CN101847711A - Porous carbon coated ferrous silicate lithium anode material and preparation method thereof - Google Patents
Porous carbon coated ferrous silicate lithium anode material and preparation method thereof Download PDFInfo
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- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 27
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 title claims abstract description 26
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- 239000010405 anode material Substances 0.000 title claims 3
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000011148 porous material Substances 0.000 claims abstract description 21
- 239000002202 Polyethylene glycol Substances 0.000 claims abstract description 16
- 229920001223 polyethylene glycol Polymers 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 12
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 18
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 13
- MCDLETWIOVSGJT-UHFFFAOYSA-N acetic acid;iron Chemical compound [Fe].CC(O)=O.CC(O)=O MCDLETWIOVSGJT-UHFFFAOYSA-N 0.000 claims description 12
- 239000000843 powder Substances 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 12
- 239000002994 raw material Substances 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 11
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 9
- 239000003054 catalyst Substances 0.000 claims description 9
- 239000011668 ascorbic acid Substances 0.000 claims description 8
- 229960005070 ascorbic acid Drugs 0.000 claims description 8
- 235000010323 ascorbic acid Nutrition 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 7
- 239000003963 antioxidant agent Substances 0.000 claims description 4
- 235000006708 antioxidants Nutrition 0.000 claims description 4
- 230000003078 antioxidant effect Effects 0.000 claims description 3
- 239000012298 atmosphere Substances 0.000 claims description 3
- 239000000654 additive Substances 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- 229910003002 lithium salt Inorganic materials 0.000 claims description 2
- 159000000002 lithium salts Chemical class 0.000 claims description 2
- IAQLJCYTGRMXMA-UHFFFAOYSA-M lithium;acetate;dihydrate Chemical compound [Li+].O.O.CC([O-])=O IAQLJCYTGRMXMA-UHFFFAOYSA-M 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims 2
- 235000012239 silicon dioxide Nutrition 0.000 claims 2
- 229910052786 argon Inorganic materials 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 238000010792 warming Methods 0.000 claims 1
- 238000005303 weighing Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 19
- 238000006243 chemical reaction Methods 0.000 abstract description 12
- 230000008569 process Effects 0.000 abstract description 10
- 238000001354 calcination Methods 0.000 abstract description 9
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 abstract description 8
- 229910001416 lithium ion Inorganic materials 0.000 abstract description 8
- 239000007774 positive electrode material Substances 0.000 abstract description 8
- 239000013078 crystal Substances 0.000 abstract description 7
- 239000002243 precursor Substances 0.000 abstract description 7
- 239000002245 particle Substances 0.000 abstract description 6
- 150000002500 ions Chemical class 0.000 abstract description 5
- 230000002776 aggregation Effects 0.000 abstract description 4
- 238000004220 aggregation Methods 0.000 abstract description 4
- 238000009833 condensation Methods 0.000 abstract description 4
- 230000005494 condensation Effects 0.000 abstract description 4
- 239000003792 electrolyte Substances 0.000 abstract description 4
- 230000007062 hydrolysis Effects 0.000 abstract description 4
- 238000006460 hydrolysis reaction Methods 0.000 abstract description 4
- 230000005012 migration Effects 0.000 abstract description 4
- 238000013508 migration Methods 0.000 abstract description 4
- 230000035515 penetration Effects 0.000 abstract description 4
- 238000009831 deintercalation Methods 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract description 3
- 230000035484 reaction time Effects 0.000 abstract description 3
- 230000004913 activation Effects 0.000 abstract description 2
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000000197 pyrolysis Methods 0.000 abstract description 2
- 150000002009 diols Chemical class 0.000 abstract 1
- 230000008521 reorganization Effects 0.000 abstract 1
- XIXADJRWDQXREU-UHFFFAOYSA-M lithium acetate Chemical compound [Li+].CC([O-])=O XIXADJRWDQXREU-UHFFFAOYSA-M 0.000 description 11
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 6
- 239000010406 cathode material Substances 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 239000011259 mixed solution Substances 0.000 description 5
- 239000012299 nitrogen atmosphere Substances 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 4
- 235000011114 ammonium hydroxide Nutrition 0.000 description 4
