Synthesis of olivine LiFePO4 cathode materials by mechanical alloying using iron(III) raw material

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磷酸铁锂掺杂改性的研究

磷酸铁锂掺杂改性的研究
[324 ]
, 氧原子的分布近乎密堆六方 ; 磷原子处
于氧原子四面体间隙 , 形成 PO4 四面体 ; 铁原子 位于八面体间隙的 Z 字链上 ; 锂原子位于交替平 面八面体间隙的直线链上 , 其中 , 1 个 FeO6 八 面体分别与 1 个 PO4 四面体和 2 个 LiO6 八面体共 边 , 同时 , 1 个 PO4 四面体还与 2 个 LiO6 八面体 共边 。所有锂均可发生脱嵌 , 得到 FePO4 层状型 结构 。由于 LiFePO4 脱锂后得到的 FePO4 具有相 同的 空 间 群 , 因 此 , 即 使 在 400 ℃的 高 温 下 ,

© 1994-2010 China Academic Journal Electronic Publishing House. All rights reserved.
第3期
窦清山等 : 磷酸铁锂掺杂改性的研究
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散 , 因而不利于提高材料的高倍率充放电性能 。 而铁位掺杂可以改善 LiFePO4 的倍率充放电性 能 , 提高循环性能 。刘芳凌等 采用包裹碳提 高其表面电子电导率 , 掺杂金属离子以提高其本 体电子电导率 。选取了离子半径接近而价态不同 的 4 种金属离子 Ga 、Ti 、Ta 、Mo 的 Fe 位掺杂 , 掺杂后的样品晶胞体积均有减少 , 电子 电导率比 LiFePO4 的电子电导率提高了 4 ~ 6 个 数量级 , 并使其在电解质溶液中的阻抗大大减 少 , 电化学性能也明显改善 。掺杂金属离子的电 4+ 负性越小 , 其电化学性能就越好 。掺杂 Ti 的样 品具有最佳的电化学性能 。 胡环宇等 采用高温固相反应法合成颗粒 细小均匀的纳米级正极材料 LiFePO4 , 具有良好 的容量循环性能 , 但其高倍率性能差 。掺入少量 的锰可降低材料的极化 , 提高材料的高倍率性 能 。这主要是由于锰的掺杂增大了 LiFePO4 的晶 胞体积 , 更有利于锂的脱出 , 另外锰的掺杂导致 了烧结过程产生晶体结构缺陷 , 提高了材料的电 子导电性 , 从而使得材料的高倍率充放电性能有 [15 ] 所改善 。

磷酸亚铁锂

磷酸亚铁锂

湖南农业大学全日制普通本科生毕业论文FePO4制备工艺对流变相法合成LiFePO4/C性能的影响EFFECTS OF FEPO4 REACTION CONDITIONS ONELECTROCHEMICAL PROPERTIES OF LIFEPO4/C BYRHEOLOGICAL PHASE METHOD学生姓名:李季年级专业及班级:2010级材料化学(2)班指导老师及职称:钟美娥讲师学院:理学院湖南·长沙提交日期:20年月湖南农业大学全日制普通本科生毕业论文(设计)诚信声明本人郑重声明:所呈交的本科毕业论文(设计)是本人在指导老师的指导下,进行研究工作所取得的成果,成果不存在知识产权争议。

除文中已经注明引用的内容外,本论文不含任何其他个人或集体已经发表或撰写过的作品成果。

对本文的研究做出重要贡献的个人和集体在文中均作了明确的说明并表示了谢意。

本人完全意识到本声明的法律结果由本人承担。

毕业论文(设计)作者签名:20 年月日目录摘要 (1)关键词 (1)1 前言 (2)1.1 LiFePO4的研究现状 (2)1.2 LiFePO4与FePO4.2H2O的结构及特点 (3)1.3 锂离子电池的工作原理 (4)1.4 课题设计思路 (5)2实验部分 (6)2.2 试验方法 (7)2.2.1 样品的的制备与实验方案设计 (7)2.2.2 LiFePO4材料的结构表征 (8)2.2.3 电极的制备及模拟电池的装配 (8)2.2.4 模拟电池的电性能测试 (8)3 结果与讨论 (8)3.1 不同碳锂比 (8)3.2 不同反应温度 (9)3.3 不同反应pH (10)3.4 不同搅拌速度 (11)3.5 不同碳源 (11)3.6 掺杂 (12)4 实验结果的总结............................................................................ 错误!未定义书签。

磷酸铁锂离子电池正极材料

磷酸铁锂离子电池正极材料

Abstract Research progress in recent years on the preparation, modification, how to control crystal size, relationship between structure and performance, and prospect of olivine-type lithium iron phosphate LiFePO4 cathode materials for the lithium-ion batteries was reviewed. Particle size and its distribution, ionic and electronic conductivity, and the content of Fe( ) have much effect on the performance of the samples. The use of inert gas, the addition of conductive dope, and the control of crystal size to gain nano-powder are the useful way to improve the electrochemical performance of LiFePO4.
关键词 锂离子电池 正极材料 磷酸铁锂 改性
LiFePO4 Cathode Materials for Lithium-ion Batteries
Lü Zhengzhong, Zhou Zhentao
(College of Material Science and Engineering, South China University of Technology, Guangzhou 510641)

改进固相法制备LiFePO_4_C正极材料及其性能

改进固相法制备LiFePO_4_C正极材料及其性能

V ol 135N o 16#46#化 工 新 型 材 料N EW CH EM ICAL M A T ERIA L S 第35卷第6期2007年6月基金项目:国家自然科学基金项目资助(20672023),番禺区科技计划项目资助(2006-Z -10-1)作者简介:李军(1975-),男,博士后,讲师,主要从事电池材料的研究。

研究开发改进固相法制备LiFePO 4/C 正极材料及其性能李 军1,2 黄慧民1 魏关锋1 夏信德3 李大光1(11广东工业大学轻工化工学院,广州510006;21广东工业大学机电工程学院博士后流动站,广州51006;31广州市鹏辉电池有限公司博士后工作站,广州511483)摘 要 采用改进的固相反应法制备了掺碳的磷酸铁锂正极材料,并用XRD ,SEM ,元素分析,红外光谱及激光粒度分布仪等对样品进行了测试分析。

结果表明,样品具有单一的橄榄石结构和较好的放电平台(约314V ),粒度较小粒径分布均匀,011C 首次放电比容量为13718mA h/g ,循环20次后容量保持率为9216%,以1C 倍率首次放电比容量为12916mA h/g ,循环20次后容量下降1018%。

