[go: up one dir, main page]

CN1395332A - LiCoO2 type cathode material and its preparation method - Google Patents

LiCoO2 type cathode material and its preparation method Download PDF

Info

Publication number
CN1395332A
CN1395332A CN01120209A CN01120209A CN1395332A CN 1395332 A CN1395332 A CN 1395332A CN 01120209 A CN01120209 A CN 01120209A CN 01120209 A CN01120209 A CN 01120209A CN 1395332 A CN1395332 A CN 1395332A
Authority
CN
China
Prior art keywords
lico
licoo
rare earth
type cathode
cathode material
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.)
Granted
Application number
CN01120209A
Other languages
Chinese (zh)
Other versions
CN1165091C (en
Inventor
周利
衣宝廉
林化新
张华民
何长青
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dalian Institute of Chemical Physics of CAS
Original Assignee
Dalian Institute of Chemical Physics of CAS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dalian Institute of Chemical Physics of CAS filed Critical Dalian Institute of Chemical Physics of CAS
Priority to CNB011202092A priority Critical patent/CN1165091C/en
Publication of CN1395332A publication Critical patent/CN1395332A/en
Application granted granted Critical
Publication of CN1165091C publication Critical patent/CN1165091C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/14Fuel cells with fused electrolytes
    • H01M8/144Fuel cells with fused electrolytes characterised by the electrolyte material
    • H01M8/145Fuel cells with fused electrolytes characterised by the electrolyte material comprising carbonates
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/8605Porous electrodes
    • H01M4/8621Porous electrodes containing only metallic or ceramic material, e.g. made by sintering or sputtering
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Ceramic Engineering (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

一种LiCoO2型阴极材料,其特征在于由以下结构式表示:LiCo1-xMxO2其中,M为碱土金属元素Be、Mg、Ca或Sr中一种或一种以上,x=0.05-0.10。该材料的制备按下述步骤:(1)按LiCo1-xMxO2 (式中x=0.05-0.10,M为Be、Mg、Ca或Sr中一种或一种以上)结构式中Li、Co、M元素的摩尔比称取含Li、Co、M的原料,并混合成配料;(2)用球磨机粉碎配料成粒径小于300μm的微粉;(3)在600-800℃高温下焙烧微粉1小时以上得到氧化物。A LiCoO 2 -type cathode material is characterized in that it is represented by the following structural formula: LiCo 1-x M x O 2 wherein, M is one or more of alkaline earth metal elements Be, Mg, Ca or Sr, and x=0.05- 0.10. The material is prepared according to the following steps: (1) according to LiCo 1-x M x O 2 (wherein x=0.05-0.10, M is one or more than one of Be, Mg, Ca or Sr) Li in the structural formula , Co, M molar ratio Weigh raw materials containing Li, Co, M, and mix them into ingredients; (2) Use a ball mill to pulverize the ingredients into fine powders with a particle size of less than 300 μm; (3) Roast at 600-800°C Micropowder for more than 1 hour to obtain oxides.

Description

一种LiCoO2型阴极材料及其制备方法 A kind of LiCoO2 type cathode material and preparation method thereof

技术领域technical field

本发明涉及一种燃料电池的阴极,特别是提供一种用于熔融碳酸盐燃料电池(MCFC)的阴极材料及其制备方法。The invention relates to a cathode of a fuel cell, in particular to a cathode material for a molten carbonate fuel cell (MCFC) and a preparation method thereof.

背景技术Background technique

燃料电池是一种将燃料与氧化剂中的化学能直接转化为电能的发电装置。它不经过热机过程,所以不受卡诺循环的限制,能量转化效率很高。同时,它又是一种清洁无污染的发电装置。其中,熔融碳酸盐燃料电池(MCFC)是操作于600-700℃一种高温发电装置,除了具有不受卡诺循环限制、能量利用率高和环境友好等特点外,还具有许多其它种类燃料电池无法比拟的优点,如燃料适用范围广,除了H2、CO外,还可直接用天然气、煤气化气和其它碳氢化合物作燃料,同时无需采用贵金属电极,可大大降低电池的成本等。但由于目前仍存在隔膜烧结、阴极腐蚀溶解,阳极蠕变及双极板腐蚀这四大技术难题,MCFC一直未能进入商品化。A fuel cell is a power generating device that directly converts the chemical energy in fuel and oxidant into electrical energy. It does not go through the heat engine process, so it is not limited by the Carnot cycle, and the energy conversion efficiency is very high. At the same time, it is a clean and pollution-free power generation device. Among them, the molten carbonate fuel cell (MCFC) is a high-temperature power generation device operating at 600-700 ° C. In addition to its characteristics of not being limited by the Carnot cycle, high energy utilization rate and environmental friendliness, it also has many other types of fuels. The incomparable advantages of batteries, such as a wide range of fuels, in addition to H 2 and CO, can also directly use natural gas, coal gasification gas and other hydrocarbons as fuels, and at the same time do not need to use noble metal electrodes, which can greatly reduce the cost of batteries. However, due to the four major technical problems of diaphragm sintering, cathode corrosion and dissolution, anode creep and bipolar plate corrosion, MCFC has not been commercialized.

