CN104150543B - A kind of Cu 2+, Ce 4+, Ag +doping ferric fluoride composite positive pole and preparation method - Google Patents
A kind of Cu 2+, Ce 4+, Ag +doping ferric fluoride composite positive pole and preparation method Download PDFInfo
- Publication number
- CN104150543B CN104150543B CN201410348459.0A CN201410348459A CN104150543B CN 104150543 B CN104150543 B CN 104150543B CN 201410348459 A CN201410348459 A CN 201410348459A CN 104150543 B CN104150543 B CN 104150543B
- Authority
- CN
- China
- Prior art keywords
- fef
- doping
- capacity
- energy
- salt
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- SHXXPRJOPFJRHA-UHFFFAOYSA-K iron(iii) fluoride Chemical compound F[Fe](F)F SHXXPRJOPFJRHA-UHFFFAOYSA-K 0.000 title claims abstract 3
- 238000002360 preparation method Methods 0.000 title claims abstract 3
- 239000002131 composite material Substances 0.000 title claims 3
- 150000000703 Cerium Chemical class 0.000 claims abstract 3
- 239000000463 material Substances 0.000 claims abstract 3
- GGCZERPQGJTIQP-UHFFFAOYSA-N sodium;9,10-dioxoanthracene-2-sulfonic acid Chemical compound [Na+].C1=CC=C2C(=O)C3=CC(S(=O)(=O)O)=CC=C3C(=O)C2=C1 GGCZERPQGJTIQP-UHFFFAOYSA-N 0.000 claims abstract 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims 4
- 239000007789 gas Substances 0.000 claims 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 2
- 229910052786 argon Inorganic materials 0.000 claims 2
- 239000012752 auxiliary agent Substances 0.000 claims 2
- 239000013078 crystal Substances 0.000 claims 2
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 2
- 101710134784 Agnoprotein Proteins 0.000 claims 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- HVUMOYIDDBPOLL-XWVZOOPGSA-N Sorbitan monostearate Chemical compound CCCCCCCCCCCCCCCCCC(=O)OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O HVUMOYIDDBPOLL-XWVZOOPGSA-N 0.000 claims 1
- LDDQLRUQCUTJBB-UHFFFAOYSA-N ammonium fluoride Chemical compound [NH4+].[F-] LDDQLRUQCUTJBB-UHFFFAOYSA-N 0.000 claims 1
- 238000000498 ball milling Methods 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 235000010482 polyoxyethylene sorbitan monooleate Nutrition 0.000 claims 1
- 229920000053 polysorbate 80 Polymers 0.000 claims 1
- 239000010949 copper Substances 0.000 abstract 2
- 230000004913 activation Effects 0.000 abstract 1
- 239000010406 cathode material Substances 0.000 abstract 1
- 150000001879 copper Chemical class 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract 1
- 229910052742 iron Inorganic materials 0.000 abstract 1
- -1 iron ions Chemical class 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000007774 positive electrode material Substances 0.000 abstract 1
- 239000002994 raw material Substances 0.000 abstract 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Abstract
一种Cu2+,Ce4+,Ag+掺杂改性氟化铁正极材料及制备方法,该方法将铜盐、铈盐、银盐与合成原料在高能球磨机中经过一段时间球磨并热处理后即得到FeF3正极材料。Cu2+通过部分占据FeF3铁离子配位,有助于提高其放电电位,提高能量密度;而通过高价Ce4+掺杂,有助于提高材料的比容量;通过Ag2+掺杂,降低充电时转换反应活化能;这样有助于提高其倍率特性和能量密度,从而提高该材料的综合电化学性能。
A Cu 2+ , Ce 4+ , Ag + doped modified ferric fluoride positive electrode material and its preparation method. In the method, copper salt, cerium salt, silver salt and synthetic raw materials are ball-milled in a high-energy ball mill for a period of time and heat-treated. That is, the FeF 3 cathode material is obtained. Cu 2+ helps to increase its discharge potential and energy density by partially occupying the coordination of FeF 3 iron ions; while doping with high-valent Ce 4+ helps to improve the specific capacity of the material; through Ag 2+ doping, Reduce the conversion reaction activation energy during charging; this helps to improve its rate characteristics and energy density, thereby improving the comprehensive electrochemical performance of the material.
Description
技术领域 technical field
本发明涉及一种高容量氟化铁复合锂电正极材料制造方法技术领域。 The invention relates to the technical field of a method for manufacturing a high-capacity iron fluoride composite lithium battery cathode material.