关键词 锂离子电池,磷酸铁锂,正极材料,固相法Preparation and properties of LiFePO 4/C cathode materials bymodified solid -state reactionsLi Jun1,2H uang H uimin 1 Wei Guangfeng 1 Xia Xinde 3 Li Dag uang1(11Schoo l of Chemical Engineering,Guangdong U niversity of T echnolog y,Guang zhou 510006;21Post -Doctor Statio n School of Electrom echanical Eng ineer ing,Guangdong U niv ersity o fTechnolog y,Guangzhou 510006;31Post -doctor Work Station,Guangzho u Peng hui Battery Ltd.,Guangzhou 511483)Abstract Carbon-do ped lithium iro n phosphate mater ials w ere prepared by mo dified solid -st ate r eact ion,and using XRD,SEM ,elemental analy sis,FT IR and laser particle size distributing to test samples.T he results sho wed that t hesamples w ith o liv ine structure g ood dischar ge platfo rm (approx imately 314V ).T he samples had an initiate ca pacity of 13718mA h/g at 011C,and 9216%of w hich r emained after 20cycles.T he fir st discharg e capacity w as 12916mA h/g at 1C and the capacity decreased 1018%after 20cycles.Key words lithium ion bat tery ,lithium ir on phosphat e,cathode mater ial,solid-st ate reactio n 新型电极材料特别是正极材料的研究与开发是推动锂离子电池技术更新的关键。

锂离子电池磷酸铁锂正极材料的制备及改性研究进展

锂离子电池磷酸铁锂正极材料的制备及改性研究进展

第29卷 第3期Vo l 29 No 3材 料 科 学 与 工 程 学 报Journal of M aterials Science &Engineering 总第131期Jun.2011文章编号:1673 2812(2011)03 0468 04锂离子电池磷酸铁锂正极材料的制备及改性研究进展俞琛捷1,莫祥银1,康彩荣2,倪 聪2,丁 毅2(1.南京师范大学分析测试中心&江苏省生物功能材料重点实验室,江苏南京 210046;2.南京工业大学材料科学与工程学院,江苏南京 210009)摘 要 橄榄石型磷酸铁锂(LiFePO 4)由于安全性能好、循环寿命长、原材料来源广泛、无环境污染等优点被公认为是最具发展潜力的锂离子动力与储能电池正极材料。

综述了近年来磷酸铁锂正极材料在制备和改性方面的最新进展。

在此基础上,提出了磷酸铁锂正极材料未来的主要研究和发展方向。

关键词 锂离子电池;正极材料;磷酸铁锂;制备;改性中图分类号:T B34 文献标识码:AProgress in Synthesis and Modification of LiFePO 4Cathode Material forLithium Ion Rechargeable BatteriesYU C hen jie 1,MO Xiang yin 1,KANG Cai rong 2,NI C ong 2,DING Yi 2(1.Nanjing Normal University,Analysis and Testing Center &Jiangsu Key Laboratory of Biof unctional Materials,Nanjing 210046,China;2.College of Materials Science and Engineering,Nanjing University of Technology,Nanjing 210009,China)Abstract Olivine lithium iron phosphate (LiFePO 4)is universally r ecognized as a pro mising catho de material for lithium ion recharg eable batteries for electr ic v ehicles due to hig h safety required to traction batteries,long lifespan,plentiful resources,and env ir onm ental friendliness.A systematical r eview of r ecent synthesis and modification research of LiFePO 4cathode material for lithium io n r echarg eable batter ies w as presented.On the basis,main research and developing trends regarding LiFePO 4cathode mater ial w ere pro posed.Key words lithium io n rechargeable batter ies;cathode m aterial;lithium iro n phosphate;synthesis;modification收稿日期:2009 09 02;修订日期:2010 07 19基金项目:国家 973 资助项目(6134501ZT01 004 02);王宽诚德国学术交流研究基金资助项目(K.C.W ong Fellows hip DAAD Section 423 C hina,M ong olia)作者简介:俞琛捷,女,硕士,助理研究员,主要从事材料化学等研究。