MCFC阴极主要起提供氧化剂还原反应活性位,催化阴极反应,提供反应物通道及传递电子作用,所以一般选用具有催化作用的多孔电子良导体。传统上,MCFC阴极为多孔镍板。用此多孔镍板组装成电池后,在氧化剂的气氛中,它原位氧化为NiO,成为MCFC阴极。但人们发现NiO易溶解于熔融碳酸盐之中,阴极消耗,结构发生变化,阴极极化不断增大,导致电池性能衰减,更为严重的是溶解后的Ni+2通过隔膜扩散到阳极侧,在阳极侧还原沉积,最终与阴极连成镍桥,导致电池短路。所以,阴极材料的NiO溶解是影响电池寿命的主要因素之一。为了消除这一影响,人们纷纷探索新的阴极材料及新制备工艺,对Ni(或NiO)进行表面修饰或以其他阴极材料完全替代NiO。替代阴极材料有钙钛矿材料、Li/Mg/Fe(Mn)/O复合材料等特别是以LiCoO2、LiFeO2等较为适宜。其中以LiCoO2最为适宜。由于以纯LiCoO2作阴极,虽然在一定程度上克服了阴极溶解问题,但其电导过低,电池性能偏差。所以对LiCoO2进行改性处理,成为提高其电导新的出发点。The MCFC cathode is mainly used to provide active sites for oxidant reduction reaction, catalyze the cathode reaction, provide reactant channels and transfer electrons, so a porous electronic conductor with catalytic effect is generally selected. Traditionally, MCFC cathodes have been porous nickel plates. After the battery is assembled with this porous nickel plate, it is oxidized to NiO in situ in the atmosphere of oxidizing agent, and becomes the cathode of MCFC. However, it is found that NiO is easily dissolved in molten carbonate, the cathode is consumed, the structure changes, and the cathode polarization continues to increase, resulting in battery performance degradation. What is more serious is that the dissolved Ni +2 diffuses to the anode side through the separator. , reductively deposited on the anode side, and finally connected to the cathode to form a nickel bridge, resulting in a short circuit of the battery. Therefore, the NiO dissolution of the cathode material is one of the main factors affecting the battery life. In order to eliminate this effect, people have been exploring new cathode materials and new preparation processes, modifying the surface of Ni (or NiO) or completely replacing NiO with other cathode materials. Alternative cathode materials include perovskite materials, Li/Mg/Fe(Mn)/O composite materials, etc. LiCoO 2 and LiFeO 2 are more suitable. Among them, LiCoO 2 is most suitable. Since pure LiCoO2 is used as the cathode, although the cathode dissolution problem is overcome to a certain extent, its conductance is too low and the performance of the battery deviates. Therefore, the modification of LiCoO 2 has become a new starting point to improve its electrical conductivity.

USP 5356731中将0.5mol LiNO3、0.5mol Co(NO3)2与1.5mol柠檬酸及2.25mol硝酸铵配制为1.5升水溶液,均匀搅拌,加热蒸发,至着火点进行反应,于500℃下焙烧8小时除去碳,用带铸法制膜,再于空气和CO2的气氛中800-1000℃烧结,制备LiCoO2电极。In USP 5356731, 0.5 mol LiNO 3 , 0.5 mol Co(NO 3 ) 2 , 1.5 mol citric acid and 2.25 mol ammonium nitrate were prepared into 1.5 liters of aqueous solution, stirred evenly, heated and evaporated, reacted at the ignition point, and roasted at 500°C for 8 The carbon is removed within hours, the film is formed by tape casting, and then sintered at 800-1000°C in an atmosphere of air and CO 2 to prepare a LiCoO 2 electrode.

USP 6063141用阳极氧化法制备LiCoO2,以Co2O3及Li2CO3为原料制备LiCoO2,并以阳极氧化法制备出LiCoO2及理化NiO双层阴极。其极化阻抗为0.2Ωcm2,150mA/cm2时过电位为30mV。USP 6063141 prepares LiCoO 2 by anodic oxidation, uses Co 2 O 3 and Li 2 CO 3 as raw materials to prepare LiCoO 2 , and prepares LiCoO 2 and physical and chemical NiO double-layer cathode by anodic oxidation. Its polarization impedance is 0.2Ωcm 2 , and its overpotential is 30mV at 150mA/cm 2 .

WO 9728571 A1以Li2CO3粉和金属Co粉均匀混合制成薄膜,经过烧结,在400-488℃温度下空气流中处理几小时,直至转化为具有较大内表面的LiCoO2电极板。WO 9728571 A1 uniformly mixes Li 2 CO 3 powder and metal Co powder to make a thin film, sinters, and treats it in an air flow at a temperature of 400-488 ° C for several hours until it is transformed into a LiCoO 2 electrode plate with a large inner surface.