背景技术 Background technique
锂离子二次电池具有体积、重量能量比高、电压高、自放电率低、无记忆效应、循环寿命长、功率密度高等绝对优点,目前在全球移动电源市场有超过300亿美元/年份额并以超过10%的速度逐渐增长。特别是近年来,随着化石能源的逐渐枯竭,太阳能、风能、生物质能等新能源逐渐成为传统能源的替代方式,其中风能、太阳能具有间歇性,为满足持续的电力供应需要同时使用大量的储能电池;汽车尾气带来的城市空气质量问题日益严重,电动车(EV)或混合电动车(HEV)的大力倡导和发展已经到了刻不容缓的地步;这些需求提供了锂离子电池爆发式增长点,同时也对锂离子电池的性能提出了更高的要求。 Lithium-ion secondary batteries have the absolute advantages of high volume, weight-to-energy ratio, high voltage, low self-discharge rate, no memory effect, long cycle life, and high power density. Currently, the global mobile power market has an annual share of more than 30 billion US dollars and Gradually grow at a rate of more than 10%. Especially in recent years, with the gradual depletion of fossil energy, new energy sources such as solar energy, wind energy, and biomass energy have gradually become alternatives to traditional energy sources. Among them, wind energy and solar energy are intermittent, and a large amount of energy is used simultaneously to meet the needs of continuous power supply Energy storage batteries; urban air quality problems caused by vehicle exhaust are becoming more and more serious, and the vigorous advocacy and development of electric vehicles (EV) or hybrid electric vehicles (HEV) has reached an urgent point; these demands provide an explosive growth point for lithium-ion batteries , but also put forward higher requirements on the performance of lithium-ion batteries.
锂离子电池正极材料的容量的提高是科技人员研究的首要目标,高容量正极材料的研发可以缓解目前锂离子电池组体积大、份量重、价格高难以满足高耗电及高功率设备需要的局面。然而自从1991年锂离子电池商业化以来,正极材料的实际比容量始终徘徊在100-180mAh/g之间,正极材料比容量低已经成为提升锂离子电池比能量的瓶颈。目前商用的锂离子电池最为广泛的实用的正极材料是LiCoO2,钴酸锂的理论比容量为274mAh/g,而实际比容量在130-140mAh/g之间,而且钴为战略物资,价格昂贵并有较大的毒性。因此近年来,世界各国的研究人员一直致力于新型锂离子电池正极材料的研究和开发,到目前,筛选出的锂离子电池正极多达数十种,但真正有潜在商业化应用前景或已经出现在市场上的正极材料确是非常之少。如尖晶石型锰酸锂LiMn2O4,其成本较低,比较容易制备,安全性能也比较好,然而容量较低,理论容量为148mAh/g,实际容量在100-120mAh/g,而且该材料容量循环保持能力不佳,高温下容量衰减很快,Mn3+的John-Teller效应及在电解质中的溶解长期以来困扰着研究人员。层状结构的LiNiO2和LiMnO2虽然有着较大的理论比容量,分别为275mAh/g和285mAh/g,但是它们制备非常困难,热稳定性差,循环性很差,容量衰减很快。而目前已经逐步商业化的磷酸铁锂LiFePO4成本低、热稳定性好、环境友好,但是其理论容量约只有170mAh/g,而实际容量在140mAh/g左右[ChunSY,BlokingJT,ChiangYM,NatureMaterials,2002,1:123-128.]。目前有市场前景的超过200mAh/g比容量的正极材料只有钒酸锂Li1+xV3O8,Li1+xV3O8材料能有拥有甚至接近300mAh/g的容量,但其放电平均电压较低而且生产过程中钒氧化物往往毒性较大。近年来高锂比正极材料上,特别是锰基锰-镍二元及锰基锰-镍-钴三元固溶体系的高锂比正极材料,具有超过200mAh/g的容量比、较高的热稳定性和相对低廉的成本而受到人们的关注,然而该材料高倍率下的性能非常不理想,限制了其在动力电池中的应用[Young-SikHong,YongJoonPark,etal.,SolidStateIonics,2005,176:1035-1042]。 The improvement of the capacity of lithium-ion battery cathode materials is the primary goal of scientific research. The research and development of high-capacity cathode materials can alleviate the current situation that lithium-ion battery packs are large in size, heavy in weight, and high in price and cannot meet the needs of high-power consumption and high-power equipment. . However, since the commercialization of lithium-ion batteries in 1991, the actual specific capacity of cathode materials has always hovered between 100-180mAh/g, and the low specific capacity of cathode materials has become a bottleneck for improving the specific energy of lithium-ion batteries. At present, the most widely used positive electrode material for commercial lithium-ion batteries is LiCoO 2 . The theoretical specific capacity of lithium cobalt oxide is 274mAh/g, but the actual specific capacity is between 130-140mAh/g. Moreover, cobalt is a strategic material and is expensive. And have greater toxicity. Therefore, in recent years, researchers from all over the world have been committed to the research and development of new lithium-ion battery cathode materials. Up to now, there have been dozens of lithium-ion battery cathode materials screened out, but there are real potential commercial application prospects or have already appeared. There are very few cathode materials on the market. For example, spinel lithium manganese oxide LiMn 2 O 4 has lower cost, is easier to prepare, and has better safety performance. However, the capacity is relatively low. The theoretical capacity is 148mAh/g, and