickly. Peak discharge current is a critical factor in determining the speed andefficiency of capacitor-based systems. For instance, in power electronics, capacitors with high peak discharge capabilities are essential for smoothing out voltage fluctuations and providing instant power during transients. When designing electronic systems, engineers must carefully consider the peak discharge current requirements of the components involved. Selecting components with inadequate peak current ratings can lead to performance issues, component failure, or even safety hazards. Conversely, components with higher peak current ratings can ensure reliable and efficient operation, even under extreme conditions.To ensure peak discharge current ratings are met, engineers often utilize advanced testing and simulation techniques. These methods allow them to accurately predict the peak current capabilities of components under various conditions, enabling informed decisions about component selection and system design.In conclusion, peak discharge current is a fundamental parameter in the evaluation and selection of batteries, capacitors, and other energy storage devices. Understandingits importance and implications for system performance, reliability, and safety is crucial for ensuring the effective design and operation of electronic systems across a wide range of applications.**峰值放电电流:理解与应用**峰值放电电流,通常称为峰值电流,是评估电池、电容器和其他储能设备的关键参数。

不同放电倍率磷酸铁锂电池循环性能研究

不同放电倍率磷酸铁锂电池循环性能研究

不同放电倍率磷酸铁锂电池循环性能研究唐进;徐国锋;李建玲【摘要】磷酸铁锂电池的容量、能量、内阻和开路电压是其性能的重要指标,也是涉及电池管理系统设计的重要参数.这些特性均与电池充放电倍率紧密相关.通过对40℃下不同放电倍率的LiFePO4锂离子电池的容量、能量、交流阻抗和开路电压等循环性能试验,研究不同放电倍率循环下以上特性的变化规律.结果表明,电池放电容量与放电倍率间满足幂函数规律;高倍率下循环,电池容量衰减更快;在循环过程中,放电倍率对电池的欧姆阻抗和电化学阻抗的影响程度不同,欧姆内阻受倍率影响很小,电化学阻抗则随着放电倍率升高,增加越快;另外,在循环后期,放电倍率越高,开路电压下降越快;大电流下,电池放出能量降低,产热增加,老化加快,寿命降低.%The capacity, energy, internal resistance and open-circuit voltage are key indicators to represent the performance of lithium iron phosphate battery and important parameters in battery management system (BMS) design as well.These characteristics are closely related to the charge and discharge rate. The cycling performance of the LiFePO4 battery at different discharge rates was tested at 40℃in terms of battery capacity, energy,AC impedance and open-circuit voltage to investigate their changing laws in the circulation of different discharge rates. The result shows that the relation between discharge capacity and discharge rate follows the rule of power function;battery capacity declines more quickly with a high rate of circulation;the discharge rate has different influences on ohmic impedance and electrochemical impedance of the battery in the course of circulation, that is, the ohmic impedance is little affected by the rate but theelectrochemical impedance increases quickly with the rate rising; in addition,the higher the discharge rate,the faster the open-circuit voltage falls in the late cycle;the battery emits less energy,with its heat production increasing,burn-in accelerating and lifetime decreasing in a large current.