WO 9853513 A1制备出具有双层结构的阴极,一层为理化NiO,另一层为铈化的LiCoO2,双层电极的极化阻抗随温度影响极小,具有较长活性寿命。第二电极层的制备材料为活化的氧化钴与铈共沉淀,用碳酸锂处理形成恳浮液。将悬浮液涂到第一层上,经过干燥和高温烧结就形成第二电极层。WO 9853513 A1 prepared a cathode with a double-layer structure, one layer is physical and chemical NiO, and the other layer is cerified LiCoO 2 . The polarization resistance of the double-layer electrode has little influence with temperature and has a long active life. The preparation material of the second electrode layer is co-precipitation of activated cobalt oxide and cerium, which is treated with lithium carbonate to form a floating liquid. The suspension is applied to the first layer, dried and sintered at high temperature to form the second electrode layer.

WO 008702 A1阐述了直接制备出含有电解质的电极板的方法。用这种方法制备出阴极可以有二层或更多层组成,开始将由LiCoO2和碳酸盐组成的混合物制成膜板,在加热炉中加热使电解质熔融。WO 008702 A1 describes the direct production of electrode plates containing electrolytes. The cathode prepared in this way can consist of two or more layers, starting with a mixture of LiCoO 2 and carbonate to make a membrane plate, which is heated in a furnace to melt the electrolyte.

Eur.Pat.Appl.EP 661767 A1将钴粉和Li2CO3的混合物、粘结剂、消泡剂及溶剂混合,用带铸技术制膜于一平板上,加热处理形成LiCoO2,部分烧结处理产生与MCFC中阴极所需相匹配的孔隙率。Eur.Pat.Appl.EP 661767 A1 Mix the mixture of cobalt powder and Li 2 CO 3 , binder, defoamer and solvent, and use the tape casting technology to form a film on a flat plate, heat treatment to form LiCoO 2 , and partially sinter The treatment produces a porosity that matches that required for the cathode in the MCFC.

但是,上述文献尚未提出提高LiCoO2阴极电导的有效方法。However, the above-mentioned literatures have not yet proposed an effective method to enhance the cathode conductance of LiCoO2 .

发明内容Contents of the invention

本发明的目的是克服上述公知技术中LiCoO2阴极电导性低,电池性能较差的问题,提供一种LiCoO2型阴极电极材料,利用这种电极材料所制备的阴极能大大降低了阴极在熔融碳酸盐中的溶解度,提高了阴极稳定性,延长了电池寿命;提高了阴极本身的电导(其中电导≥NiO的电导)。The purpose of the present invention is to overcome the low electrical conductivity of LiCoO2 cathode in the above-mentioned known technology, and the problem of poor battery performance, to provide a LiCoO2 type cathode electrode material, and the cathode energy prepared by using this electrode material can greatly reduce the negative energy of the cathode during melting. The solubility in carbonate improves the stability of the cathode and prolongs the battery life; it improves the conductance of the cathode itself (where the conductance is greater than or equal to the conductance of NiO).

为实现上述的目的,本发明提供了一种LiCoO2型阴极材料,其特征在于由以下结构式表示:To achieve the above object, the invention provides a LiCoO2 type cathode material, characterized in that it is represented by the following structural formula:

LiCo1-xMxO2 LiCo 1-x M x O 2

其中,M为碱土金属元素Be、Mg、Ca或Sr中一种或一种以上,x=0.05-0.10。Wherein, M is one or more of alkaline earth metal elements Be, Mg, Ca or Sr, and x=0.05-0.10.

在上述的LiCoO2型阴极材料中,其特征在于M为Mg元素。In the above-mentioned LiCoO 2 -type cathode material, it is characterized in that M is a Mg element.

另外,在上述的LiCoO2型阴极材料中,其特征在于LiCo1-xMxO2中还可以掺杂钇和/或稀土元素,其掺杂量按氧化物重量计为LiCo1-xMxO2的10-40%。In addition, in the above-mentioned LiCoO 2 -type cathode material, it is characterized in that LiCo 1-x M x O 2 can also be doped with yttrium and/or rare earth elements, and the doping amount is LiCo 1-x M 10-40% of x O2 .

另外,在上述的LiCoO2型阴极材料中,其特征在于所述的稀土元素为La、Ce、Pr、Na、Pm、Sm、Eu、Gd、Dy中一种或几种。In addition, in the above-mentioned LiCoO 2 -type cathode material, it is characterized in that the rare earth element is one or more of La, Ce, Pr, Na, Pm, Sm, Eu, Gd, Dy.

另外,在上述的LiCoO2型阴极材料中,其特征在于所述的稀土元素为La和/或Ce。In addition, in the above-mentioned LiCoO 2 -type cathode material, it is characterized in that the rare earth element is La and/or Ce.