the actual capacity is 100-120mAh/g. The capacity cycle retention of this material is not good, and the capacity fades quickly at high temperature. The John-Teller effect of Mn 3+ and its dissolution in electrolytes have long puzzled researchers. Although LiNiO 2 and LiMnO 2 with layered structure have relatively large theoretical specific capacities of 275mAh/g and 285mAh/g respectively, they are very difficult to prepare, have poor thermal stability, poor cycle performance, and rapid capacity decay. At present, the lithium iron phosphate LiFePO 4 that has been gradually commercialized has low cost, good thermal stability, and environmental friendliness, but its theoretical capacity is only about 170mAh/g, while the actual capacity is about 140mAh/g [ChunSY, BlokingJT, ChiangYM, NatureMaterials, 2002, 1:123-128.]. At present, only lithium vanadate Li 1+x V 3 O 8 is the only positive electrode material with a specific capacity exceeding 200mAh/g in the market. Li 1+x V 3 O 8 can have a capacity even close to 300mAh/g, but its discharge The average voltage is lower and the vanadium oxides tend to be more toxic during production. In recent years, high-lithium ratio cathode materials, especially manganese-based manganese-nickel binary and manganese-based manganese-nickel-cobalt ternary solid solution systems, have a capacity ratio of more than 200mAh/g, higher thermal Stability and relatively low cost have attracted people's attention, but the performance of this material at high rates is very unsatisfactory, which limits its application in power batteries [Young-SikHong, YongJoonPark, et al., SolidStateIonics, 2005, 176: 1035-1042].
近年来,FeF3材料由于其容量高、原材料价格低而进入了研究者的视野。FeF3材料与传统锂离子电池正极材料的工作原理有所不同,传统的锂离子电池正极和负极都存在锂离子可以嵌入或脱嵌的空间,而电解质中的锂离子在正极和负极之间来回嵌入和脱嵌而放电正如Armand等所提出的“摇椅”电池。而FeF3则是一种转换材料,也就是在整个放电过程中,FeF3发生如下的变化[BadwayF,CosandeyF,PereiraN,etal.,ElectrodesforLiBatteries,J.Electrochem.Soc.,2003,150(10):A1318-A1327.]: In recent years, FeF3 material has entered the field of vision of researchers due to its high capacity and low raw material price. The working principle of FeF 3 material is different from that of traditional lithium-ion battery cathode materials. There are spaces for lithium ions to intercalate or deintercalate in both the positive and negative electrodes of traditional lithium-ion batteries, while the lithium ions in the electrolyte travel back and forth between the positive and negative electrodes. Intercalation and deintercalation with discharge as proposed by Armand et al. "rocking chair" battery. FeF3 is a conversion material, that is, during the entire discharge process, FeF3 undergoes the following changes [BadwayF, CosandeyF, PereiraN, et al., ElectrodesforLiBatteries, J. Electrochem.Soc., 2003, 150(10): A1318-A1327.]:
Li++FeF3+e→LiFeF3----(1) Li + +FeF 3 +e→LiFeF 3 ----(1)
LiFeF3+2Li++2e→3LiF+Fe-(2) LiFeF 3 +2Li + +2e→3LiF+Fe-(2)
第一步与也就是传统锂离子的锂离子嵌入,整个反应过程中晶格没有大的变化;而第二部为金属的置换反应,母体晶格完全发生了转换。第一步的理论容量为237mAh.g-1;完全反应能实现3电子的转化,即第二阶段的理论容量为474mAh.g-1;总容量为711mAh.g-1;虽然该材料没有明确的放电平台,平均放电电压也比较低,但其接近800mAh.g-1的理论比容量还是获得了材料研究人员高度的重视。然而,经过如Arai,Amatucci[BadwayF,PereiraN,CosandeyF,etal.,J.Electrochem.Soc.,2003,150(9):A1209-A1218.]等学者的研究发现,要将其理论容量大部分释放出来并不是一件容易的事情。首先FeF3的电子导电能力非常差,同时其锂离子电导率也很低,而且转换后的产物LiF是电子绝缘体,同时传导锂离子的能力也很差,从而造成了FeF3材料能利用的有效容量较低,充放电电流小,倍率特性差;充放电过程中的极化较为严重,充放电电压平台差距很大;容量保持能力不佳,随着充放电次数的增加,容量衰减严重。在研究的早期只能释放约50-100mAh.g-1的可逆容量;后来Amatucci等通过与碳材料经过长时间高能球磨形成碳/氟化铁纳米复合物(CMFNCs)改善了其导电能力,大大提高了其电化学性能,其放电容量能达到200mAh.g-1左右[BadwayF,MansourA.N,PereiraN,etal.,Chem.Mater.,2007,19(17):4129-4141.]。但是,碳材料在正极材料颗粒表面上的附着主要靠物理吸附,构成完整碳导电链路比较难。在此,如前所述,该材料的放电电压比较低,有效的能量密度并不是太出色;最后,因为FeF3材料微溶于冷水,所以通常采用乙醇液相的方法制备,在合成过程中需要使用大量的乙醇,经济性不佳。不适于在工业化应用。 