【期刊名称】《有色金属科学与工程》【年(卷),期】2017(008)005【总页数】8页(P95-102)【关键词】磷酸铁锂电池;放电倍率;容量;交流阻抗;开路电压;能量【作者】唐进;徐国锋;李建玲【作者单位】北京科技大学冶金与生态工程学院,北京 100083;北京科技大学冶金与生态工程学院,北京 100083;北京科技大学冶金与生态工程学院,北京 100083【正文语种】中文【中图分类】TM911.14;TF111.52自锂离子电池问世以来,有关它的研究和发展一直是全世界关注的焦点.锂离子电池作为一种可重复使用的环保电池,它是通过锂离子在正负极间相互脱嵌来完成电量转化过程,具有循环寿命长、工作电压高和能量密度大等许多优点[1-5].近年来,由于锂离子电池技术的不断进步,使得它在便携式电子设备、电动汽车和军事航天等领域均获得了广泛的应用[6-8].在现有的各种电池体系中,磷酸铁锂电池的原料来源更加丰富、成本更低、循环寿命最长、安全性更好,无疑是目前最具发展潜力的电池体系[9-13].电池的容量、能量、内阻和开路电压等是反映其性能的重要指标,也是电池管理系统设计的重要参数.电池容量的变化规律,会直接影响到电池的寿命管理和荷电状态估算[14-15];电池内阻大小的变化主要影响动力电池的功率和产热特性[16-17];而开路电压(O pen circuit voltage,OCV)曲线可以参与电池荷电状态的估算以及电池健康状态的评价,便于电池的应用优化和性能维护,进而提高电池管理系统(BMS)的使用效率[18-20].文中研究了磷酸铁锂动力电池在不同放电倍率下的容量衰减情况,并且在循环过程中测试了对应条件下的电化学交流阻抗和电池开路电压,分析了交流阻抗及开路电压与电池循环圈数间的变化规律,为电池健康状态的评价和电池寿命快速预测系统的建立提供技术上的支持.实验采用的电池为天津力神公司生产的18650型商用LiFePO4锂离子电池,标准电压范围2.0~3.65 V,标称容量为1 350 mAh,标准放电倍率为0.2 C.用5 V/5 A蓝电电池充放电测试系统(武汉产)进行充放电.恒温箱为某国产高低温调湿实验箱,为电池充放电实验提供恒定的环境温度.交流阻抗测试采用瑞士万通Auto Lab Pgstat302N电化学工作站.将待测电池放置于25℃恒温干燥箱中,使用不同放电倍率对电池进行放电实验,充电过程采用先恒流再恒压的模式,放电过程采用恒流模式,研究电池放电容量与放电倍率间关系.充电方式为,将电池以1 C电流恒流充电至电压为3.65 V,转恒压充电至电流小于0.05 C(65 mA)时,停止充电.将电池充满电后,在25℃的环境温度下静置1 h,再分别以0.1 C、0.2 C、0.5 C、1 C、1.5 C、2 C电流恒流放电至电压为2.0 V时,停止放电,计算电池的放电容量.适当的提高电池循环时环境温度,可以加速电池的老化,减少测试时间,便于比较不同倍率下电池特性的变化规律.因此,在40℃环境温度下对实验电池进行不同倍率充放电循环实验,充电方式均采用1 C恒流充电至上限电压3.65 V,转恒压充电至电流小于0.05 C后,停止充电,静置0.5 h.为了研究放电倍率对锂离子电池的影响,将放电过程分为3组,静置完成后,第1组以0.5 C恒流放电至下限电压2.0 V后,停止放电,静置0.5 h.以1次完整的充放电过程为1个周期,进行循环实验.第2、第3组实验分别采用1 C和2 C放电倍率进行循环实验,其他条件均与第1组实验相同.电池每循环50个周期时进行一次标准放电容量测定.当电池的循环周期达到0次、50次、100次、200次、300次、400次、500次时,进行一次交流阻抗测试.标准放电容量测试的步骤如下:在25℃恒温箱中,以1 C恒流充电至上限电压3.65 V,转恒压充电至电流小于0.05 C后,停止充电,静置0.5 h.再以1 C恒流放电至下限电压2.0 V,停止放电,计算电池放出的容量.交流阻抗测试(EIS),电池进行交流阻抗测试时均处于放空电状态.实验采用恒电势EIS法,设置电势值为电池开路电压,扫描的频率范围为100 kHz~10 mHz,正弦电压振幅值为10 mV,测试电池处于不同循环周期的交流阻抗谱,建立相应合适的等效电路进行拟合分析,得到电池各阻抗参数与循环周期间的变化规律.图1所示为LiFePO4动力电池在25℃的环境温度下分别以0.1 C、0.2 C、0.5 C、1 C、1.5 C和2 C不同倍率的放电曲线.可知,LiFePO4电池不同倍率下的放电过程均存在一个稳定的放电平台,平台电压介于3.0~3.4 V之间,另外,平台电压随着放电倍率的增加而降低,这是因为放电倍率的增加,增大了电池的放电电流,又由于电池内阻的存在,造成电池放电时电压将会增大.另一方面,大倍率电流放电还会使电池的极化增大,也会使电池的电压平台降低.LiFePO4电池在不同放电倍率下放电放出的容量如图2所示.电池放出的容量会随着电池放电倍率的增加而减小.在0.1 C的小倍率下电池放出的容量比电池的标称容量有所增大,而在2 C倍率下放电容量仅为标称容量的90%.由此说明,放电倍率与电池放出的容量之间具有一定的负相关性.1897年,Peukert[20]在对铅酸电池的恒流放电试验中发现恒流放电电流与持续放电时间/容量关系的经验公式,其方程表示如下:式(1)中,I为放电电流,p为Peukert系数,t为最大放电时间.此公式给出了电池放电电流与最大放电时间的关系,但在实际应用过程中对于最大放电时间不好界定,研究人员对其进行修正,将电池最大放电时间与电池的放电容量联系起来,推出了电池放出容量与电池电流满足幂函数关系,而放电电流与放电倍率满足线性对应关系,进一步得出电池放电容量与电池的放电倍率间满足幂函数规律.将电池放电容量与放电倍率进行曲线拟合,得到如下关系式:式(2)中,Q是电池放电容量,K是放电倍率,X2是该拟合的相关系数.它表示拟合曲线与原数据的吻合程度,其数值在0~1之间,X2越大时,曲线拟合的吻合度就越好;反之,则拟合的越差.图2中容量与放电倍率采用幂函数拟合后的拟合相关系数为0.992 5,说明容量与放电倍率之间是符合幂函数规律.