英文文献-溶胶-凝胶法制备LiFePO4改进其电化学性能

英文文献-溶胶-凝胶法制备LiFePO4改进其电化学性能

Electrochimica Acta 92 (2013) 248–256Contents lists available at SciVerse ScienceDirectElectrochimicaActaj o u r n a l h o m e p a g e :w w w.e l s e v i e r.c o m /l o c a t e /e l e c t a c taGel-combustion synthesis of LiFePO 4/C composite with improved capacity retention in aerated aqueous electrolyte solutionMilica Vujkovi´c a ,Ivana Stojkovi´c a ,Nikola Cvjeti´canin a ,Slavko Mentus a ,b ,∗,1a University of Belgrade,Faculty of Physical Chemistry,P.O.Box 137,Studentski trg 12-16,11158Belgrade,Serbia bThe Serbian Academy of Sciences and Arts,Kenz Mihajlova 35,11158Belgrade,Serbiaa r t i c l ei n f oArticle history:Received 2October 2012Received in revised form 3January 2013Accepted 5January 2013Available online 11 January 2013Keywords:Aqueous rechargeable Li-ion battery Galvanostatic cycling Gel-combustion Olivine LiFePO 4LiFePeO 4/C compositea b s t r a c tThe LiFePO 4/C composite containing 13.4wt.%of carbon was synthesized by combustion of a metal salt–(glycine +malonic acid)gel,followed by an isothermal heat-treatment of combustion product at 750◦C in reducing atmosphere.By a brief test in 1M LiClO 4–propylene carbonate solution at a rate of C/10,the discharge capacity was proven to be equal to the theoretical one.In aqueous LiNO 3solu-tion equilibrated with air,at a rate C/3,initial discharge capacity of 106mAh g −1was measured,being among the highest ones observed for various Li-ion intercalation materials in aqueous solutions.In addition,significant prolongation of cycle life was achieved,illustrated by the fact that upon 120charg-ing/discharging cycles at various rates,the capacity remained as high as 80%of initial value.The chemical diffusion coefficient of lithium in this composite was measured by cyclic voltammetry.The obtained val-ues were compared to the existing literature data,and the reasons of high scatter of reported values were considered.© 2013 Elsevier Ltd. All rights reserved.1.IntroductionThanks to its high theoretical Coulombic capacity (170mAh g −1)and environmental friendliness,LiFePO 4olivine became a desir-able cathodic material of Li-ion batteries [1,2],competitive to other commercially used cathodic materials (LiMnO 4,LiCoO 2).As evidenced in non-aqueous electrolyte solutions,a small vol-ume change (6.81%)that accompanies the phase transition LiFePO 4 FePO 4enables Li +ion insertion/deinsertion reactions to be quite reversible [1–3].The problem of low rate capability,caused by low electronic conductivity [4,5],was shown to be solv-able to some extent by reduction of mean particle size [6].Further improvements in both conductivity and electrochemical perform-ances were achieved by forming composite LiFePO 4/C,where in situ produced carbon served as an electronically conducting con-stituent [5,7–27].Ordinarily,both in situ formed carbon and carbon black additive,became unavoidable constituent of the LiFePO 4-based electrode materials [28–37].Zhao et al.[27]reported that Fe 2P may arise as an undesirable product during the synthesis of LiFePO 4/C composite under reducing conditions,however,other authors found later that this compound may contribute positively∗Corresponding author at:University of Belgrade,Faculty of Physical Chemistry,P.O.Box 137,Studentski trg 12-16,11158Belgrade,Serbia.Tel.:+381112187133;fax:+381112187133.E-mail address:slavko@ffh.bg.ac.rs (S.Mentus).1ISE member.to the electronic conductivity and improve the electrochemical per-formance of the composite [28–30].Severe improvement in rate capability and capacity retention was achieved by partial replace-ment of iron by metals supervalent relative to lithium [31–37].Thus one may conclude that the main aspects of practical applica-bility of LiFePO 4in Li-ion batteries with organic electrolytes were successively resolved.After the pioneering studies by Li and Dahn [38,39],recharge-able Li-ion batteries with aqueous electrolytes (ARLB)attracted considerable attention [40–50].The first versions of ARLB’s,suf-fered of very low Coulombic utilization and significantly more pronounced capacity fade relative to the batteries with organic electrolyte,regardless on the type of electrode materials [43].For the first time,LiFePO 4was considered as a cathode material in ARLB’s by Manickam et al.in 2006[44].He et al.[46],in an aqueous 0.5M Li 2SO 4solution,found that LiFePO 4displayed both a surprisingly high initial capacity of 140mAh g −1at a rate 1C and recognizable voltage plateau at a rate as high as 20C,which was superior relative to the other electrode materials in ARLB’s.Recently,the same authors reported a high capacity decay in aer-ated electrolyte solution,amounting to 37%after only 10cycles [48].In the same study,they demonstrated qualitatively by a brief cyclovoltammetric test,that a carbon layer deposited from a vapor phase over LiFePO 4particles,suppressed the capacity fade [48].Inspired by the recent discoveries about excellent rate capa-bility [46]but short cycle life [48]of LiFePO 4in aerated aqueous solution,we attempted to prolong the cycle life by means of protecting carbon layer over the LiFePO 4particles.Therefore we0013-4686/$–see front matter © 2013 Elsevier Ltd. All rights reserved./10.1016/j.electacta.2013.01.030M.Vujkovi´c et al./Electrochimica Acta92 (2013) 248–256249synthesized LiFePO4/C composite by a fast and simple glycine-nitrate gel-combustion technique.This method,although simpler than a classic solid state reaction method combined with ball milling[44,48],was rarely used for LiFePO4synthesis[19,27].It yielded a porous,foamy LiFePO4/C composite,easily accessible to the electrolyte.Upon the fair charging/discharging performance was confirmed by a brief test in organic electrolyte,we examined in detail the electrochemical behavior of this material in aqueous electrolyte,by cyclic voltammetry,complex impedance and cyclic galvanostatic charging/discharging methods.In comparison to pure LiFePO4studied in Ref.[48],this composite displayed markedly longer cycle life in aerated aqueous solutions.The chemical dif-fusion coefficient of lithium was also determined,and the reasons of its remarkable scatter in the existing literature were considered.2.ExperimentalThe LiFePO4/C composite was synthesized using lithium nitrate, ammonium dihydrogen phosphate(Merck)and iron(II)oxalate dihydrate(synthesized according to the procedure described else-where[51])as raw materials.Our group acquired the experience in this synthesis technique on the examples of spinels LiMn2O4 [52]and LiCr0.15Mn1.85O4[53],where glycine served as both fuel and complexing/gelling agent to the metal ions.A stoichiometric amount of each material was dissolved in deionized water and mixed at80◦C using a magnetic stirrer.Then,first glycine was added into the reaction mixture to provide the mole ratio of glycine: nitrate of2:1,and additionally,malonic acid(Merck)was added in an amount of60wt.%of the expected mass of LiFePO4.The role of malonic acid was to decelerate combustion and provide con-trollable excess of carbon[14].After removing majority of water by evaporation,the gelled precursor was heated to initiate the auto-combustion,resulting in aflocculent product.The combustion product was heated in a quartz tube furnacefirst at400◦C for3h in Ar stream,and then at750◦C for6h,under a stream of5vol.%H2in Ar.This treatment consolidated the olivine structure and enabled to complete the carbonization of residual organic matter.The VO2powder prepared by hydrothermal method was used as an active component of the counter electrode in the galvanostatic experiments in aqueous electrolyte solution.The details of the syn-thesis and electrochemical behavior of VO2are described elsewhere [54,55].The considerable stoichiometric excess of VO2was used,to provide that the LiFePO4/C composite only presents the main resis-tive element,i.e.,determines the behavior of the assembled cell on the whole.The XRD experiment was performed using Philips1050diffrac-tometer.The Cu K␣1,2radiation in15–70◦2Ârange,with0.05◦C step and2s exposition time was used.The carbon content in the composite was determined by its com-bustion in theflowing air atmosphere,by means of thermobalance TA SDT Model2090,at a heating rate of10◦C min−1.The morphology of the synthesized compounds was observed using the scanning electron microscope JSM-6610LV.For electrochemical investigations,the working electrode was made from LiFePO4/C composite(75%),carbon black-Vulcan XC72 (Cabot Corp.)