- 238000011161 development Methods 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000002441 X-ray diffraction Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910000519 Ferrosilicon Inorganic materials 0.000 description 2
- 239000012300 argon atmosphere Substances 0.000 description 2
- 229940075614 colloidal silicon dioxide Drugs 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 229960002089 ferrous chloride Drugs 0.000 description 2
- 229940062993 ferrous oxalate Drugs 0.000 description 2
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 2
- OWZIYWAUNZMLRT-UHFFFAOYSA-L iron(2+);oxalate Chemical compound [Fe+2].[O-]C(=O)C([O-])=O OWZIYWAUNZMLRT-UHFFFAOYSA-L 0.000 description 2
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910018119 Li 3 PO 4 Inorganic materials 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000840 electrochemical analysis Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 229960002413 ferric citrate Drugs 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- -1 iron (III) ions Chemical class 0.000 description 1
- NPFOYSMITVOQOS-UHFFFAOYSA-K iron(III) citrate Chemical compound [Fe+3].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NPFOYSMITVOQOS-UHFFFAOYSA-K 0.000 description 1
- 229940006116 lithium hydroxide Drugs 0.000 description 1
- PAZHGORSDKKUPI-UHFFFAOYSA-N lithium metasilicate Chemical compound [Li+].[Li+].[O-][Si]([O-])=O PAZHGORSDKKUPI-UHFFFAOYSA-N 0.000 description 1
- 229910052912 lithium silicate Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000003446 memory effect Effects 0.000 description 1
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- 238000012986 modification Methods 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 238000010532 solid phase synthesis reaction Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
本发明涉及多孔碳包覆硅酸亚铁锂正极材料及制备方法,采用聚乙二醇为造孔剂,通过正硅酸乙酯的水解缩合形成凝胶,在前驱体煅烧过程中由于聚乙二醇热解形成连续的骨架和贯通的大孔/介孔孔道,大孔平均孔径介于0.5~3.9μm,介孔平均孔径介于18~40nm,平均孔隙率介于57.2~71.9%。通过正硅酸乙酯的水解缩合形成三维网络结构,从而降低了离子在晶格重组时迁移的距离和迁移所必需的活化能,有利于降低反应温度和缩短反应时间,生成物相纯度高、符合化学计量比的产物。多孔结构增加了材料的比表面积,不仅有利于电解液在颗粒中的渗透,提高了晶体内部锂离子的脱嵌概率,提高了锂离子利用率,还避免了晶粒在煅烧过程中的长大与充放电过程中的聚集,提高正极材料的电化学性能。
The invention relates to a porous carbon-coated lithium ferrous silicate positive electrode material and a preparation method. Polyethylene glycol is used as a pore-forming agent to form a gel through hydrolysis and condensation of ethyl orthosilicate. During the calcination process of the precursor, due to polyethylene glycol Diol pyrolysis forms a continuous skeleton and through macropores/mesoporous channels. The average pore diameter of macropores is 0.5-3.9 μm, the average pore diameter of mesopores is 18-40 nm, and the average porosity is 57.2-71.9%. The three-dimensional network structure is formed through the hydrolysis and condensation of ethyl orthosilicate, which reduces the migration distance and activation energy necessary for the migration of ions during lattice reorganization, which is beneficial to reduce the reaction temperature and shorten the reaction time. A product that conforms to the stoichiometric ratio. The porous structure increases the specific surface area of the material, which is not only conducive to the penetration of the electrolyte in the particles, but also improves the probability of lithium ion deintercalation inside the crystal, improves the utilization rate of lithium ions, and avoids the growth of the crystal grains during the calcination process. The aggregation during charging and discharging improves the electrochemical performance of the positive electrode material.
Description
技术领域technical field
本发明涉及一种多孔碳包覆硅酸亚铁锂正极材料及制备方法,属于能源材料制备技术领域。The invention relates to a porous carbon-coated lithium ferrous silicate positive electrode material and a preparation method, belonging to the technical field of energy material preparation.
背景技术Background technique
人类对能源的需求飞速增长,能源成为世界各国经济发展遇到的重要问题,并由此引发能源危机和环境污染等亟待解决的问题。在能源开发中,充分利用自然力如风能、潮汐能、太阳能等具有重要意义,由于这些能源作用的不连续,要大规模利用这些自然能,需要有与之配套的能量储存器。锂离子电池是一种新型的二次电池,由于其电压高、容量高、体积小、重量轻、循环寿命长、安全性能好、无记忆效应等优点而成为世界各国争相发展的对象。Li2FeSiO4具有比容量较高(理论容量为166mAh/g)、安全性好、无毒、价格低廉、资源丰富等优点,被认为是铁基正极材料中极具发展潜力的锂离子电池正极材料。With the rapid growth of human demand for energy, energy has become an important problem encountered in the economic development of countries all over the world, which has led to urgent problems such as energy crisis and environmental pollution. In energy development, it is of great significance to make full use of natural forces such as wind energy, tidal energy, and solar energy. Due to the discontinuity of these energy sources, to use these natural energies on a large scale requires a matching energy storage device. Lithium-ion battery is a new type of secondary battery. Due to its advantages such as high voltage, high capacity, small size, light weight, long cycle life, good safety performance, and no memory effect, it has become the object of development all over the world. Li 2 FeSiO 4 has the advantages of high specific capacity (theoretical capacity is 166mAh/g), good safety, non-toxicity, low price, abundant resources, etc. Material.