为了研究不同倍率循环过程中的放电容量变化规律,对不同循环次数的电池进行了充放电倍率均为1 C的容量测定.图3所示为电池在40℃环境温度下0.5 C、1 C和2 C倍率循环后每隔50次周期所测的标准放电容量.从图3中可知,电池在整个500次循环过程中放电容量呈现2个阶段的变化趋势.在循环前100圈,0.5 C、1 C和2 C倍率下的电池标准放电容量均逐渐上升,循环100次时放电容量达到最大值,在此阶段电池的容量变化规律基本保持一致.但循环次数大于100次时,电池的放电容量才开始衰减,且不同倍率下的衰减程度不同.以循环100次测得电池最大放电容量为电池的额定放电容量,计算电池处于不同倍率循环周期时的容量衰减率,绘制容量衰减率与循环周期关系曲线,如图4所示.500次循环周期后,2 C放电倍率的电池放电容量衰减率为其额定放电容量的12.8%,放电倍率为0.5 C、1 C的电池放电容量衰减率分别达到6.3%和9.6%.在2 C倍率下循环的电池其容量衰减曲线斜率要高于0.5 C和1 C.由此表明,电池在较高倍率下循环容量衰减更快,放电倍率对电池的循环放电容量的影响很大.图5(a)、图5(b)和图5(c)分别为电池在40℃下,经过0.5 C、1 C和2 C 放电倍率循环后,在放电态下不同循环周期的EIS图谱,可知,所有EIS图均是由高频区的直线段、中高频区的圆弧段和低频区的斜线段3部分组成,分别对应感抗部分、电荷转移部分和扩散部分的阻抗特征.前100次的电池循环过程中,3组放电倍率循环下的EIS图整体均向左偏移,其中低频区的扩散斜率偏移程度最大.在100~500次的循环过程中,组成EIS的各部分阻抗又逐渐增加.由此表明,电池在循环前期处于活化阶段,活化结束后,继续循环,电池处于逐渐衰退状态.为了研究循环过程中各部分的阻抗的变化规律,可采用图6所示的等效电路对交流阻抗数据进行拟合,其中L表示感抗;Rs为欧姆阻抗,包括电池的电解液、隔膜、集流体及其与正负极界面的阻抗等;Rct为由电荷传递作用产生的电化学阻抗,包括正负极的电极反应阻抗;Qdl代表电极反应的界面电容;CPE为常相角元件,表示电荷扩散阻抗的常相位角元件.通过图6的等效电路模拟,电池在不同放电倍率循环下不同循环次数的欧姆阻抗(Rs)及电化学阻抗(Rct)变化情况如图7和图8所示.在循环前期,欧姆内阻迅速减小,100次循环后又逐渐增大,由此表明,电池循环的前期是一个内部活化的阶段,电池内部的各组分处于调整过程,包括电解液渗入电极内部、活性材料的均匀分布和电极结构的空间排列紧凑等,这些因素共同导致电池欧姆内阻的减小.继续循环,电池内部副反应增多,导致电解液逐渐被消耗.另外,电极材料在反复充放电过程中使电极结构变得疏松或者SEI膜的破坏等,均有可能增大电池欧姆阻抗.电池循环前期,Rct的值先迅速减小,100次循环后逐渐趋于稳定,但200次循环后又逐渐增加,这一结果与欧姆内阻的变化规律基本相近,随着电池循环前期的活化,电极活性材料的结构将更适宜锂离子脱嵌过程,正负极的电极反应更易发生.循环继续进行,电池的内部结构又逐渐劣化,使锂离子在电池内部脱嵌的难度增大,造成电池的电化学阻抗增加.整个循环过程中,电池的欧姆阻抗和电化学阻抗都随着循环次数的增加遵循先减小后增大的规律,这也与容量分析的结果一致. 通过图7和图8比较可知,不同放电倍率下循环得到的欧姆阻抗变化趋势基本一致,但电化学阻抗的变化情况受放电倍率影响很大,在充放电前期主要受电池的活化作用影响,因此电化学阻抗在各放电倍率下变化基本一致,但随着电池内部结构充分活化之后,放电倍率对电化学阻抗的影响较大,且倍率越高,电池的电化学阻抗增加越快.这一现象表明,放电倍率对电池的电极极化作用影响较大,而对电池内部结构的改变影响较小.图9所示为电池处于不同放电倍率不同循环周期的欧姆阻抗与电化学阻抗加和得到的电池阻抗(Rtol)曲线.可知,在整个500次循环中,电池内阻在循环前期先快速下降,继续循环后又逐渐增加.放电倍率对电池内阻的影响主要集中在电池衰退阶段,而在循环的活化阶段影响较小.电池开路电压(Open circuit voltage,OCV)是指电池处于未接负载的开路状态时电池两极的端电压,是反映电池基本性能的重要特性.图10所示为电池在不同放电倍率循环后电池处于放电态下静置12 h后测得的开路电压曲线.从曲线上可以看出,电池在前100次循环时开路电压缓慢减小,100次到200次开路电压迅速下降,200次后电池开路电压基本保持不变,400次后电池的开路电压又开始快速下降.这一变化趋势表明,在循环前期(100次以内),电池开路电压受循环次数的影响较小,这进一步验证了电池循环前期是一个电池的活化过程.继续循环,电池开路电压呈现先快速下降再保持不变最后又快速下降的趋势,这主要是由于在循环过程中正负极的结构发生改变以及活性锂离子的损失而引起的.另外,比较图10中3组放电倍率下的开路电压曲线可知,放电倍率对电池开路电压的影响主要分布在循环400次以后,且放电倍率越高,开路电压下降越快.图11所示为循环500次后不同放电倍率下测得的开路电压与荷电状态(SOC,state of charge)的关系曲线.由图11曲线可知,电池在循环500次后电池开路电压随电池荷电状态的变化规律分成3个区段.当电池的SOC值低于0.3时,电池的开路电压值变化较大,且SOC值越小,开路电压值下降的越快;在0.3~0.9 SOC的中间区段,开路电压曲线缓慢上升,电池开路电压变化很小;SOC大于0.9时,电池开路电压又快速升高.比较不同放电倍率下的电池开路电压曲线可以发现,开路电压会随着放电倍率的增大而升高,但升高的幅度较小,也就是说,放电倍率对电池的开路电压的影响很小,低倍率下电池的开路电压较低.锂离子电池在放电循环过程中,一方面需要向外部输出电能,同时由于电池内部阻抗和电化学反应的存在也会产生热能,这2部分的能量都是以化学能的形式储存在电池内部,化学能的多少不仅跟电池内部各部件的材料结构与活性相关,还受温度、充放电电流以及循环次数等影响.图12(a)反映了电池在不同倍率下循环后测得的放电能量.由图12(a)可知,放电能量的变化规律,同容量变化趋势基本一致,循环前100圈,不同放电倍率下的电池放电能量均增加,且所发出的能量基本相等.这说明在这一阶段,电池的放电倍率对放电能量的影响较小,此时放电倍率不是放电能量的主要影响因素.100圈循环之后,电池放出的能量会随着循环次数的增加而逐渐下降,且不同放电倍率的能量下降速率不一样,在高倍率下放电能量下降更快,此时放电倍率对电池循环放电能量的影响很大.锂离子电池主要有4个热量的来源:欧姆热、电化学反应热、极化热以及副反应热.