本发明还提供了一种LiCoO2型阴极材料的制备方法,其特征是按下述步骤:The present invention also provides a kind of preparation method of LiCoO2 type cathode material, it is characterized in that according to the following steps:

1).按LiCo1-xMxO2(式中x=0.05-0.10,M为Be、Mg、Ca或Sr中一种或一种以上)结构式中Li、Co、M元素的摩尔比称取含Li、Co、M的原料,并混合成配料;1). According to the molar ratio of Li, Co and M elements in the structural formula of LiCo 1-x M x O 2 (where x=0.05-0.10, M is one or more of Be, Mg, Ca or Sr) Take raw materials containing Li, Co, M and mix them into ingredients;

2).用球磨机粉碎配料成粒径小于300μm的微粉;2). Use a ball mill to pulverize the ingredients into a fine powder with a particle size of less than 300 μm;

3).在600-800℃高温下焙烧微粉1小时以上得到氧化物。3). Calcining the fine powder at a high temperature of 600-800°C for more than 1 hour to obtain oxides.

在上述球磨中,通常经10小时以上的球磨了为达到所需粒度。为保证得到更好的配料最好进行20-60小时球磨。In the above-mentioned ball milling, the ball milling is usually performed for more than 10 hours in order to achieve the desired particle size. In order to ensure better ingredients, it is best to carry out ball milling for 20-60 hours.

在上述的制备方法中,其特征在于Li、Co、M的原料分别为其硝酸盐、碳酸盐、醋酸盐或氧化物。In the above preparation method, it is characterized in that the raw materials of Li, Co and M are nitrates, carbonates, acetates or oxides respectively.

另外,在上述的制备方法中,其特征在于在步骤1)中按LiCo1-xMxO2量掺杂Y和/或稀土元素以氧化物重量计为10-40%比例将含Y和/或稀土元素的原料加入并混合成配料。In addition, in the above-mentioned preparation method, it is characterized in that in step 1) doping Y and/or rare earth elements in the amount of LiCo 1-x M x O 2 will contain Y and / or raw materials of rare earth elements are added and mixed into ingredients.

另外,在上述的制备方法中,其特征在于所述的Y和/或稀土元素为其硝酸盐、碳酸盐、醋酸盐或氧化物。In addition, in the above preparation method, it is characterized in that the Y and/or rare earth elements are nitrates, carbonates, acetates or oxides.

另外,在上述的制备方法中,其特征在于在步骤3)后进一步按LiCo1-xMxO2,量掺杂Y和/或稀土元素以氧化物重量计为10-40%比例将含Y和/或稀土元素的原料加入并混合成配料。In addition, in the above-mentioned preparation method, it is characterized in that after step 3), Y and/or rare earth elements are further doped with LiCo 1-x M x O 2 in an amount of 10-40% based on the oxide weight. Raw materials of Y and/or rare earth elements are added and mixed into ingredients.

在上述的本发明中,由于以LiCoO2作为阴极基质材料,其溶解速度比NiO阴极低8倍到一个数量级,但其电导低,电极性能偏低。用半导体掺杂法掺杂碱土元素如Mg、Ca、Be、Sr等,含量在0.05-0.10(摩尔比),掺杂后的LiCo1-xMxO2,阴极电导可提高一至五倍左右。同时又用化学吸附法,增加电极对Li+离子吸附,吸附大量Li+离子的LiCo1-xMxO2阴极,其电导又可提高一至三倍左右。这样阴极大幅度提度电导,提高了电池性能,同时又降低了电极溶解速度,增加了电池性能稳定性,延长电池寿命。In the above-mentioned present invention, since LiCoO2 is used as the cathode matrix material, its dissolution rate is 8 times to an order of magnitude lower than that of the NiO cathode, but its electrical conductivity is low, and the electrode performance is low. Use semiconductor doping method to dope alkaline earth elements such as Mg, Ca, Be, Sr, etc., the content is 0.05-0.10 (molar ratio), after doping LiCo 1-x M x O 2 , the cathode conductance can be increased by about 1 to 5 times . At the same time, the chemical adsorption method is used to increase the electrode's adsorption of Li + ions, and the conductivity of the LiCo 1-x M x O 2 cathode that absorbs a large amount of Li + ions can be increased by about one to three times. In this way, the conductivity of the cathode is greatly improved, which improves the performance of the battery, and at the same time reduces the dissolution rate of the electrode, increases the stability of the battery performance, and prolongs the battery life.