(20%),poly(vinylidenefluoride)(PVDF)binder(5%) and a N-methyl-2-pyrrolidone solvent.The resulting suspension was homogenized in an ultrasonic bath and deposited on electron-ically conducting support.The electrode was dried at120◦C for 4h.Somewhat modified weight ratio,85:10:5,and the same drying procedure,were used to prepare VO2electrode.The non-aqueous electrolyte was1M LiClO4(Lithium Corpo-ration of America)dissolved in propylene carbonate(PC)(Fluka). Before than dissolved,LiClO4was dried over night at140◦C under vacuum.The aqueous electrolyte solution was saturated LiNO3solution.The cyclic voltammetry and complex impedance experiments were carried out only for aqueous electrolyte solutions,by means of the device Gamry PCI4/300Potentiostat/Galvanostat.The three electrode cell consisted of a working electrode,a wide platinum foil as a counter electrode,and a saturated calomel electrode(SCE) as a reference one.The experiments were carried out in air atmo-sphere.The impedance was measured in open-circuit conditions, at various stages of charging and discharging,within the frequency range10−2−105Hz,with7points per decade.Galvanostatic charging/discharging experiments were carried out in a two-electrode arrangement,by means of the battery testing device Arbin BT-2042,with two-terminal connectors only.In the galvanostatic tests in non-aqueous solution,working electrode was a2×2cm2platinum foil carrying2.3mg of compos-ite electrode material(1.5mg of olivine),while counter electrode was a2×2cm2lithium foil.The cell was assembled in an argon-filled glove box and cycled galvanostatically within a voltage range 2.1–4.2V.The galvanostatic tests in the aqueous electrolyte solution were carried out in a two-electrode arrangement,involving3mg of cathodic material,as a working electrode,and VO2in a multi-ple stoichiometric excess,as a counter electrode.According to its reversible potential of lithiation/delithiation reaction[55],VO2per-formed as an anode in this cell.The4cm2stainless steel plates were used as the current collectors for both positive and negative electrode.The cell was assembled in room atmosphere,and cycled within the voltage window between0.01and1.4V.3.Result and discussion3.1.The XRD,SEM and TG analysis of the LiFePO4/C compositeFig.1shows the XRD patterns of the composite LiFePO4/C pre-pared according to the procedure described in the Experimental Section.As visible,the diffractogram agrees completely with the one of pure LiFePO4olivine,found in the JCPDS card No.725-19. The narrow diffraction lines indicate complete crystallization and relatively large particle dimensions.On the basis of absence of diffraction lines of carbon,we may conclude that the carbonized product was amorphous one.Fig.2shows the SEM images of the LiFePO4/C composite at two different magnifications.Theflaky agglomerates,Fig.2left,with apparently smooth surface and low tap density,are due to a partial liquefaction and evolution of gas bubbles during gel-combustion procedure.These agglomerates consist of small LiFePO4/CFig.1.XRD patterns of LiFePO4/C composite in comparison to standard crystallo-graphic data.250M.Vujkovi´c et al./Electrochimica Acta 92 (2013) 248–256Fig.2.SEM images of LiFePO 4/C composite at two different magnification,20000×and 100000×.composite particles visible better at higher magnification,Fig.2,ly at the magnification of 100,000×,one may see that the size of majority of composite particles was in the range 50–100nm.The mean particle diameter,2r,as per SEM microphotograph amounted to 75nm.This analysis evidences that the gel-combustion method may provide nanodisprsed particles,desirable from the point of view of rate capability.For instance,Fey et al.[16]demonstrated that particle size reduction from 476to 205nm improved the rate capa-bility of LiFePO 4/C composite in organic electrolyte,illustrated by the increase of discharge capacity from 80mAh g −1to 140mAh g −1at discharging rate 1C.Also,carbon matrix prevented particles from agglomeration providing narrow size distribution,contrary to often used solid state reaction method of synthesis,when sintering of ini-tially nanometer sized particles caused the appearance of micron sized agglomerates [22].The SEM microphotograph (Fig.2)alone did not permit to rec-ognize carbon constituent of the LiFePO 4/C composite.However,carbonized product was evidenced,and its content measured,by means of thermogravimetry,as described elsewhere [9].The dia-gram of simultaneous thermogravimetry and differential thermal analysis (TG/DTA)of the LiFePO 4/C composite performed in air is presented in Fig.3.The process of moisture release,causing a slight mass loss of 1%,terminated at 150◦C.In the temperature range 350–500◦C carbon combustion took place,visible as a drop of the TG curve and an accompanying exothermic peak of the DTA curve.However,the early stage of olivine oxidation merged to some extent with the late stage of carbon combustion,and therefore,the minimum of the TG curve,appearing at nearly 500◦C,was not so low as to enable to read directly the carbon content.Fortunately,as proven by XRD analysis,the oxidation of LiFePO 4at tempera-ture exceeding 600◦C,yielded only Li 3Fe 2(PO 4)3and Fe 2O 3,whatFig.3.TGA/DTA curve of LiFePO 4/C under air flow at heating rate of 10C min−1.corresponded to the relative gain in mass of exactly 5.07%[9].Therefore,the weight percentage of carbonaceous fraction in the LiFePO 4/C composite was determined as equal to the difference between the TG plateaus at temperatures 300and 650◦C,aug-mented for 5.07%.According to this calculation the carbon fraction amounted to 13.4wt.%,and by means of this value,the electro-chemical parameters discussed in the next sections were correlated to pure LiFePO 4.Specific surface area of LiFePO 4,required for the measurement of diffusion constant,was determined from SEM image (Fig.2).Assuming a spherical particle shape and accepting mean particle radius r =37.5nm,the specific surface area was estimated on the basis of equation [17,22,45,46]:S =3rd(1)where the bulk density d =3.6g cm −3was used .This calculation resulted in the value S =22.2m 2g −1.In this calculation the contri-bution of carbon to the mean particle radius was ignored,however the error introduced in such way is more acceptable than the error which may arise if standard BET method were applied to the com-posite with significant carbon ly,due to a usually very developed surface area of carbon,the measured specific sur-face may exceed many times the actual surface area of LiFePO 4.3.2.Electrochemical measurements3.2.1.Non-aqueous electrolyte solutionIn order to compare the behavior of the synthesized LiFePO 4/C composite to the existing literature data,available predominantly for non-aqueous solutions,a brief test was performed in non-aqueous 1M LiClO 4+propylene carbonate solution by galvano-static experiments only.The results for the rates C/10,C/3and C,within the voltage limits 2.1–4.2V,were presented in Fig.4.The polarizability of the lithium electrode was estimated on the basis of the study by Churikov [56–67],who measured the current–voltage curves of pure lithium electrode in LiClO 4/propylene carbon-ate solutions at various temperatures.To the highest rate of 1C =170mA g −1in nonaqueous electrolyte,the corresponding cur-rent amounted to 0.25mA,which was equal to the current density of 0.064mA cm −2through the Li counter electrode.According to Fig.2in Ref.[67],for room temperature,the corresponding over-voltage amounted to only 6mV.Since lithium electrode is thus practically non-polarizable in this system,the voltages presented on the ordinate of the left diagram are the potentials of the olivine electrode expressed versus Li/Li +reference electrode.The clear charge and discharge plateaus at about 3.49V and 3.40V,respec-tively,correspond to the LiFePO 4 FePO 4phase equilibria [5].At discharging rate of C/10,the initial discharge capacity,within the limits of experimental error,was close to a full theoreticalM.Vujkovi´c et al./Electrochimica Acta 92 (2013) 248–256251Fig.4.The initial charge/discharge curves (a)and cyclic performance (b)of LiFePO 4/C composite in 1M LiClO 4+PC at different rates within a common cut-off voltage of2.1–4.2V.Fig.5.Charge/discharge profile and corresponding cyclic behavior of LiFePO 4/C in 1M LiClO 4+PC at the rate of 1C.capacity of LiFePO 4(170mAh g −1).This value is higher than that for LiFePO 4/C composite obtained by glycine [19],malonic acid [14]and adipic acid/ball milling [15]assisted methods.As usual,the discharge capacity decreased with increasing discharging rate (Fig.4b),and amounted to 127mAh g −1at C/3,and 109mAh g −1at 1C.For practical application of Li-ion batteries,a satisfactory rate capability and long cycle life are of primary importance.The charge/discharge profiles and dependence of capacity on the cycle number at the rate 1C are presented in Fig.5.The capacity was almost independent on the number of cycles,similarly to theearlier reports by Fey et al.[37–39].For comparison,Kalaiselvi et al.[19],by a glycine assisted gel-combustion procedure,with an additional amount (2wt.%)of carbon black,produced a similar nanoporous LiFePO 4/C composite displaying somewhat poorer per-formance,i.e.,smaller discharge capacity of 160mAh g −1at smaller discharging rate of C/20.On the other hand,better rate capability of LiFePO 4/C com-posite,containing only 1.1–1.8wt.%of carbon,in a non-aqueous solution,was reported by Liu et al.