正硅酸盐Li2FeSiO4具有与低温Li3PO4相似的结构,属于正交晶系,空间群为Pmn21,其中氧原子以正四面体紧密堆积方式排列,Fe与Si各自处于氧原子四面体中心位置。目前报道的Li2FeSiO4制备方法主要有:(1)高温固相法:A.Nyten等人以硅酸锂、草酸亚铁和正硅酸乙酯为原料,与C凝胶充分研磨混合后,在CO/CO2气流(50∶50)加热至750℃并保温24h合成Li2FeSiO4。电化学测试结果表明:在60℃,C/16倍率,2.0~3.7V电压范围条件下,放电容量稳定在130mAh/g左右,呈现出了良好的充放电可逆性,循环10次后容量保持率为84%。中国专利CN101582495A采用微波合成法制备锂离子电池正极材料Li2FeSiO4,得到了Li2FeSiO4/C复合正极材料,在10mA/g和30mA/g下放电比容量分别为119.6mAh/g和103.7mAh/g。日本专利JP2001266882(A)采用FeO和Li2SiO3为原料,球磨4h后,800℃下煅烧4h,得到目标产物Li2FeSiO4。但是该法由于原料只是机械混合,需要高温下长时间的煅烧,导致产物粒度较粗,粒径分布范围广,且杂相较多,电化学活性不足。(2)水热合成法:R.Dominko等人以氢氧化锂,胶态二氧化硅和四水合氯化亚铁为原料,将氢氧化锂和胶态二氧化硅均匀分散于氯化亚铁溶液中,然后转移至不锈钢制的密闭高压釜中,在N2气氛下于150℃恒温反应14d,然后将得到的绿色粉末在氩气气氛下用蒸馏水反复洗涤,再于50℃下干燥1d得到Li2FeSiO4粉体。室温下C/30倍率,2.0~4.2V电压范围条件充放电,可逆容量约为91mAh/g。该法制得的产物电化学性能较差,反应时间较长,且不利于离子掺杂改性。(3)溶胶凝胶法:R.Dominko等人提出以摩尔比率为1∶1的柠檬酸铁和硝酸铁的混合物、醋酸锂和胶态SiO2为原料,将醋酸锂和铁(III)离子混合物分别溶解于水后,将三者混合搅拌1h,保存使其形成溶胶。将得到的溶胶在60℃干燥24h以上。经过研磨后将得到的粉末于700℃的惰性气氛下反应1h后冷却至室温得到Li2FeSiO4。在60℃,C/2倍率的条件下循环10次后可逆容量保持率为75%。杨勇等人申请的相关专利提出:将醋酸锂,草酸亚铁和正硅酸乙酯加入到150ml乙醇中,在80℃油浴条件下反应20h,转移到蒸发皿中100℃烘干。将得到的混合物转移到玛瑙球磨罐中,加入蔗糖,以丙酮为分散剂,球磨5h。待丙酮挥发后,转移到瓷舟中于管式电阻炉中在N2保护下,650℃热处理10h,自然冷却至室温,即得到Li2FeSiO4复合材料。此外,中国专利CN101499527A以沉淀法首先制备出硅铁共混物,经洗涤后烘干,然后与锂源化合物,有机碳源混合球磨,干燥后得Li2FeSiO4的前驱体材料,然后在保护气氛下低温焙烧得Li2FeSiO4正极材料。该法在洗涤过程中不可避免地将硅铁共混物中的可溶性离子洗去,造成化学计量比的失配,从而影响产物的电化学性能。Orthosilicate Li 2 FeSiO 4 has a structure similar to that of low-temperature Li 3 PO 4 , belongs to the orthorhombic crystal system, and the space group is Pmn2 1 , in which the oxygen atoms are arranged in a regular tetrahedral close-packed manner, and Fe and Si are each in the oxygen atom The center position of the tetrahedron. The currently reported Li 2 FeSiO 4 preparation methods mainly include: (1) High-temperature solid-phase method: A. Nyten et al. used lithium silicate, ferrous oxalate and ethyl orthosilicate as raw materials, and after fully grinding and mixing with C gel, Li 2 FeSiO 4 was synthesized by heating to 750°C in CO/CO 2 airflow (50:50) and keeping it warm for 24h. Electrochemical test results show that: at 60°C, C/16 rate, 2.0-3.7V voltage range, the discharge capacity is stable at about 130mAh/g, showing good charge-discharge reversibility, and the capacity retention rate after 10 cycles was 84%. Chinese patent CN101582495A uses a microwave synthesis method to prepare lithium ion battery cathode material Li 2 FeSiO 4 , and obtains a Li 2 FeSiO 4 /C composite cathode material, and the discharge specific capacities at 10mA/g and 30mA/g are 119.6mAh/g and 103.7 mAh/g. Japanese patent JP2001266882 (A) uses FeO and Li 2 SiO 3 as raw materials, ball mills for 4 hours, and then calcines at 800° C. for 4 hours to obtain the target product Li 2 FeSiO 4 . However, because the raw materials are only mechanically mixed in this method, long-term calcination at high temperature is required, resulting in coarser particle size of the product, wide particle size distribution range, more impurity phases, and insufficient electrochemical activity. (2) Hydrothermal synthesis method: R.Dominko et al use lithium hydroxide, colloidal silicon dioxide and ferrous chloride tetrahydrate as raw materials, and uniformly disperse lithium hydroxide and colloidal silicon dioxide in ferrous chloride solution, then transferred to a closed stainless steel autoclave, and reacted at a constant temperature of 150°C under N2 atmosphere for 14d, and then the obtained green powder was repeatedly washed with distilled water under an argon atmosphere, and then dried at 50°C for 1d to obtain Li 2 FeSiO 4 powder. C/30 rate at room temperature, charge and discharge in the voltage range of 2.0-4.2V, the reversible capacity is about 91mAh/g. The electrochemical performance of the product prepared by this method is poor, the reaction time is long, and it is not conducive to ion doping modification. (3) Sol-gel method: R.Dominko et al. proposed to use a mixture of ferric citrate and ferric nitrate, lithium acetate and colloidal SiO with a