The first step is the lithium ion intercalation of traditional lithium ions, and the lattice does not change much during the whole reaction process; while the second step is the metal replacement reaction, the matrix lattice is completely transformed. The theoretical capacity of the first step is 237mAh.g -1 ; the complete reaction can realize the conversion of 3 electrons, that is, the theoretical capacity of the second stage is 474mAh.g -1 ; the total capacity is 711mAh.g -1 ; although the material is not clearly The discharge platform has a relatively low average discharge voltage, but its theoretical specific capacity close to 800mAh.g -1 has been highly valued by material researchers. However, after studies by scholars such as Arai, Amatucci [BadwayF, PereiraN, CosandeyF, et al., J. Electrochem.Soc., 2003, 150(9): A1209-A1218.] found that most of its theoretical capacity should be released Getting out is not an easy task. First of all, the electronic conductivity of FeF 3 is very poor, and its lithium ion conductivity is also very low, and the converted product LiF is an electronic insulator, and the ability to conduct lithium ions is also very poor, resulting in the effective utilization of FeF 3 materials. The capacity is low, the charge and discharge current is small, and the rate characteristics are poor; the polarization during the charge and discharge process is serious, and the charge and discharge voltage platform is very different; the capacity retention is not good, and the capacity decays seriously with the increase of charge and discharge times. In the early stage of research, only a reversible capacity of about 50-100mAh.g -1 could be released; later, Amatucci et al. improved their electrical conductivity by forming carbon/iron fluoride nanocomposites (CMFNCs) with carbon materials after long-term high-energy ball milling, which greatly Its electrochemical performance is improved, and its discharge capacity can reach about 200mAh.g -1 [BadwayF, MansourA.N, PereiraN, et al., Chem.Mater., 2007, 19(17): 4129-4141.]. However, the attachment of carbon materials on the surface of positive electrode material particles mainly depends on physical adsorption, and it is difficult to form a complete carbon conductive link. Here, as mentioned earlier, the discharge voltage of this material is relatively low, and the effective energy density is not very good; finally, because FeF 3 material is slightly soluble in cold water, it is usually prepared by the ethanol liquid phase method, during the synthesis process A large amount of ethanol needs to be used, which is not economical. Not suitable for industrial applications.
因此,提高FeF3正极材料的电化学性能需要探寻一种能够提高锂离子电导率及能量密度的方法,同时使得制备流程尽可能简单、成本低、方便快捷,这对FeF3正极材料的开发和应用尤为重要。 Therefore, to improve the electrochemical performance of FeF 3 positive electrode materials, it is necessary to find a method that can improve the conductivity and energy density of lithium ions, and at the same time make the preparation process as simple as possible, low in cost, convenient and quick, which is of great importance to the development and development of FeF 3 positive electrode materials. Application is especially important.
发明内容 Contents of the invention
本发明针对现有背景技术提出了一种Cu2+,Ce4+,Ag+掺杂改性氟化铁正极材料及制备方法。该方法将铜盐、铈盐、银盐与合成原料在高能球磨机中经过一段时间球磨并热处理后即得到FeF3正极材料。Cu2+通过部分占据FeF3铁离子配位,有助于提高其放电电位,提高能量密度;而通过高价Ce4+掺杂,有助于提高材料的比容量;通过Ag+掺杂,降低充电时转换反应活化能,这样有助于提高其倍率特性、能量密度及循环性能,从而提高该材料的综合电化学性能。 The present invention proposes a Cu2 + , Ce 4+ , Ag + doped modified ferric fluoride cathode material and a preparation method aiming at the existing background technology. In the method, copper salt, cerium salt, silver salt and synthetic raw materials are ball-milled in a high-energy ball mill for a period of time and heat-treated to obtain the FeF3 positive electrode material. Cu2 + helps to increase its discharge potential and energy density by partially occupying FeF 3 iron ion coordination; and through high-valence Ce 4+ doping, it helps to increase the specific capacity of the material; through Ag + doping, it reduces the charge Time conversion reaction activation energy, which helps to improve its rate characteristics, energy density and cycle performance, thereby improving the comprehensive electrochemical performance of the material.