一般而言,电池正常使用时,发生的副反应较少,并且充放电过程中,锂离子电池的电化学反应热较低,在计算总热量时,可以忽略不计.锂离子电池的欧姆热是电池在充放电过程中由于电池内部的欧姆内阻在电流的作用下产生的热量,其计算公式为:式(3)中:Qj为焦耳热,J;I为充放电电流,A;t为充电时间,s;Rs为欧姆内阻,Ω.极化热计算公式:式(4)中:Qp为极化热,J;I为充放电电流,A;t为充电时间,s;Rp为极化内阻,Ω.总热量计算公式:式(5)中:Q为总热量,J.将不同循环周期后的电池,通过直流脉冲法测量电池在不同放电深度下的直流阻抗.整个放电过程分为20个放电深度,每次放出5%的电量,再以大电流对电池进行短时间恒流放电,根据该过程中电压的变化计算出电池的直流欧姆内阻和直流极化内阻.当放电深度足够小时,可认为其直流阻抗值近似恒定.以电池在不同放电深度下的直流欧姆阻抗和直流极化阻抗分别计算出电池处于不同SOC区间段内的欧姆热和极化热,将全部SOC区间段内的欧姆热和极化热分别加和,可得整个放电过程的焦耳热与极化热.图12(b)、图12(c)和图12(d)分别是根据上述热量公式计算得到的焦耳热、极化热以及总热量的循环关系曲线.从图12中可知,在低倍率下,电池的焦耳热、极化热以及总热量随循环次数的增加基本保持不变,这是因为低倍率下循环时,放电电流较小,电池的极化程度低,对电池的内部结构影响较小,电池内部各阻抗值变化不大.增大电池放电倍率,放电电流增大,极化程度也加大,随着循环次数增加,电池内部结构受到的影响加剧,电池内部的阻抗值也就逐渐增大,因此产热也会逐渐增多.另外,在相同的循环次数下,大电流放电也会造成热量增加,这会使电池内部温度升高,电池的老化加快.通过研究磷酸铁锂电池的不同放电倍率下容量、交流阻抗与开路电压特性,得到了不同放电倍率循环下各特性的变化规律.1)磷酸铁锂电池的容量受放电倍率的影响较大,放电倍率越高,电池放出的容量越少,且电池放出容量与电池的放电倍率间满足幂函数规律.2)不同倍率循环过程中电池放出容量随循环次数的增加呈现先增后减的变化规律,电池在较高倍率下循环容量衰减更快,放电倍率对电池的循环放电容量的影响很大. 3)循环过程中,放电倍率对电池欧姆内阻影响不大,而对电池的电化学阻抗影响明显,在电池经过充分活化过后,放电倍率越高,电池的电化学阻抗增加越快. 4)电池的开路电压在循环后期受电池放电倍率的影响较大,且放电倍率越高,开路电压下降越快.5)放电倍率与电池的放电能量以及热量存在明显的相关性,高倍率下电池放出的能量较少,热量产生较多,老化速度加快,使用寿命降低.电池在不同放电倍率条件下循环的容量、内阻和能量特性差别很大,因此,对电池的容量的估算要考虑倍率带来的影响;电池在大电流条件下使用时易造成极化程度增加和电池内部材料老化加快;磷酸铁锂电池在高倍率下循环性更差;电池的开路电压在不同循环阶段受放电倍率影响程度不一.这些结论明确了磷酸铁锂电池的倍率循环性能特性,对电池的管理技术和寿命研究具有十分重要的意义.【相关文献】[1] 韦连梅,燕溪溪,张素娜,等.锂离子电池低温电解液研究进展[J].储能科学与技术,2017,6(1):69-77.[2] SCROSATI B,GARCHE J.Lithium batteries:status,prospects and future[J].Journal of Power Source,2010,195(9):2419-2430.[3] 段建锋.20Ah富锂锰动力电池的性能研究[J].有色金属科学与工程,2013,4(2):37-41.[4] 赵世玺,郭双桃,赵建伟,等.锂离子电池低温特性研究进展[J].硅酸盐学报,2016,44(1):19-28.[5] 孙艳霞,周园,申月,等.动力型锂离子电池富锂三元正极材料研究进展[J].化学通报,2017,80(1):34-40.[6] 李恒,张丽鹏,于先进,等.锂离子电池正极材料的研究进展[J].硅酸盐通报,2012,31(6):1486-1490.[7] 汤雁,刘攀,徐友龙,等.锂离子正极材料的研究现状与发展趋势[J].电子元件与材料,2014,33(8):1-6.[8] 闫金定.锂离子电池发展现状及其前景分析[J].航空学报,2014,35(10):2767-2775.[9] 杨见青,关杰,梁波,等.我国废弃磷酸铁锂电池的资源化研究[J].环境工程,2017,35(2):127-132.[10] 张克宇,姚耀春.锂离子电池磷酸铁锂正极材料的研究进展[J].化工进展,2015,34(1):166-171.[11] 刘冬生,陈宝林.磷酸铁锂电池特性的研究[J].河南科技学院学报,2012,40(1):65-68.[12] 杜江,张正富,彭金辉,等.动力锂离子电池正极材料磷酸铁锂的研究进展[J].新能源进展,2013,1(3):263-268.[13] 郭红霞,乔月纯,穆培振,等.锂离子电池正极材料研究与应用进展[J].无机盐工业,2016,48(3):5-8.[14] 詹世安,汤宁平,王建宽,等.磷酸铁锉电池荷电状态估算方法研究[J].无机盐工业,2015,39(8):1620-1624.[15] 李哲,韩雪冰,欧阳明高,等.动力型磷酸铁锂电池的温度特性[J].机械工程学,2011,47(18):115-120.[16] 匡勇,刘霞,钱振,等.锂离子电池产热特性理论模型研究进展[J].储能科学与技术,2015,4(6):599-608.[17] 李海英,贾永丽,张丹,等.动力磷酸铁锂电池产热特性研究[J].电源技术,2016,140(5):968-971.[18] MARTIN-MARTIN L,GASTELURRUTIA J,NIETO N,et al.Modeling based on design of thermal management systems for vertical elevation applications powered by lithium-ion batteries[J].Applied Thermal Engineering,2016,102(5):1081-1094.[19] 许守平,侯朝勇,胡娟,等.储能用锂离子电池管理系统研究[J].电网与清洁能源,2014,30(5):70-78.[20] PEUKERT W.ber die Abhängigkeit der Kapacität von der Entladestromstärcke beiBeiakkumulatoren[J].Elektrotechnische Zeitschrift,1897,20:20-21.。