molar ratio of 1: 1 as raw materials to combine lithium acetate and iron (III) ions After the mixture was dissolved in water respectively, the three were mixed and stirred for 1 h, and preserved to form a sol. The obtained sol was dried at 60 °C for more than 24 h. After grinding, react the obtained powder under an inert atmosphere at 700° C. for 1 h and then cool to room temperature to obtain Li 2 FeSiO 4 . The reversible capacity retention rate is 75% after 10 cycles at 60°C and C/2 rate. The relevant patent applied by Yang Yong et al. proposes: add lithium acetate, ferrous oxalate and ethyl orthosilicate to 150ml of ethanol, react in an oil bath at 80°C for 20h, transfer to an evaporating dish and dry at 100°C. The obtained mixture was transferred to an agate ball mill jar, sucrose was added, acetone was used as a dispersant, and ball milled for 5 hours. After the acetone is volatilized, it is transferred to a porcelain boat and placed in a tubular resistance furnace under the protection of N 2 , heat-treated at 650°C for 10 hours, and cooled naturally to room temperature to obtain a Li 2 FeSiO 4 composite material. In addition, the Chinese patent CN101499527A firstly prepared the ferrosilicon blend by precipitation method, washed and dried, then mixed with lithium source compound and organic carbon source for ball milling, and dried to obtain the precursor material of Li 2 FeSiO 4 , and then protected The Li 2 FeSiO 4 cathode material is obtained by calcining at low temperature under the atmosphere. In this method, the soluble ions in the ferrosilicon blend are inevitably washed away during the washing process, resulting in a mismatch of the stoichiometric ratio, thereby affecting the electrochemical performance of the product.
制约硅酸亚铁锂作正极材料发展的主要原因在于硅酸亚铁锂材料本身较低的电子电导率和较小的锂离子扩散系数,严重影响了材料充放电电流密度以及比容量,限制了硅酸亚铁锂的实际应用。目前改善硅酸亚铁锂电导率方法包括:掺杂、表面碳包覆和细化晶粒尺寸等,这些方法都能在一定程度上改善硅酸亚铁锂的电化学性能。此外,如果将硅酸亚铁锂做成多孔材料,多孔结构增加了材料的比表面积,不仅有利于电解液在颗粒中的渗透,增大了固液接触界面面积,提高了晶体内部锂离子的脱嵌概率,还避免了晶粒在煅烧过程中的长大与充放电过程中的聚集,从而明显提高正极材料的电化学性能。The main reason restricting the development of lithium ferrous silicate as positive electrode material is the low electronic conductivity and small lithium ion diffusion coefficient of lithium ferrous silicate material itself, which seriously affects the charge and discharge current density and specific capacity of the material, limiting the Practical application of lithium ferrous silicate. The current methods for improving the conductivity of lithium ferrous silicate include: doping, surface carbon coating, and grain size refinement, etc., all of which can improve the electrochemical performance of lithium ferrous silicate to a certain extent. In addition, if lithium ferrous silicate is made into a porous material, the porous structure increases the specific surface area of the material, which not only facilitates the penetration of the electrolyte in the particles, but also increases the solid-liquid contact interface area and improves the lithium ion density inside the crystal. The probability of deintercalation also avoids the growth of crystal grains during the calcination process and the aggregation during the charge and discharge process, thereby significantly improving the electrochemical performance of the positive electrode material.
发明内容Contents of the invention
本发明采用聚乙二醇作为造孔剂,通过正硅酸乙酯的水解缩合形成凝胶,在前驱体煅烧过程中由于聚乙二醇热解形成连续的骨架和贯通的大孔/介孔孔道,大孔平均孔径介于0.5~3.9μm,介孔平均孔径介于18~40nm,平均孔隙率介于57.2~71.9%。The present invention uses polyethylene glycol as a pore-forming agent to form a gel through the hydrolysis and condensation of tetraethyl orthosilicate, and forms continuous skeletons and through macropores/mesopores due to the pyrolysis of polyethylene glycol during the calcination process of the precursor In the pores, the average pore diameter of macropores is between 0.5-3.9 μm, the average pore diameter of mesopores is between 18-40 nm, and the average porosity is between 57.2-71.9%.