Cu2+,Ce4+,Ag+掺杂改性氟化铁正极材料及制备方法,其特征在于将含结晶水铁盐和氟化铵(摩尔比为1.0∶3.0-3.6)与重量百分比为3-15%的铜盐、铈盐、银盐、重量百分比为0.1-3.0%的乙醇、重量百分比为0.5-3.0%的助剂,在高能球磨机中气氛保护下常温球磨5-20小时后,取出物料,在5%氢气与95%氩气的混合气体保护下升温到300-450度恒温2-10小时后冷却,制备得到Cu2+,Ce4+,Ag+掺杂改性的FeF3复合正极材料。 Cu 2+ , Ce 4+ , Ag + doped modified ferric fluoride cathode material and its preparation method, characterized in that the ratio by weight of ferric salt containing crystalline water and ammonium fluoride (molar ratio is 1.0:3.0-3.6) is 3-15% of copper salt, cerium salt, silver salt, 0.1-3.0% by weight of ethanol, 0.5-3.0% by weight of additives, after 5-20 hours of ball milling at room temperature under the protection of atmosphere in a high-energy ball mill, Take out the material, heat up to 300-450 degrees under the protection of a mixed gas of 5% hydrogen and 95% argon for 2-10 hours, and then cool down to prepare Cu2 + , Ce 4+ , Ag + doped modified FeF 3 composite Cathode material.
上述的含结晶水铁盐为Fe(NO3)3·9H2O,FeCl3·6H2O和Fe2(SO4)3·9H2O中的一种; The above-mentioned iron salt containing crystalline water is one of Fe(NO 3 ) 3 9H 2 O, FeCl 3 6H 2 O and Fe 2 (SO 4 ) 3 9H 2 O;
上述的铜盐为Cu(C2O4)·0.5H2O,Cu(NO3)2·3H2O和CuSO4·5H2O中的一种; The above-mentioned copper salt is one of Cu(C 2 O 4 )·0.5H 2 O, Cu(NO 3 ) 2 ·3H 2 O and CuSO 4 ·5H 2 O;
上述的铈盐为Ce(NH4)2(NO3)6; The above-mentioned cerium salt is Ce(NH 4 ) 2 (NO 3 ) 6 ;
上述的银盐为AgNO3; The above-mentioned silver salt is AgNO 3 ;
上述的助剂为吐温-80,span-60及tx-10中的一种; The above-mentioned additive is one of Tween-80, span-60 and tx-10;
上述的气氛为高纯氮气或高纯氩气; The above-mentioned atmosphere is high-purity nitrogen or high-purity argon;
图1为该材料的前10次循环的充电容量、放电容量和充放电效率图,电压区间2.0V-4.0V,充放电电流0.1C。 Figure 1 is a diagram of the charge capacity, discharge capacity and charge-discharge efficiency of the material in the first 10 cycles, the voltage range is 2.0V-4.0V, and the charge-discharge current is 0.1C.
与现有技术相比,本发明的优点在于:Cu2+通过部分占据FeF3铁离子配位,有助于提高其放电电位,提高能量密度;而通过高价Ce4+掺杂,有助于提高材料的比容量;通过Ag+掺杂,降低充电时转换反应活化能;通过Cu2+,Ce4+,Ag+共掺杂从而提高该材料的综合电化学性能。 Compared with the prior art, the present invention has the advantages of: Cu 2+ helps to improve its discharge potential and energy density by partially occupying FeF 3 iron ion coordination; and through high-valence Ce 4+ doping, it helps Improve the specific capacity of the material; through Ag + doping, reduce the conversion reaction activation energy during charging; through Cu 2+ , Ce 4+ , Ag + co-doping to improve the comprehensive electrochemical performance of the material.
附图说明 Description of drawings
图1该材料的前10次循环的充电容量、放电容量和充放电效率图,电压区间2.0V-4.0V,充放电电流0.1C。 Figure 1 is the charge capacity, discharge capacity and charge-discharge efficiency diagram of the material for the first 10 cycles, the voltage range is 2.0V-4.0V, and the charge-discharge current is 0.1C.
具体实施方式 detailed description
以下结合实施实例对本发明作进一步详细描述。 The present invention will be further described in detail below in conjunction with the implementation examples.
实施例1:将Fe(NO3)3·9H2O和氟化铵(摩尔比为1.0∶3.2)与重量百分比为3.2%的Cu(C2O4)·0.5H2O、重量百分比为3%的Ce(NH4)2(NO3)6、重量百分比为4%的AgNO3、重量百分比为0.6%的吐温-80及重量百分比为0.5%的乙醇在高能球磨机中高纯氮气保护下常温球磨5小时后,取出物料,在5%氢气与95%氩气的混合气体保护下升温到450度恒温3小时后冷却,制备得到Cu2+,Ce4+,Ag+掺杂改性的FeF3正极材料。 Example 1: Fe(NO 3 ) 3 9H 2 O and ammonium fluoride (molar ratio 1.0:3.2) and 3.2% by weight of Cu(C 2 O 4 )·0.5H 2 O, the weight percentage is 3% Ce(NH 4 ) 2 (NO 3 ) 6 , 4% by weight of AgNO 3 , 0.6% by weight of Tween-80 and 0.5% by weight of ethanol in a high-energy ball mill under the protection of high-purity nitrogen After 5 hours of ball milling at room temperature, the material was taken out, heated to 450 degrees under the protection of a mixed gas of 5% hydrogen and 95% argon, and then cooled for 3 hours to prepare Cu 2+ , Ce 4+ , Ag + doped modified FeF 3 cathode material.