另外,在本发明,为了使Li+注入LiCo1-xMxO2晶体层中,进一步增加其电导在LiC1-xMxO2粉料中重掺杂La、Ca、Y等稀土元素。掺杂量按氧化物计为10-40%左右。其原料为碳酸盐,硝酸盐和醋酸盐等。其中以硝酸盐的效果最好。其方法是混合均匀,在高温下分解和烧结。为了增加其在LiCoO2表面的浓度,烧结温度于650℃为宜。低于650℃,稀土元素在LiCoO2表面不均匀,高于650℃,由于热扩散增强,稀土元素在粉料表面的浓度降低。In addition, in the present invention, in order to inject Li + into the LiCo 1-x M x O 2 crystal layer, and further increase its conductance, the LiC 1-x M x O 2 powder is heavily doped with rare earth elements such as La, Ca, Y, etc. . The doping amount is about 10-40% based on oxide. Its raw materials are carbonates, nitrates and acetates. Among them, nitrate has the best effect. The method is to mix evenly, decompose and sinter at high temperature. In order to increase its concentration on the surface of LiCoO 2 , the sintering temperature is preferably 650 °C. Below 650 °C, the rare earth elements are not uniform on the surface of LiCoO2 , and above 650 °C, the concentration of rare earth elements on the powder surface decreases due to the enhanced thermal diffusion.

另外,在本发明中,重掺杂稀土元素的方法是按LiCo1-xMxO2与稀土元素的摩尔比配料,混合均匀,在高温下分解和烧结,再制备成为电极。也可先将配料混合均匀,制备成电极,在电池中高温原位烧结成为氧化物,由于Ce(NO3)3 6H2O在200℃分解,La(NO3)3 6H2O在126℃分解,所以在电池中不仅原位烧结使其成为氧化物,而且此过程在电极起到造孔作用。利用上述本发明所制阴极材料,制成电极,再按常规技术组装成电池,可得到良好的电池性能。具体地说,如果选用多孔烧结Ni-Cr板作阳极, -LiCoO2型阴极组装成单电池,电池性能良好。LiCoO2-掺杂Mg作阴极时,在0.9MPa下,200mA/cm2及300mA/cm2放电时,电池输出电压分别为0.853V和0.721V,最高功率密度为216.3mW/cm2。LiCoO2-掺杂Mg、La作阴极时,在0.9MPa下,200mA/cm2及372mA/cm2放电时,电池输出电压分别为0.944V和0.781V,最高功率密度为291mW/cm2。LiCoO2-掺杂Mg、Ce、La作阴极时,在0.9MPa下,200mA/cm2及300mA/cm2放电时,电池输出电压分别为0.838V和0.685V,最高功率密度为205.5mW/cm2In addition, in the present invention, the method of heavily doping rare earth elements is to mix LiCo 1-x M x O 2 to the molar ratio of rare earth elements, mix evenly, decompose and sinter at high temperature, and then prepare electrodes. It is also possible to mix the ingredients evenly first to prepare an electrode, and in-situ sintering in the battery to form an oxide. Since Ce(NO 3 ) 3 6H 2 O decomposes at 200°C, La(NO 3 ) 3 6H 2 O decomposes at 126°C Decomposition, so in-situ sintering in the battery not only makes it an oxide, but also creates pores in the electrode during this process. Using the above-mentioned cathode material prepared by the present invention to make an electrode, and then assemble it into a battery according to the conventional technology, good battery performance can be obtained. Specifically, if a porous sintered Ni-Cr plate is used as the anode, - LiCoO2 type cathode assembled into a single cell with good battery performance. When LiCoO 2 -doped with Mg is used as the cathode, at 0.9MPa, when discharged at 200mA/cm 2 and 300mA/cm 2 , the battery output voltages are 0.853V and 0.721V respectively, and the highest power density is 216.3mW/cm 2 . When LiCoO 2 -doped with Mg and La is used as the cathode, at 0.9MPa, when discharged at 200mA/cm 2 and 372mA/cm 2 , the battery output voltages are 0.944V and 0.781V respectively, and the highest power density is 291mW/cm 2 . When LiCoO 2 -doped with Mg, Ce, La is used as the cathode, at 0.9MPa, when discharged at 200mA/cm 2 and 300mA/cm 2 , the output voltage of the battery is 0.838V and 0.685V respectively, and the highest power density is 205.5mW/cm 2 .

附图说明Description of drawings

图1为利用本发明实施例1所制得电极材料制作的电极所组装电池在第2次启动时的电池性能曲线图。Fig. 1 is a graph showing the performance curve of a battery assembled with electrodes made of the electrode material obtained in Example 1 of the present invention at the second start-up.

图2为利用本发明实施例2所制得电极材料制作的电极所组装电池在第9次启动时的电池性能曲线图。Fig. 2 is a graph showing the battery performance of the assembled battery using the electrode material prepared in Example 2 of the present invention at the ninth start-up.

图3为利用本发明实施例3所制得电极材料制作的电极所组装电池在第9次启动时的电池性能曲线图。Fig. 3 is a graph showing the performance curve of the battery assembled with electrodes made of the electrode material obtained in Example 3 of the present invention at the ninth start-up.

具体实施方式Detailed ways

下面结合附图对本发明的技术给予进一步的说明。The technology of the present invention will be further described below in conjunction with the accompanying drawings.