[21].For instance they mea-sured 160mAh g −1at the rate 1C,and 110at even 30C [21].This may be due to a thinner carbon layer around the LiFePO 4olivine particles.However the advantage of here applied thicker carbon layer exposed itself in aqueous electrolyte solutions,as described in the next section.3.2.2.Aqueous electrolyte solution3.2.2.1.Cyclic voltammetry.By the cyclic voltammetry method (CV)the electrochemical behavior of LiFePO 4/C composite in satu-rated aqueous LiNO 3solution was preliminary tested in the voltage range 0.4–1V versus SCE.The cyclic voltammograms are pre-sented in Fig.6.The highest scan rate of 100mV s −1,tolerated by this material,was much higher than the ones (0.01–5mV s −1)used in previous studies in both organic [13,24,25]and aqueous electrolyte solutions [47,48].Since one deals here with the thin layer solid redox electrode,limited in both charge consumption and diffusion length,the voltammogram is more complicated for interpretation comparing with the classic case of electroactive species in a liquid solution.A sharp,almost linear rise of current upon achieving reversible potential,with overlapped rising parts at various scan rates,similar to ones reported elsewhere [21,25],resembles closely the voltammogram of anodic dissolution ofaFig.6.Cyclic voltammograms of LiFePO 4/C in saturated LiNO 3aqueous electrolyte with a scan rate of 1mV s −1(left)and at various scan rates in the range 1–100mV s −1.252M.Vujkovi´c et al./Electrochimica Acta 92 (2013) 248–256Fig.7.Anodic and cathodic peak current versus square root of scan rate forLiFePO 4/C composite in aqueous LiNO 3electrolyte solution.thin metal layer [56],which proceeds under constant reactant activity.Since the solid/solid phase transitions LiFePO 4 FePO 4accompanies the redox processes in this system [5,8,57,58],the positive scan of the voltammograms depict the phase transition of LiFePO 4to FePO 4,while the negative scan depicts the phase transi-tion FePO 4to LiFePO 4.As shown by Srinivasan et al.[5],LiFePO 4may be exhausted by Li not more than 5mol.%before to trans-form into FePO 4,while FePO 4may consume no more than 5%Li before to transform into LiFePO 4,i.e.cyclic voltammetry exper-iments proceeds under condition of almost constant activity of the electroactive species.Although these aspects of the Li inser-tion/deinsertion process do not fit the processes at metal/liquid electrolyte boundary implied by Randles–Sevcik equation:i p =0.4463F RT1/2C v 1/2AD 1/2(2)this equation was frequently used to estimate apparent diffusion coefficient in Li insertion processes [5,17,21,46,59].To obtain peak current,i p ,in amperes,the concentration of lithium,C =C Li ,should be in mol cm −3,the real surface area exposed to the electrolyte in cm 2,chemical diffusion coefficient of lithium through the solid phase,D =D Li ,in cm 2s −1,and sweep rate,v ,in V s −1.The Eq.(2)pre-dicts the dependence of the peak height on the square root of sweep rate to be linear,as found often in Li-ion intercalation processes [17,21,25,59,60].This condition is fulfilled in this case too,as shown in Fig.7.The average value of C Li may be estimated as a reciprocal value of molar volume of LiFePO 4(V M =44.11cm 3mol −1),hence C Li =2.27×10−2mol cm −3.The determination of the actual surface area of olivine is a more difficult task,due to the presence of carbon in the LiFePO 4/C ly,classical BET method of sur-face area measurement may lead to a significantly overestimated value,since carbon surface may be very developed and participate predominantly in the measured value [15].Thus the authors in this field usually calculated specific surface area by means of Eq.(1),using mean particle radius determined by means of electron microscopy [17,22,45,46].Using S =22.2m 2g −1determined by means of Eq.(1),and an actual mass of the electroactive substance applied to the elec-trode surface (0.001305g),the actual electrode surface area was calculated to amount to A =290cm 2.This value introduced in Randles–Sevcik equation yielded D Li ∼0.8×10−14cm 2s −1.From the aspect of capacity retention,the insolubility of olivine in aqueous solutions is advantageous compared to the vanadia-based Li-ion intercalation materials,such as Li 1.2V 3O 8[61],LiV 3O 8[62]and V 2O 5[63],the solubility of which in LiNO 3solution was perceivable through the yellowish solutioncoloration.Fig.8.The Nyquist plots of LiFePO 4/C composite in aqueous LiNO 3solution at var-ious stages of delithiation;inset:enlarged high-frequency region.3.2.2.2.Impedance measurements.Figs.8and 9present the Nyquist plots of the LiFePO 4/C composite in aqueous LiNO 3solution at various open circuit potentials (OCV),during delithiation (anodic sweep,Fig.8)and during lithiation (cathodic sweep,Fig.9).The delithiated phase,observed at OCV =1V,as well as the lithi-ated phase,observed at OCV =0V,in the low-frequency region (f <100Hz)tend to behave like a capacitor,characteristic of a surface thin-layered redox material with reflective phase bound-ary conditions [64].At the OCV not too far from the reversible one (0.42V during delithiation,0.308V during lithiation),where both LiFePO 4and FePO 4phase may be present,within the whole 10−2–105Hz frequency range,the reaction behaves as a reversible one (i.e.shows the impedance of almost purely Warburg type).The insets in Figs.8and 9present the enlarged parts of the impedance diagram in the region of high frequencies,where one may observe a semicircle,the diameter of which corresponds theoretically to the charge transfer resistance.As visible,the change of open circuit potential between 0and 1V,in spite of the phase transition,does not cause significant change in charge transfer resistance.The small charge transfer resistance obtained with the carbon participation of 13.4%,being less than 1 ,is the smallest one reported thus far for olivine based materials.This finding agrees with the trend found by Zhao et al.[27],that the charge transfer resistance scaleddownFig.9.The Nyquist plots of LiFePO 4/C composite in aqueous LiNO 3solution at var-ious stages of lithiation;inset:enlarged high-frequency region.M.Vujkovi´c et al./Electrochimica Acta 92 (2013) 248–256253Fig.10.The dependence Z Re vs.ω−1/2during lithiation at 0.308V (top)and delithi-ation at 0.42V (down)in the frequency range 72–2.68Hz.to 1000,400and 150 when the amount of in situ formed carbon in the LiFePO 4/C composite increased in the range 1,2.8and 4.8%.For OCV corresponding to the cathodic (0.42V)and anodic (0.308V)peak maxima,the Warburg constant W was calculated from the dependence [21]:Z Re =R e +R ct + W ω−1/2(3)In the frequency range 2.7–72Hz,almost purely Warburg impedance was found to hold (i.e.the slope of the Nyquist plot very close to 45degrees was found).At the potential of cathodic current maximum (0.42V),from Fig.10, W was determined to amount to 7.96 s −1/2.At the potential of anodic maxima,0.308V, W was determined to amount to 9.07 s −1/2.In the published literature,for the determination of diffusion coefficient on the basis of impedance measurements,the following equation was often used [66,68,69]:D =0.5V M AF W ıE ıx2(4)where V M is molar volume of olivine,44.1cm 3, W is Warburg con-stant and ıE /ıx is the slope of the dependence of electrode potential on the molar fraction of Li (x )for given value of x .However,the potentials of CV maxima in the here studied case correspond to the x range of two-phase equilibrium,where for an accurate deter-mination of ıE /ıx a strong control of perturbed region of sample particles is required [69],and thus the determination of diffusion coefficients was omitted.3.2.2.3.Galvanostatic measurements.The galvanostatic measure-ments of LiFePO 4/C in saturated LiNO 3aqueous solution were performed in a two-electrode arrangement using hydrother-mally synthesized VO 2[55]as the active material of thecounterFig.11.Capacity versus cycle number and charge/discharge profiles (inset)for thecell consisting of LiFePO 4/C composite as cathode,and VO 2in large excess as anode,in saturated LiNO 3aqueous electrolyte observed at rate C/3.electrode.Preliminary cyclovoltammetric tests of VO 2in saturated LiNO 3solution at the sweep rate 10mV s −1,evidenced excellent cyclability and stable capacity of about 160mAh g −1during at least 50cycles.The voltage applied to the two-electrode cell was cycled within the limits 0and 1.4V.Due to a significant stoichiometric excess of VO 2over LiFePO 4/C composite (5:1)the actual voltage may be considered to be the potential versus reference VO 2/Li x VO 2electrode.Fig.11shows the dependence of the discharging Coulombic capacity of the LiFePO 4/C composite on the number of galvano-static cycles at discharging rate C/3,as well as (in the inset)the voltage vs.charging/discharging degree for 1st,2nd and 50th cycle.The charge/discharge curves do not change substantially in shape upon cycling,indicating stable capacity.For an aqueous solution,a surprisingly high initial discharge capacity of 106mAh g −1and low capacity fade of only 6%after 50charge/discharge cycles were evidenced.This behavior is admirable in comparison to other elec-trode materials in aqueous media reported in literature (LiTi 2(PO 4)3[42],LiV 3O 8[57]),and probably enabled by a higher thermody-namic stability of olivine structure [1].Fig.12presents the results of cyclic galvanostatic investigations of LiFePO 4/C composite in aqueous LiNO 3solution at various dis-charging rates.The charging/discharging rate was initially C/3for 80cycles and then was increased stepwise up to 3C.ThecapacityFig.12.Cyclic performance of LiFePO 4/C in saturated LiNO 3aqueous electrolyte at different charging/discharging rates.。