非晶卤化物电解质

非晶卤化物电解质

非晶卤化物电解质【中英文实用版】Title: Amorphous Halide Electrolytes任务标题:非晶卤化物电解质Amorphous halide electrolytes have garnered significant attention as a promising candidate for next-generation battery technology.Their unique properties, such as high ionic conductivity and good chemical stability, make them highly suitable for use in energy storage devices.非晶卤化物电解质作为下一代电池技术的有力候选者,已经引起了广泛关注。

它们独特的性质,如高离子导电性和良好的化学稳定性,使其非常适合用于储能设备。

Research has shown that amorphous halide electrolytes can exhibit superior ionic conductivity compared to traditional crystalline electrolytes.This is due to the absence of a regular lattice structure in amorphous materials, which allows for more efficient ion movement.研究表明,与传统的晶体电解质相比,非晶卤化物电解质可以展现出更优越的离子导电性。

这是因为非晶材料中缺乏规则的晶格结构,从而使得离子运动更加高效。

Furthermore, the flexibility of the halide anions in amorphous electrolytes contributes to their high thermal stability.This is crucial for battery applications, as it ensures that the electrolyte remains stable over a wide range of temperatures.此外,非晶电解质中卤素阴离子的灵活性为其提供了较高的热稳定性。

高温固相法一步合成碳包覆钛酸锂

高温固相法一步合成碳包覆钛酸锂

高温固相法一步合成碳包覆钛酸锂袁敏娟;阚素荣;卢世刚【摘要】以纳米二氧化钛(TiO2)、碳酸锂(Li2CO3)、蔗糖(C12H22O11)为原料,以去离子水作混合溶剂,以氩气(Ar)作为保护气,高温固相合成了碳包钛酸锂(Li4Ti5O12/C)材料.采用XRD、SEM和电化学测试等方法分别对合成材料的结构、形貌和电化学性能进行了表征.结果表明:与传统的高温固相法合成的钛酸锂相比,碳包覆钛酸锂的颗粒明显减小,一次颗粒平均粒度为82 nm;碳包覆钛酸锂放电比容量明显提高,0.1 C、1.0 C、5.0 C倍率下的放电质量比容量分别为171.3、162.3、157.8 mAh/g,循环20周后的容量保持率为100%.%The Li4Ti5O12/C material was synthesized by high temperature solid state with Li2CO3,TiO2 and sucrose (C12H22O11) as raw material,with deionized water as mixed solvent,with argon as protective gas.The crystalline structure,morphology and electrochemical performances of the sample were investigated by X-ray diffraction,scanning electron microscope and charge discharge test.The results show,compared with lithium titanate synthesized by traditional high temperature solid state,the particle size of carbon coating lithium titanateis obviously smaller.The average particle size of the primary particle is only 82 nm.The discharge specific capacity of carbon coating lithium titanate is obviously higher,and the discharge specific capacity are 171.3,162.3,157.8 mAh/g by the charge-discharge rate of 0.1 C,1 C,5 C respectively,and the capacity retention rate is 100% after 20 cycles.【期刊名称】《电源技术》【年(卷),期】2018(042)003【总页数】3页(P333-334,342)【关键词】钛酸锂;负极材料;碳包覆;粒度【作者】袁敏娟;阚素荣;卢世刚【作者单位】国联汽车动力电池研究院有限责任公司,北京100088;国联汽车动力电池研究院有限责任公司,北京100088;国联汽车动力电池研究院有限责任公司,北京100088【正文语种】中文【中图分类】TM9141971年法国Deschanvre等合成出Li1/3Ti5/3O4(x=0~1/3)。