本发明的目的在于提供一种多孔Li2FeSiO4/C正极材料制备方法,依该方法制备的多孔碳包覆硅酸亚铁锂粉体,晶粒具有连续的骨架和贯通的大孔/介孔孔道。这种结构提高了材料的孔隙率,增加了材料的比表面积,不仅有利于电解液在颗粒中的渗透,还避免了晶粒在煅烧过程中的长大与充放电过程中的聚集,从而提高正极材料的电化学性能。The object of the present invention is to provide a method for preparing a porous Li 2 FeSiO 4 /C positive electrode material. The porous carbon-coated lithium ferrous silicate powder prepared according to the method has a continuous skeleton and through macropores/intermediates. Hole channel. This structure improves the porosity of the material and increases the specific surface area of the material, which not only facilitates the penetration of the electrolyte in the particles, but also avoids the growth of the grains during the calcination process and the aggregation during the charging and discharging process, thereby improving Electrochemical properties of cathode materials.
本发明是通过以下技术方案加以实现的:The present invention is achieved through the following technical solutions:
本发明的多孔碳包覆硅酸亚铁锂正极材料,形成连续的骨架和贯通的大孔/介孔孔道,大孔平均孔径介于0.5~3.9μm,介孔平均孔径介于18~40nm,平均孔隙率介于57.2~71.9%,合成过程中煅烧温度较低,600℃下即可,产物化学计量比准确。The porous carbon-coated lithium ferrous silicate positive electrode material of the present invention forms a continuous skeleton and through macropores/mesoporous channels, the average pore diameter of the macropores is between 0.5 and 3.9 μm, and the average pore diameter of the mesopores is between 18 and 40 nm. The average porosity is between 57.2% and 71.9%. The calcination temperature in the synthesis process is relatively low, 600° C., and the stoichiometric ratio of the product is accurate.
本发明的多孔碳包覆硅酸亚铁锂正极材料的制备方法,步骤如下:The preparation method of porous carbon-coated lithium ferrous silicate cathode material of the present invention, the steps are as follows:
1)以二水醋酸锂、醋酸亚铁、正硅酸乙酯为原料,按物质量比称取相应物质,使Li∶Fe∶Si物质量比为2∶1∶1;以乙醇为溶剂,正硅酸乙酯的浓度为0.5~0.8mol/L;添加剂聚乙二醇造孔剂,醋酸或氨水催化剂,抗坏血酸为抗氧化剂,其中聚乙二醇占理论合成硅酸亚铁锂质量的10%~30%,抗氧化剂占理论合成硅酸亚铁锂质量的3%,催化剂配成0.1~0.3mol/L的水溶液;将锂盐、正硅酸乙酯和聚乙二醇溶于乙醇中,搅拌混合均匀,再向混合液加入醋酸亚铁和抗坏血酸,搅拌溶解,加入催化剂调节溶液体系pH在2~7之间;1) Lithium acetate dihydrate, ferrous acetate, and ethyl orthosilicate are used as raw materials, and the corresponding substances are weighed according to the mass ratio of the substances, so that the mass ratio of Li:Fe:Si is 2:1:1; with ethanol as the solvent, The concentration of ethyl orthosilicate is 0.5-0.8mol/L; the additive polyethylene glycol pore-forming agent, acetic acid or ammonia water catalyst, and ascorbic acid are antioxidants, in which polyethylene glycol accounts for 10% of the mass of theoretically synthesized lithium ferrous silicate. % to 30%, the antioxidant accounts for 3% of the mass of theoretically synthesized lithium ferrous silicate, and the catalyst is made into an aqueous solution of 0.1 to 0.3 mol/L; lithium salt, tetraethyl orthosilicate and polyethylene glycol are dissolved in ethanol , stir and mix evenly, then add ferrous acetate and ascorbic acid to the mixed solution, stir to dissolve, add a catalyst to adjust the pH of the solution system between 2 and 7;
2)将步骤1)的混合液转移至反应釜,将反应釜放入恒温箱中在120~180℃下反应12~20h,得到的凝胶混合物于干燥箱中在60~100℃烘干后得到干凝胶;2) Transfer the mixed liquid in step 1) to the reaction kettle, put the reaction kettle into a constant temperature box and react at 120~180°C for 12~20h, and dry the obtained gel mixture in a drying oven at 60~100°C get xerogel;
3)将步骤2)的干凝胶研细后转移至程序控温的管式炉中,在氩气气氛下以10℃·min-1的速度升温至600~750℃并恒温7~10h,随炉冷却至室温,得到多孔Li2FeSiO4/C粉体。3) Grinding the xerogel in step 2) and transferring it to a temperature-programmed tube furnace, raising the temperature to 600-750°C at a rate of 10°C·min -1 under an argon atmosphere and keeping the temperature constant for 7-10 hours, Cool down to room temperature with the furnace to obtain porous Li 2 FeSiO 4 /C powder.