关于磷酸铁锂的英文文献翻译

关于磷酸铁锂的英文文献翻译

锂离子电池正极材料覆碳LiFePO4的制备和表征摘要:用两种方法合成纳米LiFePO4/C复合材料,用国产的非晶体纳米FePO4作离子前驱体,可溶性淀粉、蔗糖、柠檬酸和间苯二酚甲醛聚合物四种物质分别作碳的前驱体。

其中可溶性淀粉、蔗糖、柠檬酸作碳前驱体时用第一种方法合成,间苯二酚甲醛聚合物作碳前驱体时用第二种方法合成。

得到样品后用XRD,TEM ,拉曼波谱和循环伏安法对制得样品的晶体结构,形貌,相成分以及电化学特性进行测试研究。

研究结果显示用可溶性淀粉和蔗糖作碳的前驱体制得的LiFePO4颗粒表面的碳的包覆层不充分,而用柠檬酸和间苯二酚甲醛聚合物作前驱体所得的样品实现了在LiFePO4颗粒表面得到均匀一致的碳包覆层的目的,并且相应的碳包覆层的厚度分别为2.5 nm和4.5 nm。

在制得的四种样品中,使用间二苯酚甲醛聚合物作碳的前驱体时,样品的首次放电比容量最高(室温下0.2 C 时放电比容量为138.4 mAh/ g),倍率性能最好。

第一章引言LiFePO4作为锂离子电池正极材料由于其理论比容量高(170mAh/g),环保,热稳定性好而受到广泛关注。

然而其低于10−13Scm−1的电导率限制了其电池性能【1】,例如在高电流密度下功率的显著减小是其商业化发展的主要障碍。

目前人们已经引进了很多有效的方法克服LiFePO4电导率低的缺点,诸如金属替换法【2-5】,金属粉末混合法【6】,以及传导性碳包覆法【7-15】,通过形成良好的导电通路来提高最终产物的电导率。

在这些方法中,制备LiFePO4/C 复合材料是最受关注的。

此外,碳还可以用作还原剂使Fe3+降价为Fe2+。

值得提及的是包括纳米尺寸的磷酸铁锂的合成在内的很多研究用昂贵的Fe2+盐作前驱体【3.16-20】,例如FeC2O4·2H2O 和(CH 3COO)2Fe。

因此,研究新的制备方法和应用廉价的材料对磷酸铁锂作为锂离子电池正极材料的产业发展至关重要。

LiFePO4正极材料倍率性能改善的研究进展

LiFePO4正极材料倍率性能改善的研究进展

LiFePO4正极材料倍率性能改善的研究进展王旭峰;冯志军;张华森;丛欣泉;曾佑鹏【摘要】Olivine-type lithium iron phosphate (LFP) was used as cathode material of lithium ion battery due to its good electrochemical performance,such as stable charging and discharging platform and steady structure during cycling of Li ions.What's more,it had high safety,non-toxic and polluting-free,as well as long cycle life and rich rawmaterial.However,there was a instinct drawback of olive structure that baffles the marketization of LEP in the field of electrical vehicle,and that was the poor rate performance.The main approaches to improve rate performance of LEP include ion doping,surfacecoating,nanocrystallization,ect.On the base of improved approaches mentioned above,the methods in enhancing rate performance of LFP were reviewed in recent years.%橄榄石型磷酸铁锂(LFP)作为锂离子电池正极材料,具有良好的电化学性能、平稳的充放电平台、稳定的充放电结构,而且无毒、无污染、安全性能好、循环寿命长、原材料来源广泛.然而由于其本身结构的缺陷,导致其倍率性能低下,这将直接影响该材料在动力汽车市场的应用.改善其倍率性能的方法主要有离子掺杂、表面包覆、合成纳米材料.以这几类改性方法为主线,综述了近年来LFP倍率性能改善的研究进展.【期刊名称】《电源技术》【年(卷),期】2017(041)008【总页数】4页(P1202-1205)【关键词】锂离子电池;正极材料;磷酸铁锂;倍率性能【作者】王旭峰;冯志军;张华森;丛欣泉;曾佑鹏【作者单位】南昌航空大学材料科学与工程学院,江西南昌330063;南昌航空大学材料科学与工程学院,江西南昌330063;南昌航空大学材料科学与工程学院,江西南昌330063;南昌航空大学材料科学与工程学院,江西南昌330063;南昌航空大学材料科学与工程学院,江西南昌330063【正文语种】中文【中图分类】TM912锂离子电池以其能量密度高、使用寿命长、无记忆效应、可再次充放电、轻巧、工作电压高、无污染等优点,成为便携式产品和动力车载电池发展的主要方向。