实施例2:将FeCl3·6H2O和氟化铵(摩尔比为1.0∶3.6)与重量百分比为6.5%的Cu(C2O4)·0.5H2O、重量百分比为13%的Ce(NH4)2(NO3)6、重量百分比为8%的AgNO3、重量百分比为0.9%的span-60及重量百分比为1.0%的乙醇在高能球磨机中高纯氮气保护下常温球磨20小时后,取出物料,在5%氢气与95%氩气的混合气体保护下升温到400度恒温6.5小时后冷却,制备得到Cu2+,Ce4+,Ag+掺杂改性的FeF3正极材料。 Example 2: Combining FeCl 3 .6H 2 O and ammonium fluoride (molar ratio 1.0:3.6) with 6.5% by weight of Cu(C 2 O 4 )·0.5H 2 O and 13% by weight of Ce (NH 4 ) 2 (NO 3 ) 6 , AgNO 3 with a weight percentage of 8%, span-60 with a weight percentage of 0.9% and ethanol with a weight percentage of 1.0% were ball milled at room temperature for 20 hours in a high-energy ball mill under the protection of high-purity nitrogen. , take out the material, under the protection of the mixed gas of 5% hydrogen and 95% argon, the temperature is raised to 400°C for 6.5 hours and then cooled to prepare Cu 2+ , Ce 4+ , Ag + doped modified FeF 3 cathode material.
实施例3:将Fe2(SO4)3·9H2O和氟化铵(摩尔比为1.0∶3.5)与重量百分比为15%的Cu(NO3)2·3H2O、重量百分比为7.5%的Ce(NH4)2(NO3)6、重量百分比为13%的AgNO3、重量百分比为1.5%的吐温-80及重量百分比为2.0%的乙醇在高能球磨机中高纯氩气保护下常温球磨10小时后,取出物料,在5%氢气与95%氩气的混合气体保护下升温到350度恒温8.5小时后冷却,制备得到Cu2+,Ce4+,Ag+掺杂改性的FeF3正极材料。 Example 3: Combining Fe 2 (SO 4 ) 3 .9H 2 O and ammonium fluoride (molar ratio 1.0:3.5) with 15% by weight Cu(NO 3 ) 2 .3H 2 O, 7.5% by weight % Ce(NH 4 ) 2 (NO 3 ) 6 , 13% by weight of AgNO 3 , 1.5% by weight of Tween-80 and 2.0% by weight of ethanol in a high-energy ball mill under the protection of high-purity argon After 10 hours of ball milling at room temperature, the material was taken out, heated to 350 degrees under the protection of a mixed gas of 5% hydrogen and 95% argon, and then cooled for 8.5 hours to prepare Cu2 + , Ce 4+ , Ag + doped modified FeF 3 Cathode material.
实施例4:将FeCl3·6H2O和氟化铵(摩尔比为1.0∶3.3)与重量百分比为8%的CuSO4·5H2O、重量百分比为5.5%的Ce(NH4)2(NO3)6、重量百分比为6%的AgNO3、重量百分比为3.0%的tx-10及重量百分比为3.0%的乙醇在高能球磨机中高纯氩气保护下常温球磨15小时后,取出物料,在5%氢气与95%氩气的混合气体保护下升温到450度恒温10小时后冷却,制备得到Cu2+,Ce4+,Ag+掺杂改性的FeF3正极材料。 Example 4: Combining FeCl 3 .6H 2 O and ammonium fluoride (molar ratio 1.0:3.3) with 8% by weight of CuSO 4 .5H 2 O and 5.5% by weight of Ce(NH 4 ) 2 ( NO 3 ) 6 , AgNO 3 with a weight percentage of 6%, tx-10 with a weight percentage of 3.0% and ethanol with a weight percentage of 3.0% were ball milled at room temperature for 15 hours under the protection of high-purity argon in a high-energy ball mill, and then the materials were taken out and placed in Under the protection of a mixed gas of 5% hydrogen and 95% argon, the temperature was raised to 450°C for 10 hours and then cooled to prepare a Cu 2+ , Ce 4+ , Ag + doped modified FeF 3 cathode material.