本发明的优点在于通过正硅酸乙酯的水解缩合形成三维网络结构,将反应物中的各种离子固定在网络结构中,达到了分子水平的混合,从而降低了离子在晶格重组时迁移的距离和迁移所必需的活化能,有利于降低反应温度和缩短反应时间,生成物相纯度高、符合化学计量比的产物。另外,以聚乙二醇作为造孔剂,形成的晶粒具有连续的骨架和贯通的大孔/介孔孔道,并且可以通过调节反应物浓度、pH和聚乙二醇的加入量控制孔的分布和大小,这种多孔结构增加了材料的比表面积,不仅有利于电解液在颗粒中的渗透,增大了固液接触界面面积,提高了晶体内部锂离子的脱嵌概率,提高了锂离子利用率,有利于改善材料的比容量,还避免了晶粒在煅烧过程中的长大与充放电过程中的聚集,从而提高正极材料的电化学性能。The advantage of the present invention is that a three-dimensional network structure is formed through the hydrolysis and condensation of tetraethyl orthosilicate, various ions in the reactants are fixed in the network structure, and the mixing at the molecular level is achieved, thereby reducing the migration of ions during lattice recombination The distance and the activation energy necessary for migration are beneficial to reduce the reaction temperature and shorten the reaction time, and produce products with high phase purity and stoichiometric ratio. In addition, using polyethylene glycol as a pore-forming agent, the formed grains have a continuous skeleton and through macropores/mesoporous channels, and the pores can be controlled by adjusting the concentration of reactants, pH and the amount of polyethylene glycol added. Distribution and size, this porous structure increases the specific surface area of the material, which not only facilitates the penetration of the electrolyte in the particles, but also increases the area of the solid-liquid contact interface, improves the probability of deintercalation of lithium ions inside the crystal, and improves the lithium ion density. The utilization rate is conducive to improving the specific capacity of the material, and also avoids the growth of crystal grains during the calcination process and the aggregation during the charging and discharging process, thereby improving the electrochemical performance of the positive electrode material.
附图说明Description of drawings
图1实施例一合成的Li2FeSiO4/C的XRD图谱;The XRD pattern of Li 2 FeSiO 4 /C synthesized in Fig. 1 embodiment one;
图2实施例一合成的Li2FeSiO4/C的SEM图;The SEM figure of Li 2 FeSiO 4 /C synthesized in Fig. 2 embodiment one;
图3实施例一合成的Li2FeSiO4/C的充放电曲线;Figure 3 is the charge-discharge curve of Li 2 FeSiO 4 /C synthesized in Example 1;
图4实施例一合成的Li2FeSiO4/C的循环性能曲线。Fig. 4 is the cycle performance curve of Li 2 FeSiO 4 /C synthesized in Example 1.
具体实施方式Detailed ways
实施例1:Example 1:
以醋酸锂、醋酸亚铁、正硅酸乙酯为原料,按物质的量比称取相应物质,使Li∶Fe∶Si物质量比为2∶1∶1,精确称取1.640g醋酸锂,1.8ml正硅酸乙酯和0.399g聚乙二醇,将上述物质溶解于13.3ml乙醇,使得正硅酸乙酯的浓度为0.6mol/L。所得溶液体系充分搅拌10min混合均匀。精确称取1.391g醋酸亚铁,精确称取0.039g抗坏血酸,将其加入到上述溶液中,搅拌溶解,以0.3mol/L的氨水作为催化剂调节pH值至7。将混合液转移至反应釜,将反应釜置于恒温箱中在120℃下反应20h,得到的凝胶混合物于真空干燥箱中在60℃烘干后得到干凝胶。Lithium acetate, ferrous acetate, and ethyl orthosilicate are used as raw materials, and the corresponding substances are weighed according to the ratio of substances, so that the mass ratio of Li:Fe:Si is 2:1:1, and 1.640g of lithium acetate is accurately weighed, 1.8ml of tetraethyl orthosilicate and 0.399g of polyethylene glycol were dissolved in 13.3ml of ethanol so that the concentration of tetraethyl orthosilicate was 0.6mol/L. The obtained solution system was fully stirred for 10 min and mixed evenly. Accurately weigh 1.391g ferrous acetate, accurately weigh 0.039g ascorbic acid, add it to the above solution, stir to dissolve, and adjust the pH value to 7 with 0.3mol/L ammonia water as a catalyst. The mixed solution was transferred to a reaction kettle, and the reaction kettle was placed in a constant temperature oven to react at 120°C for 20 hours, and the obtained gel mixture was dried in a vacuum oven at 60°C to obtain a xerogel.