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High-rate electrochemical energy storage through Li +intercalation pseudocapacitanceVeronica Augustyn 1,Jérémy Come 2,3,Michael A.Lowe 4,Jong Woung Kim 1,Pierre-Louis Taberna 2,3,Sarah H.T olbert 5,Héctor D.Abruña 4,Patrice Simon 2,3and Bruce Dunn 1*Pseudocapacitance is commonly associated with surface or near-surface reversible redox reactions,as observed with RuO 2·x H 2O in an acidic electrolyte.However,we recently demonstrated that a pseudocapacitive mechanism occurs when lithium ions are inserted into mesoporous and nanocrystal films of orthorhombic Nb 2O 5(T -Nb 2O 5;refs 1,2).Here,we quantify the kinetics of charge storage in T -Nb 2O 5:currents that vary inversely with time,charge-storage capacity that is mostly independent of rate,and redox peaks that exhibit small voltage offsets even at high rates.We also define the structural characteristics necessary for this process,termed intercalation pseudocapacitance,which are a crystalline network that offers two-dimensional transport pathways and little structural change on intercalation.The principal benefit realized from intercalation pseudocapacitance is that high levels of charge storage are achieved within short periods of time because there are no limitations from solid-state diffusion.Thick electrodes (up to 40µm thick)prepared with T -Nb 2O 5offer the promise of exploiting intercalation pseudocapacitance to obtain high-rate charge-storage devices.Pseudocapacitance occurs whenever the charge (Q )depends on the change in potential (d E ),yielding a capacitance (d Q /d E )(ref.3).The capacity can be due to monolayer adsorption of ions at an electrode surface,as in the underpotential deposition of metals 4;surface redox reactions as in RuO 2;or ion intercalation that does not result in a phase change.Although these redox processes are Faradaic in nature,their phenomenological behaviour,and response to experimental variables such as sweep rate,are those typical of capacitors.All of these scenarios produce a relationship between the fractional extent of charge storage,X ,and the potential of the form 3,5:E ∼RT nF ln X (1−X )(1)where R is the ideal gas constant (J mol −1K −1),T is the temperature (K),F is Faraday’s constant (96,485As mol −1)and n is the number of electrons involved in the reaction.In all of these cases,a constant-current experiment yields a potential E that changes with the extent of charge Q according to:Q =C Ewhere Q is the charge passed (Coulombs), E is the potential change (V)and C is the pseudocapacitance (F).This behaviour1Departmentof Materials Science and Engineering,University of California,Los Angeles,California 90095,USA,2Department of Materials Science,UniversitéPaul Sabatier,CIRIMAT UMR CNRS 5085,T oulouse 31062,France,3Réseau sur le Stockage Electrochimique de l’Energie (RS2E),FR CNRS 3459,France,4Department of Chemistry and Chemical Biology,Cornell University,Ithaca,New York 14853,USA,5Department of Chemistry and Biochemistry,University of California,Los Angeles,California 90095,USA.*e-mail:bdunn@ .is typical of capacitive charge/discharge,thus leading to theterm pseudocapacitance 3.Of the three pseudocapacitive mechanisms mentioned above,underpotential deposition and surface redox reaction pseudoca-pacitance exhibit kinetics indicative of surface-controlled electro-chemical processes 6:i =Cvwhere i is the current (A)and v is the sweep rate (mV s −1)of a cyclic voltammetry experiment.However,in intercalation pseudocapacitance,as described herein,charge storage does not occur on the surface but in the bulk material.The kinetics are not diffusion-limited and instead are limited by surface processes so that the overall behaviour seems capacitive.Intercalation pseudocapacitance is rarely observed because in most intercalation materials charge storage (even in thin films,as in anatase TiO 2;refs 7,8)is limited by solid-state diffusion and therefore the peak currents scale with v 1/2.Here we investigate the phenomenon of intercalation pseudo-capacitance and the high-rate behaviour of T -Nb 2O 5using two different electrode techniques that provide a wide variation in sweep rates.For timescales between ∼3h and 60s (sweep rates of 0.1–20mV s −1within a voltage window of 1.2V),we used a thin-film electrode.For shorter timescales where ohmic polariza-tion is significant (60–500mV s −1),we used a cavity microelectrode where the active material was mixed with a conductive carbon black to alleviate the loss of electrical transport (ohmic losses)9.To confirm the small ohmic drop of this electrode,we performed cyclic voltammetry from 100–500mV s −1in a bulky-ion electrolyte (Sup-plementary Fig.S1).In addition,we prepared thick films (∼40µm)of T -Nb 2O 5to determine whether the high-rate capability was limited to thin films.Charge storage from the intercalation of lithium ions into Nb 2O 5can be expressed as:Nb 2O 5+x Li ++x e −↔Li x Nb 2O 5where the maximum capacity is x =2(ref.10).Figure 1a shows cyclic voltammograms from 100to 500mV s −1in a cavity microelectrode where it is evident that both anodic and cathodic peaks are broad,about 600mV.There is also a noticeable peak shift (and increase in peak separation E p )as the sweep rate increases,but the capacity remains reversible.Figure 1b presents a plot of log(i )versus log(ν)from 0.1to 500mV s −1for both cathodic and anodic peaks.Assuming that the current obeys a power-law1 × 10aC u r r e n t (m A )N o r m a l i z e d c a p a c i t ySweep rate ¬1/2 (s 1/2 mV ¬1/2)¬1 × 10log(sweep rate, mV s ¬1)cFigure 1|Kinetic analysis of the electrochemical behaviour of T -Nb 2O 5.a ,Cyclic voltammograms from 100to 500mV s −1demonstrate the high-rate capability of the material.b ,b -value determination of the peak anodic and cathodic currents shows that this value is approximately 1up to 50mV s −1.This indicates that even at the peak currents,charge storage is capacitive.c ,Capacity versus v −1/2allows for the separation of diffusion-controlled capacity from capacitive-controlled capacity;two distinct kinetic regions emerge when the sweep rate is varied from 1to 500mV s −1.The dashed diagonal line corresponds to the extrapolation of the infinite sweep rate capacitance using the capacity between 2and 20mV s −1.d ,The variation of the cathodic peak voltage with the sweep rate exhibits a region of small peak separation followed by increased separation at 20mV s −1,and represents another method of identifying systems with facile intercalation kinetics.relationship with the sweep rate leads to 8:i =av bnumerous sources including an increase of the ohmic contribution (active material