实施例5:将Fe(NO3)3·9H2O和氟化铵(摩尔比为1.0∶3.5)与重量百分比为8%的CuSO4·5H2O、重量百分比为5.6%的Ce(NH4)2(NO3)6、重量百分比为11%的AgNO3、重量百分比为2.0%的span-60及重量百分比为0.1%的乙醇在高能球磨机中高纯氮气保护下常温球磨12小时后,取出物料,在5%氢气与95%氩气的混合气体保护下升温到300度恒温6小时后冷却,制备得到Cu2+,Ce4+,Ag+掺杂改性的FeF3正极材料。 Example 5: Combining Fe(NO 3 ) 3 .9H 2 O and ammonium fluoride (molar ratio 1.0:3.5) with 8% by weight of CuSO 4 .5H 2 O and 5.6% by weight of Ce(NH 4 ) 2 (NO 3 ) 6 , 11% by weight of AgNO 3 , 2.0% by weight of span-60, and 0.1% by weight of ethanol were ball milled in a high-energy ball mill at room temperature for 12 hours under the protection of high-purity nitrogen, and then taken out The material is heated to 300 degrees under the protection of a mixed gas of 5% hydrogen and 95% argon for 6 hours and then cooled to prepare Cu 2+ , Ce 4+ , Ag + doped modified FeF 3 cathode material.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410348459.0A CN104150543B (en) | 2014-07-14 | 2014-07-14 | A kind of Cu 2+, Ce 4+, Ag +doping ferric fluoride composite positive pole and preparation method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410348459.0A CN104150543B (en) | 2014-07-14 | 2014-07-14 | A kind of Cu 2+, Ce 4+, Ag +doping ferric fluoride composite positive pole and preparation method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104150543A CN104150543A (en) | 2014-11-19 |
CN104150543B true CN104150543B (en) | 2016-04-20 |
Family
ID=51876214
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410348459.0A Expired - Fee Related CN104150543B (en) | 2014-07-14 | 2014-07-14 | A kind of Cu 2+, Ce 4+, Ag +doping ferric fluoride composite positive pole and preparation method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104150543B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104795539B (en) * | 2015-04-19 | 2017-08-29 | 宁波大学 | A kind of liquid phase synthesis Cu2+,Fe3+Sheet of adulterating fluorination bismuth anode material for lithium-ion batteries and preparation method thereof |
CN104795536B (en) * | 2015-04-19 | 2017-08-29 | 宁波大学 | A kind of liquid phase synthesis B3+, La3+Orthohormbic structure of adulterating fluorination bismuth anode material for lithium-ion batteries and preparation method thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4938945A (en) * | 1988-10-18 | 1990-07-03 | Pennwalt Corporation | High purity anhydrous FeF3 and process for its manufacture |
CN103165888A (en) * | 2013-03-02 | 2013-06-19 | 合肥国轩高科动力能源股份公司 | Preparation method of ferric three fluoride (FeF3) nanorod with embedded lithium activity |
CN103199253A (en) * | 2013-03-31 | 2013-07-10 | 马军昌 | Preparation method of graphene-ferric fluoride composite cathode material |
CN103515598A (en) * | 2013-09-18 | 2014-01-15 | 宁波大学 | Aluminum zirconium acid ester-doped titanium phosphate double-component surface-modified ferric fluoride anode material and preparation method |
-
2014
- 2014-07-14 CN CN201410348459.0A patent/CN104150543B/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4938945A (en) * | 1988-10-18 | 1990-07-03 | Pennwalt Corporation | High purity anhydrous FeF3 and process for its manufacture |
CN103165888A (en) * | 2013-03-02 | 2013-06-19 | 合肥国轩高科动力能源股份公司 | Preparation method of ferric three fluoride (FeF3) nanorod with embedded lithium activity |
CN103199253A (en) * | 2013-03-31 | 2013-07-10 | 马军昌 | Preparation method of graphene-ferric fluoride composite cathode material |
CN103515598A (en) * | 2013-09-18 | 2014-01-15 | 宁波大学 | Aluminum zirconium acid ester-doped titanium phosphate double-component surface-modified ferric fluoride anode material and preparation method |
Also Published As
Publication number | Publication date |
---|---|
CN104150543A (en) | 2014-11-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104241642B (en) | Lithium molybdate negative material of lithium ion battery and preparation method thereof | |
CN104176785B (en) | A kind of Cu2+,Co2+,Ce4+,Ag+Doping ferric flouride composite positive pole and preparation method | |
CN104150542B (en) | A Cu2+, co2+, ag+doped iron fluoride composite anode material and its preparation method | |
CN103700814B (en) | A kind of carbon solid acid aluminum zirconate doping phosphoric acid titanium lithium three component surface modification ferric fluoride anode material and preparation method | |
CN104157836B (en) | A kind of Cu2+, Co2+, Zr4+, Ag+ doped ferric fluoride composite cathode material and preparation method | |
CN104795538A (en) | Solid-phase synthesis oxygen bearing bismuth fluoride anode material for lithium ion battery and preparation method thereof | |
CN104150543B (en) | A kind of Cu 2+, Ce 4+, Ag +doping ferric fluoride composite positive pole and preparation method | |
CN103500830B (en) | A kind of nitrogen doped silicon carbide assisted Solid-state one-step method ferric flouride lithium electricity positive electrode and preparation method | |