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Journal of Power Sources 146(2005)534–538Synthesis of olivine LiFePO 4cathode materials by mechanicalalloying using iron(III)raw materialCheol Woo Kim a ,∗,Moon Hee Lee a ,Woon Tae Jeong b ,Kyung Sub Lee aaDepartment of Materials Science and Engineering,Hanyang University,Seoul 133-791,Korea bEco-nano Research Center,Korea Institute of Science and Technology(KIST),Seoul 130-650,KoreaAvailable online 31May 2005AbstractOlivine LiFePO 4has been produced using Fe 2O 3raw material by mechanical alloying (MA)and subsequent firing.X-ray diffraction (XRD)and M¨o ssbauer spectroscopy analysis revealed that LiFePO 4prepared by MA had a well-ordered olivine-type LiFePO 4structure with an ionic state of Fe 2+by the reduction of Fe 3+precursor.It showed a maximum discharge capacity of 160mAh g −1at C/20(8.5mA g −1)when cycled from 2.5to 4.3V .Compared to the LiFePO 4prepared by conventional solid-state method,MA synthesized LiFePO 4a displayed higher charge/discharge capacity and more stable cycle life because of the improvement of the electronic conductivity.It was originated from uniformly distributed fine particles and an increased specific surface area by MA process.©2005Elsevier B.V .All rights reserved.Keywords:LiFePO 4;Cathode material;Olivine-type iron phosphate;Mechanical alloying1.IntroductionOlivine-type LiFePO 4have been known as an interesting cathode material for lithium ion batteries since it was first pro-posed by Padhi et al.[1]because of its low cost and safety.The early drawback with LiFePO 4was its extremely low elec-tronic conductivity.Many works have been reported that the poor electrical conductivity of LiFePO 4can be overcome by adding conductive carbon and by treating the particle surface with nanocrystalline carbon [2–5].But these approaches of adding conductive carbon led to a loss in energy density due to the electrochemically inertness of the carbon.Also the use of the Fe 2+precursor compound is relatively high cost and has problems for mass production.Recently,Barker et al.[6]reported that LiFePO 4and LiFe 0.9Mg 0.1PO 4were synthesized by a carbothermal reduction (CTR)technique,which is based on the C →CO transition,starting with Fe 2O 3that is very cheap and readily available.In the present study,the same concept has been applied to the technique of mechanical alloying (MA)∗Corresponding author.Tel.:+82222814914;fax:+82222814914.E-mail address:waterflower 00@ (C.W.Kim).process.Previously,we have reported on the effectiveness of synthesizing LiFePO 4and LiFePO 4/C composite from a Fe 2+precursor by mechanical alloying (MA)[7].In this work,LiFePO 4was synthesized from Fe(III)by MA and subsequent firing under the assumption that the following reaction occurred:LiOH ·H 2O +0.5(Fe 2O 3)+(NH 4)2H ·PO 4+0.5C →LiFePO 4+3H 2O +2(NH 3)+0.5CO(1)The electrochemical properties and cycle life of prepared powders were investigated and compared with those of a sample synthesized by conventional solid-state reaction.2.ExperimentalLiOH ·H 2O (Aldrich,≥98%),Fe 2O 3(Aldrich,≥99%),(NH 4)2H ·PO 4(Aldrich,≥99%),and acetylene black pow-ders were used as starting materials.The MA process was carried out for 4h under argon atmosphere using a shaker type ball miller (SPEX 8000M)rotating at around 1000rpm.Detailed MA conditions were described in a previous study0378-7753/$–see front matter ©2005Elsevier B.V .All rights reserved.doi:10.1016/j.jpowsour.2005.03.058C.W.Kim et al./Journal of Power Sources146(2005)534–538535[7].The mechanical-alloyed powders were thenfired from 500to900◦C for30min in a tube-type vacuum furnace at a pressure10−6Torr.For comparison,another LiFePO4sam-ple was prepared by the solid-state reaction under different firing condition.The mixture,which the same starting ma-terials were thoroughly mixed in an agate mortar,wasfirst decomposed at450◦C for5h and then reground andfired at 900◦C for10h(denoted as SS450+900),which was the two-stepfiring condition employed in the conventional solid-state reaction process.The crystal structures of the prepared sample powders were characterized by X-ray diffraction(Rigaku D-MAX 3000)using Cu K␣radiation.The M¨o ssbauer spectra were recorded(Austin Science,Inc.,USA)using57Co in Rh ma-trix as the source of radiation at room temperature.The powder morphology and particle size distribution were in-vestigated byfield emission scanning electron microscopy (FE-SEM),and a particle size analyzer(PSA).The spe-cific surface area of the powder particles was measured by Brunauer–Emmett–Teller(BET),and the electrical conduc-tivity of the prepared samples was also measured by a four-point probe method.The cathodes used for electrochemical characterization were fabricated by blending the prepared active material pow-ders with carbon black and polytetrafluoroethylene(PTFE) binder in a weight ratio of75:20:5.Two-electrode electro-chemical cells consisting of lithium metal foil as the negative electrode,polypropylene separator,and an electrolyte of1M LiPF6in EC:DMC(1:1,vol.)were assembled in an argon-filled glove box.The electrochemical cycle tests were per-formed using an automatic galvanostatic charge–discharge unit(Maccor series4000)at various C rates,C/x(x=1,5, 10,20)(1C=170mA g−1)between2.5and4.3V at ambient temperature(25±2◦C).3.Results and discussionAs for the MA variables,optimum MA time to produce a crystalline LiFePO4phase was decided to4h in the previous study[7].To obtain a single phase olivine-type LiFePO4,the mechanical-alloyed powders were thenfired at temperatures ranging from500to900◦C for30min.The XRD patterns for the resulting their structural an evolution with increasing firing temperature are shown in Fig.1.The sample prepared at500◦C(Fig.1(a))mainly consists of Fe2O3with a minor LiFePO4peaks.With increasing temperature above500◦C the peaks of Fe2O3were diminishing,whereas the LiFePO4 peaks became sharper and more intense.Fig.1(e)shows that well-ordered olivine structure without heterogeneity was ob-tained onfiring at900◦C for only30min(will be referred to as MA900).It indicates that the reduction of Fe2O3starts from at500◦C and completelyfinishes at900◦C.This re-sult is out of accordance with Barker’s experiment,which is synthesized at750◦C for8h using LiH2PO4and Fe2O3[6], because the starting materials is different and unsuitablere-Fig.1.XRD patterns of LiFePO4prepared from Fe2O3raw material at variousfiring temperatures:(a)500◦C;(b)600◦C;(c)700◦C;(d)800◦C;(e)900◦C.duction reaction may be blocked by the short timefiring as 30min.Although XRD pattern of MA900revealed a single phase LiFePO4,complete transfer of Fe3+to Fe2+had to be confirmed.For this reason,the ionic state of Fe was investigated by M¨o ssbauer spectroscopy.M¨o ssbauer spec-troscopy measurements for LiFePO4prepared by