resistance,solid–electrolyte interphase resistance)and/or diffusion constraints/limitations 11.In the limit of slow diffusion,b would approach a value of 0.5as described above.The relationship between capacity and sweep rate can also establish the rate-limiting step of a charge-storage mechanism 12.In a plot of Q versus v −1/2,regions that are linear represent capacity limited by semi-infinite linear diffusion whereas capacitive contributions are independent of the sweep rate.At sweep rates below 20mV s −1,the extrapolated y -intercept yields the infinite sweep rate capacitance 13.Figure 1c shows the plot of normalized capacity versus v −1/2for T -Nb 2O 5from 1to 500mV s −1(the gravimetric capacity for the thin-film electrode is shown in Supplementary Fig.S2).Analogous to the behaviour of the peak current in Fig.1b,there are two distinct regions in Fig.1c.In region 1,at sweep rates <20mV s −1,the capacity is mostly independent of sweep rate.The magnitude of the capacity is ∼130mAh g −1or ∼65%of the theoretical value based on a two-electron redox reaction with Nb 2O 5.In this range,solid-state lithium-ion diffusion is not the rate-limiting step for charge storage.In region 2,from 50to 500mV s −1,the capacity decreases linearly with v −1/2.This indicates that charge storage is mainly diffusion-controlled at high sweep rates.That is,for charging timesabC rateP o t e n t i a l (V v e r s u s L i /L i +)Capacity (mAh g ¬1)x in Li x Nb 2O 51.21.51.82.12.42.73.0Figure 2|Electrochemical cycling of a 40-µm-thick T-Nb 2O 5electrode.a ,Galvanostatic cycling of a thick Nb 2O 5electrode at a 10C rate.b ,Comparisonof the rate capability of T -Nb 2O 5with a high-rate lithium-ion anode,Li 4Ti 5O 12,at various C-rates (Li 4Ti 5O 12data reproduced from ref.16).of <20s,diffusion is rate-limiting,similar to most traditional battery electrodes.However,for charging times of 1min (60C)or longer,there is no indication of diffusion limitations and this intercalation-based system behaves in a fully capacitive manner.Another feature of T -Nb 2O 5at sweep rates <20mV s −1is that the peak voltage shifts with sweep rate are small (Fig.1d).The cathodic peak shift is <0.1V at sweep rates below 10mV s −1.As a result,the anodic and cathodic peaks overlap at 0.1mV s −1(Supplementary Fig.S3)and it is in this behaviour that the similarity to surface redox reactions is most apparent 14.In many lithium-ion intercalation materials,the peak separation is significant even in thin films and at slow sweep rates (for example, E p =0.13V for LiCoO 2at 0.1mV s −1;ref.15).This type of behaviour is often associated with crystallographic phase changes during the Faradaic process,and contrasts with intercalation materials that form a solid solution,such as T -Nb 2O 5.Besides identifying facile intercalation,the peak voltage separation is related to the high-power capability of a material.As the charging time decreases,that is,at higher current densities,the peak separation in a battery material increases owing to polarization (reflecting the higher overpotentials necessary to deliver the higher currents),so that at higher rates the energy required to fully charge the material is significantly larger than the energy available on discharge.The high-rate behaviour of T -Nb 2O 5is not limited to thin films or to experiments with small amounts of active material.The constant-current charge/discharge of a 40-µm-thick T -Nb 2O 5(1mg cm −2)electrode at a 10C rate is shown in Fig.2a.At this rate,the capacity is 130mAh g −1and E varies linearly with Q as expected for a pseudocapacitive process from equation (1).This represents capacities typical of battery materials but at rates closer to those of supercapacitors.The rate capability of T -Nb 2O 5from 1to 1,000C is shown in Fig.2b and compared with that of Li 4Ti 5O 12(of comparable electrode dimensions)16.Li 4Ti 5O 12is chosen as an example of a high-rate lithium-ion anode material.The rate capability for T -Nb 2O 5is significantly better than Li 4Ti 5O 12above 30C and even at a 1,000C rate the capacity of the thick T -Nb 2O 5electrode is ∼40mAh g −1.The thick electrode results verify that the intercalation pseudocapacitance mechanism is not due to thin-film or surface effects,such as vacancies or contributions of the first few atoms from the surface.Indeed,even for the thick electrode,the b -values for the anodic and cathodic peak currents are 1from 1to 10mV s −1(Supplementary Fig.S4).The high-rate capability of T -Nb 2O 5implies that the crystal structure permits exceptionally rapid ionic transport.As shown in Fig.3a,the unit cell has sheets of edge-or corner-sharing distorted polyhedra lying parallel to the (001)plane,with each Nb 5+surrounded by either 6or 7O 2−.The polyhedra are exclusively corner-sharing along the [001]direction with 5%of the Nb 5+ions randomly located in 9-coordinate sites between the (001)poly-hedral planes 17.The mostly empty octahedral sites between (001)planes provide natural tunnels for lithium-ion transport through-out the a –b plane.Calculations indicate that the (001)plane allows degenerate pathways with low energy barriers for ion transport 18.A previous in situ X-ray diffraction study showed that the insertion of lithium into T -Nb 2O 5results in a solid solution with no apparent phase changes 19,and negligible changes to lattice constants 2and unit-cell volume 20up to ∼1.25Li +/Nb 2O 5.In situ X-ray absorption spectroscopy (XAS)demonstrated that lithiation reduces Nb 5+to Nb 4+(ref.19).The in situ XAS studies carried out here confirm that lithiation results in a continuous change in oxidation state (Fig.3b)and the Fourier-transform of the extended X-ray absorption fine structure (EXAFS)indicates that the insertion reaction proceeds through two stages (Fig.3c).From 2.5to 1.75V,the EXAFS signal from the various Nb–O bond lengths in Nb 2O 5(1.40–1.85Å)merges to a single peak at an intermediate bond length (1.75Å),indicating that lithiation increases the Nb-centred symmetry.The lithiation is probably faster at low Li +levels 20owing to greater availability of sites and less interaction between cations.At lower potentials,the new EXAFS peak shifts to longer bond distances (1.85Å)as a consequence of increased Li–O interactions at higher Li +content.These structural studies emphasize the value of an open,layered structure to enable rapid ion transport within the active material.The results presented in this study establish that T -Nb 2O 5exhibits electrochemical features of a pseudocapacitive material despite charge storage occurring in the bulk.Such behaviour is consistent with intercalation pseudocapacitance.The electrochem-ical