CN103490048B (en) | The two component surface modification ferric fluoride anode materials of a kind of titanate esters doping phosphoric acid titanium lithium and preparation method | |
CN103500817B (en) | A kind of silane doping phosphoric acid titanium lithium double-component surface-modified ferric fluoride anode and preparation method | |
CN103682267B (en) | A kind of carbon solid acid Aluminate doping phosphoric acid titanium lithium three component surface modification ferric fluoride anode material and preparation methods | |
CN103515598B (en) | The two component surface modification ferric fluoride anode materials of a kind of aluminium zirconate doping phosphoric acid titanium lithium and preparation method | |
CN103500810B (en) | A kind of carbon solid acid borate doping phosphoric acid titanium lithium three component surface modification ferric fluoride anode material and preparation methods | |
CN105914347A (en) | A Fe2O3|FeF3-2xOx|Fe3+, Co2+ doped bismuth fluoride layer structure lithium battery cathode material and its preparation method | |
CN105914348A (en) | A Gradient Structure Covered Bi3+, B3+ Doped Copper Fluoride Lithium Electrode Material and Its Preparation Method | |
CN103500818B (en) | The two component surface modification ferric fluoride anode materials of a kind of Aluminate doping phosphoric acid titanium lithium and preparation method | |
CN103500834B (en) | The two component surface modification ferric fluoride anode materials of a kind of borate doping phosphoric acid titanium lithium and preparation method | |
CN104157837B (en) | A kind of Cu2+, Mn2+, Zr4+, Ag+ doping ferric flouride composite positive pole and preparation method | |
CN104882602B (en) | A kind of synthesis in solid state Al3+,Cu2+Adulterate cubic structure fluorination bismuth anode material for lithium-ion batteries and preparation method thereof | |
CN104900853B (en) | A kind of synthesis in solid state Co2+Doping fluorination bismuth anode material for lithium-ion batteries and preparation method thereof | |
CN103490068B (en) | A kind of carboxyl carbon titanate esters doping phosphoric acid titanium lithium three component surface modification ferric fluoride anode material and preparation methods | |
CN104795537B (en) | A kind of synthesis in solid state Co2+,Cu2+Orthohormbic structure of adulterating fluorination bismuth anode material for lithium-ion batteries and preparation method thereof | |
CN103500816B (en) | A kind of carbon solid acid silane doping phosphoric acid titanium lithium three component surface modification ferric fluoride anode material and preparation method | |
CN105914350A (en) | A Fe2O3|FeF3-2xOx|Fe3+, Ce4+ doped zirconium fluoride layer structure lithium battery cathode material and its preparation method | |
CN105742604A (en) | A Bi2O3|BiF3-2xOx|Bi3+, Mg2+ doped iron fluoride layer structure lithium battery cathode material and its preparation method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20200102 Address after: 313000 No.5-8, Changhe Road, Huaxi street, Changxing County, Huzhou City, Zhejiang Province Patentee after: Zhejiang Changxing green battery technology Co.,Ltd. Address before: Room 1,020, Nanxun Science and Technology Pioneering Park, No. 666 Chaoyang Road, Nanxun District, Huzhou City, Zhejiang Province, 313000 Patentee before: Huzhou You Yan Intellectual Property Service Co.,Ltd. Effective date of registration: 20200102 Address after: Room 1,020, Nanxun Science and Technology Pioneering Park, No. 666 Chaoyang Road, Nanxun District, Huzhou City, Zhejiang Province, 313000 Patentee after: Huzhou You Yan Intellectual Property Service Co.,Ltd. Address before: Box No. 29 No. 818 315211 Ningbo University Zhejiang province Ningbo City Fenghua Road, Jiangbei District Patentee before: Ningbo University |
|
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20200917 Address after: Room 501, Office Building of Market Supervision Bureau of Langchuan Avenue, Jianping Town, Langxi County, Xuancheng City, Anhui Province Patentee after: Langxi pinxu Technology Development Co.,Ltd. Address before: 313000 No.5-8, Changhe Road, Huaxi street, Changxing County, Huzhou City, Zhejiang Province Patentee before: Zhejiang Changxing green battery technology Co.,Ltd. |
|
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20221209 Address after: 276000 west of jiangouya village, Luoxi street, high tech Zone, Linyi City, Shandong Province Patentee after: SHANDONG GEXIN PRECISION CO.,LTD. Address before: Room 501, office building, Langchuan Avenue, Jianping Town, Langxi County, Xuancheng City, Anhui Province Patentee before: Langxi pinxu Technology Development Co.,Ltd. |
|
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160420 |