实施例1Example 1

在1立升的球磨罐中,加1/3球磨罐体积的瓷球。称取30.03克Co(NO3)3 6H2O,4.15克Li2CO3,0.36克MgO,加入球磨罐中,球磨30小时,使配料颗粒小于100μm。然后在120℃烘箱中烘干,机械粉碎,研磨,在马福炉中从100℃到800℃渐次升温,焙烧20小时,制得LiCo0.92Mg0.08O2粉料。In a 1 liter ball mill jar, add ceramic balls 1/3 of the volume of the ball mill jar. Weigh 30.03 grams of Co(NO 3 ) 3 6H 2 O, 4.15 grams of Li 2 CO 3 , and 0.36 grams of MgO, add them into a ball mill jar, and ball mill for 30 hours to make the ingredients particles smaller than 100 μm. Then it was dried in an oven at 120°C, mechanically crushed, ground, and gradually heated in a muffle furnace from 100°C to 800°C, and calcined for 20 hours to obtain LiCo 0.92 Mg 0.08 O 2 powder.

称取25.6克LiCo0.92Mg0.08O2粉料、12克功能性有机物及80克乙醇-正丁醇溶剂于1立升球磨罐中球磨,经过滤、脱气后,用带铸法制得电极,然后进行干燥,经厚度匹配后用热压机热压成电池用电极。Weigh 25.6 grams of LiCo 0.92 Mg 0.08 O Powder , 12 grams of functional organic matter and 80 grams of ethanol-n-butanol solvent are ball-milled in a 1 liter ball mill jar, after filtering and degassing, the electrode is prepared by strip casting. Then it is dried, and after the thickness is matched, it is hot-pressed with a hot press to form an electrode for a battery.

选用多孔烧结Ni-Cr板作阳极,γ-LiAlO2作隔膜及上述阴极组装成单电池。在650℃电池操作温度的下,经用N2检漏和检窜合析后,阳极通H2-CO2混合气(H2/CO2=80/20,m/o),阴极通O2-CO2混合气(O2/CO2=40/60,m/o),气体利用率为20%。在系统操作作压力分别为0.1MPa、0.5MPa、0.9MPa下测取电池性能。表1为电池多次启动性能。图1为其在第2次启动时的电池性能,在0.9MPa下,200mA/cm2及300mA/cm2放电时,电池输出电压分别为0.853V和0.721V,最高功率密度为216.3mW/cm2The porous sintered Ni-Cr plate is selected as the anode, the γ-LiAlO 2 is used as the diaphragm and the above-mentioned cathode is assembled into a single cell. Under the battery operating temperature of 650°C, after leak detection and channeling detection with N 2 , the anode is supplied with H 2 -CO 2 mixed gas (H 2 /CO 2 =80/20, m/o), and the cathode is supplied with O 2 -CO 2 mixed gas (O 2 /CO 2 =40/60, m/o), the gas utilization rate is 20%. The battery performance was measured under the operating pressure of the system at 0.1MPa, 0.5MPa and 0.9MPa respectively. Table 1 shows the performance of multiple starts of the battery. Figure 1 shows the battery performance at the second startup. Under 0.9MPa, when discharged at 200mA/ cm2 and 300mA/ cm2 , the output voltage of the battery is 0.853V and 0.721V respectively, and the highest power density is 216.3mW/cm2 2 .

                表1 *.原料气利用率20%,其中第4、6、8次为空启动。Table 1 * . The raw material gas utilization rate is 20%, and the 4th, 6th, and 8th times are empty starts.

实施例2Example 2

按实施例1方法制备LiCo0.92Mg0.08O2粉料。称取14.2克LiCo0.92Mg0.08O2粉料、3.26克La2O3,8.2克功能性有机物及54.5克乙醇-正丁醇溶剂于1立升球磨罐中球磨,经过滤、脱气后,用带铸法制得电极,然后进行干燥,经厚度匹配后用热压机热压成电池用电极。表2为电池多次启动性能。图2为其在第9次启动时的电池性能在0.9MPa下,200mA/cm2及372mA/cm2放电时,电池输出电压分别为0.944V和0.781V,最高功率密度为291mW/cm2LiCo 0.92 Mg 0.08 O 2 powder was prepared according to the method in Example 1. Weigh 14.2 grams of LiCo 0.92 Mg 0.08 O 2 powder, 3.26 grams of La 2 O 3 , 8.2 grams of functional organic matter and 54.5 grams of ethanol-n-butanol solvent and ball mill in a 1 liter ball mill jar, after filtering and degassing, The electrode is prepared by the strip casting method, then dried, and after the thickness is matched, it is hot-pressed with a hot press to form an electrode for a battery. Table 2 shows the multiple starting performance of the battery. Figure 2 shows the battery performance at the ninth startup. Under 0.9MPa, when discharged at 200mA/cm 2 and 372mA/cm 2 , the output voltage of the battery is 0.944V and 0.781V respectively, and the highest power density is 291mW/cm 2 .