features indicative of this mechanism are currents that are linearly proportional to the sweep rate,capacity that does not vary significantly with charging time,and peak potentials that do not shift significantly with sweep rate.A key design rule for intercalation pseudocapacitance at the atomic scale is a structure that does not undergo phase transformations on intercalation.In addition,facile two-dimensional (2D)lithium-ion diffusion pathways are18,98019,00019,02019,0401234D e r i v a t i v e , n o r m a l i z e d a b s o r p t i o nIncident energy (eV)ak 2|(R )| (A n g ¬3)χR (Å)b c2.50 V 1.80 V 1.65 V 1.50 V 1.35 V0.00.51.01.5Figure 3|Structural features of lithium intercalation in T -Nb 2O 5.a ,The structure of T -Nb 2O 5stacked along the c axis demonstrates the layeredarrangement of oxygen (red)and niobium (inside polyhedra)atoms along the a –b plane.b ,Derivative of Nb K-edge X-ray absorption near-edge spectra at selected cell voltages,showing a systematic shift to lower energiesas Nb 5+is reduced to Nb 4+.c ,k 2-weighted Fourier-transformed Nb K-edge EXAFS at selected cell voltages.important.Charge storage that behaves as a quasi-2D process ex-hibits similar behaviour to 2D surface adsorption reactions 14.These features contrast with those of pseudocapacitive RuO 2·x H 2O where charge storage occurs mainly on the surface or near-surface 21–24as summarized in Table 1.The results here are exciting because they demonstrate that for charging times as fast as 1min (60C rate),there are no diffusion limitations in T -Nb 2O 5.As the high-rate capability isdue to fast ion diffusion in the bulk,this mechanism may be very good for thick electrodes because surface exposure to the electrolyte is not critical.To achieve devices with high energy density,further engineering at the nanoscale and beyond will be necessary to preserve the atomic-scale behaviour observed in thin films and microelectrodes.In particular,maintaining proper electronic conduction pathways will be critical.MethodsSynthesis.The synthesis of T -Nb 2O 5nanocrystals was reported previously 2.Briefly,2.56mmol of NbCl 5(Sigma-Aldrich)was dissolved in 2ml of ethanol (Fisher Scientific).In a separate vial,0.23ml of deionized water was mixed with 2ml of ethanol.Both vials were then chilled for 2h.The two solutions were then mixed together while 1ml of propylene oxide (Sigma-Aldrich)was slowly added,forming a transparent gel.This gel was aged for 1day and then soaked in acetone (Fisher Scientific)for 5days.After supercritical drying with CO 2,the gel was transformed into an amorphous Nb 2O 5aerogel.Crystallization to the T -phase occurred by heat treatment at 600◦C for 2h in air.Characterization.Thin-film electrodes were fabricated by drop-casting a well-sonicated solution of T -Nb 2O 5in ethanol onto an oxygen plasma etched stainless-steel foil (Alfa Aesar).For thin-film measurements,lithium foils(Sigma-Aldrich)served as the reference and counter electrodes,and the electrolyte was 1M LiClO 4(Sigma-Aldrich)in propylene carbonate (Sigma-Aldrich).The microelectrode preparation was described elsewhere 9.Briefly,T -Nb 2O 5active material and carbon black (Timcal Super C65)powders were mixed in a 1:1weight ratio to ensure good electrical contact.The mixture was packed into the microcavity (30µm depth,30µm width),and subsequently immersed in the electrolyte.A 1cm 2platinum foil (Alfa Aesar)was used as the counter electrodeand lithium foil served as the reference.Thick Nb2O5electrodes were prepared by mixing the active material,carbon black(Timcal Super C65)and PVdF(Kynar) binder in a80:10:10weight ratio.The slurry was drop-cast onto12-mm-diameter aluminium-disc current collectors and dried at80◦C for12h.The electrode loading was between1and1.5mg cm−2with a thickness of40±5µm.Measurements of the thick Nb2O5electrodes were performed in three-electrode Swagelok cells with the Nb2O5electrode as the working electrode,activated carbon as the counter electrode,a glass fibre separator(Whatman,GF/A)saturated with1M LiClO4in propylene carbonate,and a lithium foil reference.All measurements were carried out in argon-filled glove boxes between1.2and3V(versus Li/Li+)with oxygen and moisture levels of<1ppm and using PAR EG&G273and Bio-Logic VMP3potentiostats.In situ X-ray absorption was performed using thin films of T-Nb2O5cast from a well-sonicated ethanol solution onto carbon-coated aluminium.2032-type coin cells were modified to include an X-ray window by drilling∼3-mm-diameter holes through the cathode casing and epoxying a125-µm-thick Kapton window on the outside of the casing.Both sides of the window were then coated with 100-nm-thick aluminium layers using a vacuum evaporator.Cells were assembled with a lithium anode,a1M LiClO4in propylene carbonate electrolyte,and a Whatman glassy fibre separator.Received17August2012;accepted19February2013; published online14April2013References1.Brezesinski,K.et al.Pseudocapacitive contributions to charge storage in highlyordered mesoporous Group V transition metal oxides with iso-oriented layered nanocrystalline domains.J.Am.Chem.Soc.132,6982–6990(2010).2.Kim,J.W.,Augustyn,V.&Dunn,B.The effect of crystallinity on the rapidpseudocapacitive response of Nb2O5.Adv.Energy Mater.2,141–148(2012). 3.Conway,B.E.Electrochemical Supercapacitors:Scientific Fundamentals andTechnological Applications(Kluwer-Academic,1999).4.Herrero,E.,Buller,L.J.&Abruña,H.D.Underpotential deposition atsingle crystal surfaces of Au,Pt,Ag and other materials.Chem.Rev.101,1897–1930(2001).5.Huggins,R.A.Supercapacitors and electrochemical pulse sources.Solid 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XAS was performed at the Cornell High Energy Synchrotron Source,supported bythe NSF and NIH/NIGMS(DMR-0936384).M.A.L.acknowledges support from the US DOD National Defense Science and Engineering Fellowship.J.C.was supportedby Delegation Generale pour l’Armement(DGA).P.S.and P-L.T.acknowledge the support from the European Research Council(ERC,Advanced Grant,ERC-2011-AdG, Project291543—IONACES)and the Chair of Excellence‘Embedded multi-functional nanomaterials’from the EADS Foundation.Author contributionsV.A.,J.C.,M.A.L.and J.W.K.:experimental work,data analysis.P-L.T.,S.H.T.,H.D.A., P.S.,B.D.:project planning,data analysis.Additional informationSupplementary information is available in the online version of the paper.Reprints and permissions information is available online at /reprints.Correspondence and requests for materials should be addressed to B.D.Competingfinancial interestsThe authors declare no competing financial interests.。

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