在N2气氛保护下,将上述硅酸亚铁锂前驱体在600℃下煅烧10h,获得碳包覆的多孔硅酸亚铁锂粉体。大孔平均孔径约3.9μm,且分布较宽,介孔平均孔径为30nm,平均孔隙率为71.9%。Li2FeSiO4/C的XRD图谱如图1所示,图中XRD的特征峰与标准Li2FeSiO4粉体的XRD图谱衍射峰对应,表明合成的粉体为Li2FeSiO4。Li2FeSiO4的SEM如图2所示,产物具有连续的骨架和贯通多孔孔道,大孔平均孔径约3.9μm。在60℃下,C/10倍率下的充放电曲线如图3所示,所合成的Li2FeSiO4/C正极材料首次充放电容量为分别为142.2mAh/g和138.7mAh/g。循环性能曲线如图4所示,Li2FeSiO4/C循环20次后容量保持在128.3mAh/g,衰减较小。Under the protection of N2 atmosphere, the above lithium ferrous silicate precursor was calcined at 600 °C for 10 h to obtain carbon-coated porous lithium ferrous silicate powder. The average pore diameter of the macropores is about 3.9 μm, and the distribution is wide, the average pore diameter of the mesopores is 30 nm, and the average porosity is 71.9%. The XRD pattern of Li 2 FeSiO 4 /C is shown in Figure 1. The characteristic peaks of the XRD in the figure correspond to the diffraction peaks of the XRD pattern of the standard Li 2 FeSiO 4 powder, indicating that the synthesized powder is Li 2 FeSiO 4 . The SEM of Li 2 FeSiO 4 is shown in Figure 2. The product has a continuous skeleton and through porous channels, and the average pore size of the macropores is about 3.9 μm. The charge-discharge curves at C/10 rate at 60°C are shown in Figure 3. The initial charge-discharge capacities of the synthesized Li 2 FeSiO 4 /C cathode materials are 142.2mAh/g and 138.7mAh/g, respectively. The cycle performance curve is shown in Fig. 4. After 20 cycles of Li 2 FeSiO 4 /C, the capacity remains at 128.3mAh/g, and the attenuation is small.
实施例2:Example 2:
以醋酸锂、醋酸亚铁、正硅酸乙酯为原料,按物质的量比称取相应物质,使Li∶Fe∶Si物质量比为2∶1∶1,精确称取1.640g醋酸锂,1.8ml正硅酸乙酯和0.129g聚乙二醇,将上述物质溶解于10.0ml乙醇,使得正硅酸乙酯的浓度为0.8mol/L。所得溶液体系充分搅拌10min混合均匀。精确称取1.391g醋酸亚铁,精确称取0.039g抗坏血酸,将其加入到上述溶液中,搅拌溶解,以0.2mol/L的氨水作为催化剂调节pH值至6。将混合液转移至反应釜,将反应釜置于恒温箱中在140℃下反应17h,得到的凝胶混合物于真空干燥箱中在70℃烘干后得到干凝胶。Lithium acetate, ferrous acetate, and ethyl orthosilicate are used as raw materials, and the corresponding substances are weighed according to the ratio of substances, so that the mass ratio of Li:Fe:Si is 2:1:1, and 1.640g of lithium acetate is accurately weighed, 1.8ml of tetraethyl orthosilicate and 0.129g of polyethylene glycol were dissolved in 10.0ml of ethanol so that the concentration of tetraethyl orthosilicate was 0.8mol/L. The obtained solution system was fully stirred for 10 min and mixed evenly. Accurately weigh 1.391g of ferrous acetate and 0.039g of ascorbic acid, add them to the above solution, stir and dissolve, and adjust the pH value to 6 with 0.2mol/L ammonia water as a catalyst. The mixed solution was transferred to a reaction kettle, and the reaction kettle was placed in a constant temperature oven at 140° C. for 17 hours. The obtained gel mixture was dried in a vacuum oven at 70° C. to obtain a xerogel.
在N2气氛保护下,将上述硅酸亚铁锂前驱体在650℃下煅烧9h,获得碳包覆的多孔硅酸亚铁锂粉体。大孔平均孔径约0.5μm,且分布较窄,介孔平均孔径为40nm,平均孔隙率为57.2%。Under the protection of N2 atmosphere, the above lithium ferrous silicate precursor was calcined at 650°C for 9h to obtain carbon-coated porous lithium ferrous silicate powder. The average pore diameter of the macropores is about 0.5 μm, and the distribution is narrow, the average pore diameter of the mesopores is 40 nm, and the average porosity is 57.2%.
实施例3:Example 3:
以醋酸锂、醋酸亚铁、正硅酸乙酯为原料,按物质的量比称取相应物质,使Li∶Fe∶Si物质量比为2∶1∶1,精确称取1.640g醋酸锂,1.8ml正硅酸乙酯和0.399g聚乙二醇,将上述物质溶解于16.0ml乙醇,使得正硅酸乙酯的浓度为0.53mol/L。所得溶液体系充分搅拌10min混合均匀。精确称取1.391g醋酸亚铁,精确称取0.039g抗坏血酸,将其加入到上述溶液中,搅拌溶解,以0.3mol/L的氨水作为催化剂调节pH值至4。将混合液转移至反应釜,将反应釜置于恒温箱中在160℃下反应15h,得到的凝胶混合物于真空干燥箱中在80℃烘干后得到干凝胶。Lithium acetate, ferrous acetate, and ethyl orthosilicate are used as raw materials, and the corresponding substances are weighed according to the ratio of substances, so that the mass ratio of Li:Fe:Si is 2:1:1, and 1.640g of lithium acetate is accurately weighed, 1.8ml of tetraethyl orthosilicate and 0.399g of polyethylene glycol were dissolved in 16.0ml of ethanol so that the concentration of tetraethyl orthosilicate was 0.53mol/L. The obtained solution system was fully stirred for 10 min and mixed evenly. Accurately weigh 1.391g of ferrous acetate, accurately weigh 0.039g of ascorbic acid, add it to the above solution, stir and dissolve, and adjust the pH value to 4 with 0.3mol/L ammonia water as a catalyst. The mixed solution was transferred to a reaction kettle, and the reaction kettle was placed in a constant temperature oven at 160° C. for 15 hours. The obtained gel mixture was dried in a vacuum oven at 80° C. to obtain a xerogel.