                   表2

Figure A0112020900101
*.原料气利用率20%,其中第2、3、5、7次为空启动。Table 2
Figure A0112020900101
* . The raw material gas utilization rate is 20%, and the 2nd, 3rd, 5th, and 7th times are empty starts.

实施例3Example 3

按实施例1方法制备LiCo0.92Mg0.08O2粉料。称取20.4克LiCo0.92Mg0.08O2粉料、5.3克Ce(NO3)3  6H2O,10.5克La(NO3)3  6H2O,12克功能性有机物及80克乙醇-正丁醇溶剂于1立升球磨罐中球磨,经过滤、脱气后,用带铸法制得电极,然后进行干燥,经厚度匹配后用热压机热压成电池用电极。LiCo 0.92 Mg 0.08 O 2 powder was prepared according to the method in Example 1. Weigh 20.4 grams of LiCo 0.92 Mg 0.08 O 2 powder, 5.3 grams of Ce(NO 3 ) 3 6H 2 O, 10.5 grams of La(NO 3 ) 3 6H 2 O, 12 grams of functional organic matter and 80 grams of ethanol-n-butanol The solvent is ball-milled in a 1-liter ball-milling tank, filtered and degassed, and the electrode is prepared by a tape casting method, then dried, and after thickness matching, is hot-pressed with a hot-press machine to form an electrode for a battery.

图3为电池性能,在0.9MPa下,200mA/cm2及300mA/cm2放电时,电池输出电压分别为0.838V和0.685V,最高功率密度为205.5mW/cm2。比较例1Figure 3 shows the performance of the battery. When discharged at 200mA/cm 2 and 300mA/cm 2 at 0.9MPa, the output voltage of the battery is 0.838V and 0.685V respectively, and the highest power density is 205.5mW/cm 2 . Comparative example 1

按USP 6063141所报导的用阳极氧化法制备LiCoO2,以CoO3及Li2CO3为原料制备LiCoO2,并以阳极氧化法制备出LiCoO2及锂化NiO双层阴极。其极化阻抗为0.2Ωcm2,150mA/cm2时过电位为30mV。LiCoO 2 was prepared by anodic oxidation as reported in USP 6063141, LiCoO 2 was prepared by using CoO 3 and Li 2 CO 3 as raw materials, and LiCoO 2 and lithiated NiO double-layer cathode was prepared by anodic oxidation. Its polarization impedance is 0.2Ωcm 2 , and its overpotential is 30mV at 150mA/cm 2 .

Claims (10)

1. LiCoO 2The type cathode material is characterized in that being represented by following structural formula:
LiCo 1-xM xO 2
Wherein, M be among alkali earth metal Be, Mg, Ca or the Sr one or more, x=0.05-0.10.
2. LiCoO according to claim 1 2The type cathode material is characterized in that M is the Mg element.
3. LiCoO according to claim 1 and 2 2The type cathode material is characterized in that LiCo 1-xM xO 2In can also doped with yttrium and/or rare earth element, its doping is counted LiCo by oxide weight 1-xM xO 210-40%.
4. LiCoO according to claim 3 2The type cathode material, it is characterized in that described rare earth element be among La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, the Dy one or more.
5. LiCoO according to claim 4 2The type cathode material is characterized in that described rare earth element is La and/or Ce.
6. LiCoO 2The preparation method of type cathode material is characterized in that by following step:
1). press LiCo 1-xM xO 2The mol ratio of Li, Co, M element takes by weighing the raw material that contains Li, Co, M in (x=0.05-0.10 in the formula, M are among Be, Mg, Ca or the Sr one or more) structural formula, and is mixed into batching;
2). prepare burden into the micro mist of particle diameter with the ball mill pulverizing less than 300 μ m;
3). the roasting micro mist obtained oxide more than 1 hour under 600-800 ℃ of high temperature.
7. preparation method according to claim 6 is characterized in that the raw material of Li, Co, M is respectively its nitrate, carbonate, acetate or oxide.
8. preparation method according to claim 6 is characterized in that in step 1) by LiCo 1-xM xO 2Amount doping Y and/or rare earth element are counted the 10-40% ratio with oxide weight and will be contained the raw material adding of Y and/or rare earth element and be mixed into batching.
9. preparation method according to claim 6 is characterized in that described Y and/or rare earth element are its nitrate, carbonate, acetate or oxide.
10. preparation method according to claim 6 is characterized in that after step 3) further by LiCo 1-xM xO 2Amount doping Y and/or rare earth element are counted the 10-40% ratio with oxide weight and will be contained the raw material adding of Y and/or rare earth element and be mixed into batching.
CNB011202092A 2001-07-06 2001-07-06 A kind of molten carbonate fuel cell cathode material and preparation method thereof Expired - Fee Related CN1165091C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB011202092A CN1165091C (en) 2001-07-06 2001-07-06 A kind of molten carbonate fuel cell cathode material and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB011202092A CN1165091C (en) 2001-07-06 2001-07-06 A kind of molten carbonate fuel cell cathode material and preparation method thereof