the MA method at800and900◦C are shown in Fig.2.For sam-plefired at800◦C,the six-line patterns were analyzed with isomer shift(IS)=0.37mm s−1and quadropole split (QS)=−0.09mm s−1.The IS and QS values indicate that the Fe ions in the sample are predominantly composed of Fe3+.For the samplefired at900◦C,however,the spec-tra was observed by only one symmetric doublet with IS=1.25mm s−1and QS=2.95mm s−1,typical for those of ionic compounds with bare Fe2+ions[5].These results mean that the electrochemically inactive Fe3+would be reduced to active Fe2+at higher temperature to form LiFePO4,and eventually a single phase of olivine could be produced at 900◦C.It is well known that LiFePO4/C composite containing carbon or carbon coated LiFePO4can improve the low elec-tronic conductivity of LiFePO4and show excellent cathode performance[2–5].In our previous work LiFePO4/C com-posite compound containing no impurities was successfully synthesized by MA using Fe2+precursor.However,in the cur-536 C.W.Kim et al./Journal of Power Sources146(2005)534–538Fig.2.M¨o ssbauer spectra of the LiFePO4prepared by MA and subsequent fired at800and900◦C,respectively.rent study,the specimen prepared with3wt.%carbon using Fe2O3raw material revealed the presence of second phase of Fe2P as shown in Fig.3(a).When a large amount of carbon is added in excess of12wt.%,most of the LiFePO4disappeared and iron phosphide was predominantly produced(Fig.3(b)). It seemed that carbon in excess of the stoichiometric amount shown in Eq.(1)reduced the phosphate and generated Fe2P as follows Eq.(2).Fe2O3+PO4+7C→Fe2P+7CO(2) On the other hand,SS450+900prepared by conventionsolid-state method through two-step and long time heattreat-Fig.3.XRD patterns of(a)LiFePO4/C composite compound(3wt.%)and (b)LiFePO4/C composite compound(12wt.%),(b)LiFePO4prepared con-ventional solid-state reactionmethod.Fig.4.SEM images of MA900and SS450+900.ment produced single phase LiFePO4with no second phase (Fig.3(c)).Electron micrographs of LiFePO4prepared by the MA and SS methods are presented in Fig.4.The particle size distri-bution of MA900ranged from0.1to2␮m,while that of the SS450+900ranged from around1–10␮m with non-uniform morphology.The particle size distributions of the samples were in good agreement with the results determined by PAS. The results of the mean particle size determined by PSA,sur-face area by BET,and electronic conductivity for MA900and SM450+900are summarized in Table1.The MA900particle size was much smaller,whereas their surface area and elec-tronic conductivity were higher than SS450+900particles. It is considered that MA process can reduce the particle size by the high energy ball milling and by a markedly reduced firing time.This would cause the surface area of LiFePO4to increase,which would enhance the electronic conductivity. These results correspond well with the study of Yamada et al.[5]who reported that improvements in the conductivity could be achieved by synthesizing small and homogeneously sized powders.The second charge and discharge curves of the Li/LiFePO4 cells obtained from the MA and SS methods are shown in Fig.5.The cells were cycled between2.5and4.3V at a cur-rent density of C/20(8.5mA g−1)rate.Typical two-phase reactions between LiFePO4and FePO4with a3.4V plateau were observed in both samples[1].The discharge capacityC.W.Kim et al./Journal of Power Sources 146(2005)534–538537Table 1The powder properties of LiFePO 4prepared by different synthesis method Sample ID Synthesis conditionSurface area (m 2g −1)Ave.particle size (␮m)Electronic conductivity (S cm −1)MA900MA+900◦C,30min8.5 1.45 1.2×10−7SS450+900Simple mixture (450◦C,5h +900◦C,10h)1.25.781.7×10−9Fig.5.The charge/discharge curves of MA900and SS450+900at C/20rate.of the SS450+900sample was 130mAh g −1,which is 76%level of the theoretical capacity.On the other hand,MA900exhibited excellent cell performance with a discharge capac-ity of 160mAh g −1,which is 94%level of the theoretical ca-pacity.The discharge capacity of MA900is similar or higher discharge capacity than LiFePO 4/C composite compound re-ported in the recent studies [8–11].Fig.6shows the variation of the specific discharge capac-ity with the number of cycles.The charge/discharge current density was relatively high at the C/5rate with a cut-off volt-age of 2.5–4.3V at room temperature.The samplepreparedFig.6.Cycle life of LiFePO 4prepared by the MA method and solid-state reaction method (cycle between 2.5and 4.3V ,C/5).by MA has a higher discharge capacity and a more stable cy-cle life than the conventional solid-state synthesized sample.The cycling retention rate of MA900after 50cycles was about 89%of its maximum capacity,whereas the retention rate for SS450+900was 62%.Consequently,it could be concluded that mechanical alloying enhanced the electronic conductiv-ity and improved the cell performances of LiFePO 4prepared from Fe 3+precursor.4.ConclusionOlivine-type LiFePO 4was successfully synthesized from Fe 2O 3by MA method,and subsequent firing at 900◦C for only 30min.A single phase LiFePO 4/C composite could not be produced with carbon in excess of the stoichiometric amount because the Fe 2P was created by a reduction reaction of phosphate at high temperature.The well-crystallized lithium iron phosphate consisting of uniformly and fine particles had a higher discharge capacity of 160mAh g −1,and better electrochemical cycling behavior compared to LiFePO 4prepared by the conventional solid-state reaction.It is reconfirmed that the MA process could be the one of the viable methods to produce olivine-type LiFePO 4for lithium rechargeable batteries.AcknowledgementThis work was supported by Korea Research Foundation Grant (KRF-2003-041-D20299).References[1]A.K.Padhi,K.S.Nanjundaswamy,J.B.Goodenough,J.Electrochem.Soc.144(1997)1188.[2]N.Ravet,J.B.Goodenough,S.Besner,M.Simoneau,P.Hovington,Abstract 127,The Electrochemical Society and The Electrochemical Society of Japan Meeting Abstracts,vol.99-2,Honolulu,HI,October 17–22,1999.[3]H.Huang,S.C.Yin,L.F.Nazar,Electrochem.Solid-State Lett.4(2001)A170.[4]Z.Chen,J.R.Dahn,J.Electrochem.Soc.149(2002)A1184.[5]A.Yamada,S.C.Chung,K.Hinokuma,J.Electrochem.Soc.148(2001)A224.[6]J.Barker,M.Y .Saidi,J.L.Swoyer,Electrochem.Solid-State Lett.6(2003)A53.[7]S.J.Kwon,C.W.Kim,W.T.Jeong,K.S.Lee,J.Power Sources 137(2004)93–99.538 C.W.Kim et al./Journal of Power Sources146(2005)534–538[8]P.P.Prosini,D.Zane,M.Pasquali,Electrochim.Acta46(2001)3517.[9]S.Franger,F.Le Cras,c.Bourbon,Rouault,Electrochem.Solid-StateLett.5(2002)A231.[10]P.P.Prosini,M.Carewska,S.Scaccia,P.Wisniewski,S.Passerini,M.Pasquali,J.Electrochem.Soc.149(2002)A886.[11]G.Arnold,J.Garche,R.Hemmer,S.Strobele, C.V ogler,M.Wohlfahrt-Mehrens,J.Power Sources119–121(2003)247.。

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