在N2气氛保护下,将上述硅酸亚铁锂前驱体在700℃下煅烧8h,获得碳包覆的多孔硅酸亚铁锂粉体。大孔平均孔径约3.4μm,介孔平均孔径为33nm,平均孔隙率为68.5%。Under the protection of N2 atmosphere, the above lithium ferrous silicate precursor was calcined at 700°C for 8h to obtain carbon-coated porous lithium ferrous silicate powder. The average pore diameter of macropores is about 3.4 μm, the average pore diameter of mesopores is 33 nm, and the average porosity is 68.5%.
实施例4:Example 4:
以醋酸锂、醋酸亚铁、正硅酸乙酯为原料,按物质的量比称取相应物质,使Li∶Fe∶Si物质量比为2∶1∶1,精确称取1.640g醋酸锂,1.8ml正硅酸乙酯和0.258g聚乙二醇,将上述物质溶解于11.4ml乙醇,使得正硅酸乙酯的浓度为0.53mol/L。所得溶液体系充分搅拌10min混合均匀。精确称取1.391g醋酸亚铁,精确称取0.039g抗坏血酸,将其加入到上述溶液中,搅拌溶解,以0.1mol/L的醋酸作为催化剂调节pH值至2。将混合液转移至反应釜,将反应釜置于恒温箱中在180℃下反应12h,得到的凝胶混合物于真空干燥箱中在100℃烘干后得到干凝胶。Lithium acetate, ferrous acetate, and ethyl orthosilicate are used as raw materials, and the corresponding substances are weighed according to the ratio of substances, so that the mass ratio of Li:Fe:Si is 2:1:1, and 1.640g of lithium acetate is accurately weighed, 1.8ml of tetraethyl orthosilicate and 0.258g of polyethylene glycol were dissolved in 11.4ml of ethanol so that the concentration of tetraethyl orthosilicate was 0.53mol/L. The obtained solution system was fully stirred for 10 min and mixed evenly. Accurately weigh 1.391g of ferrous acetate, accurately weigh 0.039g of ascorbic acid, add it to the above solution, stir and dissolve, and adjust the pH value to 2 with 0.1mol/L acetic acid as a catalyst. The mixed solution was transferred to a reaction kettle, and the reaction kettle was placed in a constant temperature box to react at 180°C for 12 hours, and the obtained gel mixture was dried in a vacuum oven at 100°C to obtain a xerogel.
在N2气氛保护下,将上述硅酸亚铁锂前驱体在750℃下煅烧7h,获得碳包覆的多孔硅酸亚铁锂粉体。大孔平均孔径约2.0μm,介孔平均孔径为18nm,平均孔隙率为63.4%。Under the protection of N2 atmosphere, the above lithium ferrous silicate precursor was calcined at 750°C for 7h to obtain carbon-coated porous lithium ferrous silicate powder. The average pore diameter of macropores is about 2.0 μm, the average pore diameter of mesopores is 18 nm, and the average porosity is 63.4%.
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CN102315438A (en) * | 2011-05-23 | 2012-01-11 | 江苏正彤电子科技有限公司 | A porous C/Li2MSiO4/C (M=Fe, mn, co) composite anode material and its preparation method |
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WO2017140645A1 (en) | 2016-02-17 | 2017-08-24 | Wacker Chemie Ag | Method for producing si/c composite particles |
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CN108467047A (en) * | 2018-05-08 | 2018-08-31 | 方嘉城 | A kind of preparation method of ferric metasilicate lithium |
CN108910901A (en) * | 2018-09-06 | 2018-11-30 | 宁夏大学 | A kind of preparation method of high-purity ferric metasilicate lithium |
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WO2021238083A1 (en) * | 2020-05-27 | 2021-12-02 | 常州大学 | Method for preparing silicate/carbon composite by using attapulgite, and application of material |
US11623210B2 (en) | 2020-05-27 | 2023-04-11 | Changzhou University | Method for preparing silicate/carbon composite from attapulgite, and use of silicate/carbon composite |
CN113830774A (en) * | 2021-10-18 | 2021-12-24 | 浙江长兴中俄新能源材料技术研究院有限公司 | Method for preparing carbon composite lithium ferrous silicate by ilmenite based on sol-gel method |
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