Publications (2)

Publication Number Publication Date
CN1395332A true CN1395332A (en) 2003-02-05
CN1165091C CN1165091C (en) 2004-09-01

Family

ID=4663981

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB011202092A Expired - Fee Related CN1165091C (en) 2001-07-06 2001-07-06 A kind of molten carbonate fuel cell cathode material and preparation method thereof

Country Status (1)

Country Link
CN (1) CN1165091C (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1316652C (en) * 2004-10-21 2007-05-16 北京化工大学 Cobalt acid lithium battery material adulterated alkaline-earth metal between layers and its preparing method
CN101740755B (en) * 2009-12-31 2012-10-31 江苏凯力克钴业股份有限公司 Production method of lithium cobalt oxide
CN104466099A (en) * 2014-12-02 2015-03-25 中南大学 High-voltage lithium cobaltate based composite cathode material of lithium ion battery and preparation method of high-voltage lithium cobaltate based composite cathode material
CN108539134A (en) * 2018-02-24 2018-09-14 西安中科爱姆特氢能源有限公司 A kind of super-low-temperature lithium-ion cell and preparation method thereof
CN112582598A (en) * 2020-11-23 2021-03-30 昆明理工大学 Short-range regeneration synergistic high-voltage modification method for waste lithium cobalt oxide positive electrode material

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1316652C (en) * 2004-10-21 2007-05-16 北京化工大学 Cobalt acid lithium battery material adulterated alkaline-earth metal between layers and its preparing method
CN101740755B (en) * 2009-12-31 2012-10-31 江苏凯力克钴业股份有限公司 Production method of lithium cobalt oxide
CN104466099A (en) * 2014-12-02 2015-03-25 中南大学 High-voltage lithium cobaltate based composite cathode material of lithium ion battery and preparation method of high-voltage lithium cobaltate based composite cathode material
CN108539134A (en) * 2018-02-24 2018-09-14 西安中科爱姆特氢能源有限公司 A kind of super-low-temperature lithium-ion cell and preparation method thereof
CN108539134B (en) * 2018-02-24 2021-02-05 白彬 Ultralow temperature lithium ion battery and preparation method thereof
CN112582598A (en) * 2020-11-23 2021-03-30 昆明理工大学 Short-range regeneration synergistic high-voltage modification method for waste lithium cobalt oxide positive electrode material

Also Published As

Publication number Publication date
CN1165091C (en) 2004-09-01

Similar Documents

Publication Publication Date Title
CN103811772B (en) Composite containing perovskite structure oxide and its production and use
CN102687324B (en) A kind of composite ceramic material and preparation method thereof
CN101295791B (en) A ternary composite cathode material for medium and low temperature solid oxide fuel cells
CN104916850B (en) Cathode of solid oxide fuel cell material and have its composite cathode material and preparation method thereof and battery composite cathode preparation method
CN102340008A (en) A kind of solid oxide fuel cell cathode material and preparation method thereof
CN108649235A (en) A kind of A laminated perovskite type electrode material and preparation method thereof
CN114628753B (en) Proton conductor solid oxide cell with negative electrode barrier layer
CN100583516C (en) A cathode material for A and B adulterated SrTiO3 solid oxide fuel battery
CN1046492C (en) Method for forming composite metal oxide and method for manufacturing electrode using same
JP2015088284A (en) Solid oxide fuel cell
CN109360991B (en) A low-temperature solid oxide fuel cell composite cathode and preparation method thereof
CN107994234B (en) Ceramic fuel cell and preparation method thereof
CN101123308A (en) A defect-doped anode material for solid oxide fuel cells
JP2003308846A (en) Perovskite oxide and air electrode for fuel cell
CN1165091C (en) A kind of molten carbonate fuel cell cathode material and preparation method thereof
CN1921196A (en) Multiple phase electrocatalysis material and method for making same
CN101299460A (en) Anode material lacking A bit for solid-oxide fuel battery
JP3729194B2 (en) Solid oxide fuel cell
CN114855203B (en) Application of perovskite LSCM materials in solid oxide electrolysis cells
CN102054992B (en) High conductivity double perovskite-type anode materials and preparation method thereof
KR101686298B1 (en) Method for manufacturing powder for cathode functional layer of solid oxide fuel cell
KR101691699B1 (en) Method for manufacturing powder for anode functional layer of solid oxide fuel cell
US20230197972A1 (en) Composite oxide powder
CN1172389C (en) A composite structure LiCoO2 type cathode for molten carbonate fuel cell and its preparation method
CN102544528A (en) Battery anode catalytic material containing magnesium and rare earth element, preparation method and application thereof

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
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
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee