CN105826527B - A kind of porous silicon-carbon composite and its preparation method and application - Google Patents
A kind of porous silicon-carbon composite and its preparation method and application Download PDFInfo
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- 239000002153 silicon-carbon composite material Substances 0.000 title claims abstract description 39
- 238000002360 preparation method Methods 0.000 title abstract description 9
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229910001416 lithium ion Inorganic materials 0.000 claims abstract description 28
- 238000000034 method Methods 0.000 claims abstract description 26
- 238000005554 pickling Methods 0.000 claims abstract description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 9
- 229910021338 magnesium silicide Inorganic materials 0.000 claims description 8
- YTHCQFKNFVSQBC-UHFFFAOYSA-N magnesium silicide Chemical compound [Mg]=[Si]=[Mg] YTHCQFKNFVSQBC-UHFFFAOYSA-N 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000005119 centrifugation Methods 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 238000001291 vacuum drying Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 11
- 229910021426 porous silicon Inorganic materials 0.000 abstract description 8
- HMDDXIMCDZRSNE-UHFFFAOYSA-N [C].[Si] Chemical compound [C].[Si] HMDDXIMCDZRSNE-UHFFFAOYSA-N 0.000 abstract description 7
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 abstract description 6
- 239000002131 composite material Substances 0.000 abstract description 6
- 229910052749 magnesium Inorganic materials 0.000 abstract description 5
- 239000011777 magnesium Substances 0.000 abstract description 5
- 238000009776 industrial production Methods 0.000 abstract description 4
- 229910052802 copper Inorganic materials 0.000 abstract 1
- 239000010949 copper Substances 0.000 abstract 1
- 239000000428 dust Substances 0.000 abstract 1
- 238000012805 post-processing Methods 0.000 abstract 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 48
- 229910052799 carbon Inorganic materials 0.000 description 32
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 21
- 229910052710 silicon Inorganic materials 0.000 description 21
- 239000010703 silicon Substances 0.000 description 21
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 12
- 229910052744 lithium Inorganic materials 0.000 description 12
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 10
- 239000007789 gas Substances 0.000 description 10
- 239000007773 negative electrode material Substances 0.000 description 9
- 239000001569 carbon dioxide Substances 0.000 description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 description 6
- 239000002041 carbon nanotube Substances 0.000 description 6
- 229910021393 carbon nanotube Inorganic materials 0.000 description 6
- 239000005543 nano-size silicon particle Substances 0.000 description 6
- 239000010405 anode material Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 229910021389 graphene Inorganic materials 0.000 description 5
- 229910002804 graphite Inorganic materials 0.000 description 5
- 239000010439 graphite Substances 0.000 description 5
- 239000011856 silicon-based particle Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 239000003575 carbonaceous material Substances 0.000 description 4
- 229940091250 magnesium supplement Drugs 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000012495 reaction gas Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000010306 acid treatment Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 238000003917 TEM image Methods 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 210000001787 dendrite Anatomy 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000009830 intercalation Methods 0.000 description 2
- 230000002687 intercalation Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- WCCJDBZJUYKDBF-UHFFFAOYSA-N copper silicon Chemical compound [Si].[Cu] WCCJDBZJUYKDBF-UHFFFAOYSA-N 0.000 description 1
- 238000009831 deintercalation Methods 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000006138 lithiation reaction Methods 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 229960000869 magnesium oxide Drugs 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000004611 spectroscopical analysis Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/386—Silicon or alloys based on silicon
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/362—Composites
- H01M4/364—Composites as mixtures
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
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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
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
技术领域technical field
本发明属于复合材料的制备领域,具体涉及一种多孔硅-碳复合材料及其制备方法和应用。The invention belongs to the field of preparation of composite materials, and in particular relates to a porous silicon-carbon composite material and its preparation method and application.
背景技术Background technique
锂离子电池是一种现代社会广泛使用的可充电电池。由于锂在各金属中具有极低的比重,又有最负的电极电位,所以,锂作为电池材料时,将具有高能量密度和高充电电压等显著的优势。但是,当锂在作为电池负极材料使用时,其在析出锂的过程中将产生枝晶偏析,形成树枝状的锂枝晶,这种锂枝晶逐渐长大将刺穿隔膜,连接正负极,使得电池短路,发生危险。所以,如今产业化的锂电池负极材料并非是金属锂,而是一种层状材料,锂离子可以在它们之间不断的嵌入与脱出,实现充电和放电,因此,锂电池全称为锂离子电池或者摇椅式电池。Lithium-ion battery is a rechargeable battery widely used in modern society. Since lithium has an extremely low specific gravity among all metals and has the most negative electrode potential, when lithium is used as a battery material, it will have significant advantages such as high energy density and high charging voltage. However, when lithium is used as a battery negative electrode material, it will produce dendrite segregation during the process of lithium precipitation, forming dendritic lithium dendrites, which will gradually grow to pierce the separator and connect the positive and negative electrodes. Make the battery short circuit, dangerous. Therefore, today's industrialized lithium battery anode material is not metallic lithium, but a layered material. Lithium ions can be continuously intercalated and extracted between them to realize charging and discharging. Therefore, lithium batteries are called lithium ion batteries in full. Or a rocking chair battery.
至今为止,能够实现产业化应用的锂离子电池负极材料主要是以石墨为代表的碳材料。石墨是一种层状材料,具有很好的导电性,可以很好的嵌入锂离子而几乎不发生体积的改变,所以,石墨在充放电循环时具有优异的稳定性。但是,石墨层与层之间能够容纳锂离子的空间是有限的,因而只有372mAh/g的最高理论比容量,这使得石墨为代表的碳材料越来越难以满足现代社会特别是电子产品和电动汽车行业对高比容量电池的需求。So far, the anode materials of lithium ion batteries that can realize industrial application are mainly carbon materials represented by graphite. Graphite is a layered material with good conductivity and can intercalate lithium ions very well without volume change. Therefore, graphite has excellent stability during charge-discharge cycles. However, the space between graphite layers that can accommodate lithium ions is limited, so there is only the highest theoretical specific capacity of 372mAh/g, which makes it increasingly difficult for carbon materials represented by graphite to meet the requirements of modern society, especially electronic products and electric vehicles. Demand for high specific capacity batteries in the automotive industry.
硅,是一种间接禁带的半导体材料,它可以和锂形成多种类型的合金,在作为锂离子电池负极材料使用时,它具有最高的理论比容量(4200mAh/g)和较低的电极电位,这使得硅成为高比容量和高充电电压锂电负极的热门候选材料。但是,硅在锂离子嵌入和脱出过程中,将发生高达300%的体积膨胀和收缩,在不断的这种剧烈的体积变化下,硅将逐渐破裂甚至粉碎,直到和电极完全脱离,失去电学活性。此外,硅的导电性并不好,其传输电荷的效率不高,这将降低整个电池的电传输效率。Silicon is a semiconductor material with an indirect band gap. It can form various types of alloys with lithium. When used as a negative electrode material for lithium-ion batteries, it has the highest theoretical specific capacity (4200mAh/g) and lower electrode Potential, which makes silicon a popular candidate material for lithium battery anodes with high specific capacity and high charging voltage. However, during the process of intercalation and extraction of lithium ions, silicon will undergo volume expansion and contraction of up to 300%. Under such continuous drastic volume changes, silicon will gradually break or even shatter, until it is completely separated from the electrode and loses electrical activity. . In addition, silicon is not very conductive, and it does not transport charge efficiently, which will reduce the electrical transport efficiency of the entire battery.
为了解决硅作为锂离子电池负极材料的这些问题,国内外的研究者们提出了许多方案。其中,硅-碳复合的方式受到了最多的关注,这是因为:首先,碳的导电性非常好,硅和碳复合后,将极大的提高这个体系的导电性。然后,碳的机械延展性很好,可以有效缓解硅的体积膨胀,提高体系的循环稳定性。In order to solve these problems of using silicon as the anode material of lithium-ion batteries, researchers at home and abroad have proposed many schemes. Among them, the way of silicon-carbon composite has received the most attention. This is because: First, the conductivity of carbon is very good. After silicon and carbon are composited, the conductivity of this system will be greatly improved. Then, the mechanical ductility of carbon is very good, which can effectively alleviate the volume expansion of silicon and improve the cycle stability of the system.
Shilong Jing等(Shilong Jin,Hao Jiang,Yanjie Hu,Jianhua Shen,andChunzhong Li.Face-to-Face Contact and Open-Void Coinvolved SiC NanohybridsLithium-Ion Battery Anodes with Extremely Long CycleLife.Adv.Funct.Mater.2015,25,5395-5401.)设计了一种石墨烯/碳纳米管三维气凝胶复合材料作为载体,然后将纳米的硅颗粒负载在气凝胶的网络中间的方案。这样的话,三维的碳材料网络将与硅颗粒保持优良的电接触,使得这个体系的导电性得到显著的提高。此外,硅颗粒膨胀之后依然与三维的碳材料网络保持电接触,保持了硅的活性。但是,石墨烯和碳纳米管以及纳米硅颗粒都价格昂贵且难以量产,因此,这种材料的设计难以产业化。Shilong Jing et al. (Shilong Jin, Hao Jiang, Yanjie Hu, Jianhua Shen, and Chunzhong Li. Face-to-Face Contact and Open-Void Coin Involved SiC Nanohybrids Lithium-Ion Battery Anodes with Extremely Long CycleLife. Adv. Funct. Mater. 2015, 25 , 5395-5401.) designed a graphene/carbon nanotube three-dimensional airgel composite as a carrier, and then loaded nano silicon particles in the middle of the airgel network. In this way, the three-dimensional carbon material network will maintain excellent electrical contact with the silicon particles, making the electrical conductivity of this system significantly improved. In addition, the silicon particles still maintain electrical contact with the three-dimensional carbon material network after swelling, maintaining the activity of silicon. However, graphene and carbon nanotubes and nano-silicon particles are expensive and difficult to mass-produce, so the design of this material is difficult to industrialize.
Qinbai Yun等(Qinbai Yun,Xianying Qin,Wei Lv,Yan-Bing He,Baohua Li,Feiyu Kang,Quan-Hong Yang.‘Concrete’inspired construction of a siliconcarbonhybrid electrode for high performance lithium ion battery.CARBON 93(2015)59-67.)设计了一种结构类似于水泥的电极,即将石墨烯、纳米硅颗粒、PAN先制成浆料涂敷在集流体上,然后高温将PAN裂解成碳,得到的负极结构为:硅纳米颗粒分散在石墨烯和裂解碳构成的三维网络之中,使得体系的导电性提高,硅的体积膨胀也得到有效缓解。但是,与上面方案的问题类似,石墨烯以及纳米硅颗粒价格昂贵,难以量产,因此,这种材料体系也就难以实现产业化。Qinbai Yun et al. (Qinbai Yun, Xianying Qin, Wei Lv, Yan-Bing He, Baohua Li, Feiyu Kang, Quan-Hong Yang.'Concrete'inspired construction of a silicon carbon hybrid electrode for high performance lithium ion battery. CARBON 93(2015) 59-67.) designed an electrode with a structure similar to cement, that is, graphene, nano-silicon particles, and PAN were first made into slurry and coated on the current collector, and then PAN was cracked into carbon at high temperature, and the obtained negative electrode structure was : Silicon nanoparticles are dispersed in the three-dimensional network composed of graphene and cracked carbon, which improves the conductivity of the system and effectively alleviates the volume expansion of silicon. However, similar to the problem of the above solution, graphene and nano-silicon particles are expensive and difficult to mass-produce. Therefore, it is difficult to achieve industrialization of this material system.
Wan-Jing Yu等(Wan-Jing Yu,Chang Liu,Peng-Xiang Hou,Lili Zhang,Xu-YiShan,Feng Li and Hui-Ming Cheng.Lithiation of Silicon Nanoparticles Confinedin Carbon Nanotubes.ACS NANO 2015,5063-5071.)通过CVD的办法在碳纳米管内部沉积硅颗粒,使得硅能够限制在碳管内部,这样,硅颗粒体积膨胀时碳纳米管也会随之膨胀,但不至于破裂,可以有效缓解硅的体积膨胀效应,因而具有较高的循环稳定性。但是,CVD的办法在纳米碳管内沉积硅颗粒对设备要求非常高,难以量产,造价高昂,难以走上产业化之路。Wan-Jing Yu et al. (Wan-Jing Yu, Chang Liu, Peng-Xiang Hou, Lili Zhang, Xu-YiShan, Feng Li and Hui-Ming Cheng. Lithiation of Silicon Nanoparticles Confinedin Carbon Nanotubes. ACS NANO 2015, 5063-5071. ) Deposit silicon particles inside the carbon nanotubes by CVD, so that the silicon can be confined inside the carbon tubes. In this way, when the volume of the silicon particles expands, the carbon nanotubes will also expand, but they will not break, which can effectively relieve the volume of silicon. Expansion effect, so it has high cycle stability. However, the method of CVD to deposit silicon particles in carbon nanotubes has very high requirements on equipment, it is difficult to mass produce, the cost is high, and it is difficult to embark on the road of industrialization.
发明内容Contents of the invention
本发明提供了一种多孔硅-碳复合材料的制备方法,工艺简单,易于重复,可实现大规模的工业化生产。制备得到的多孔硅-碳复合材料作为负极材料应用于锂离子电池中,将显著提高锂离子电池的循环稳定性。The invention provides a method for preparing a porous silicon-carbon composite material, the process is simple and easy to repeat, and large-scale industrial production can be realized. The prepared porous silicon-carbon composite material is used as an anode material in a lithium-ion battery, which will significantly improve the cycle stability of the lithium-ion battery.
一种制备多孔硅-碳复合材料的方法,具体包括以下步骤:A method for preparing a porous silicon-carbon composite material, specifically comprising the following steps:
将硅化镁粉末置于CO2/Ar混合气氛下,在700~900℃下进行热处理,再经酸洗及后处理得到所述的多孔硅-铜复合材料;The magnesium silicide powder is placed in a CO 2 /Ar mixed atmosphere, heat-treated at 700-900° C., and then pickled and post-treated to obtain the porous silicon-copper composite material;
所述的CO2/Ar混合气氛中,CO2的体积分数为10~90%。In the CO 2 /Ar mixed atmosphere, the volume fraction of CO 2 is 10-90%.
本发明中,使用硅化镁为原料,CO2/Ar混合气为反应气,成功合成出了多孔硅-碳复合材料。该发明利用了硅化镁受热分解为硅和镁,以及镁能够还原出二氧化碳中的碳的化学反应原理,其后酸洗得到的多孔硅-碳作为锂离子负极材料时,具有很高的比容量和优异的循环稳定性。该方法十分简单,操作过程简便,使用的仪器设备常见易得,采用的原料均为工业成品,容易实现大规模工业化生产。In the present invention, using magnesium silicide as raw material and CO 2 /Ar mixed gas as reaction gas, the porous silicon-carbon composite material is successfully synthesized. This invention utilizes the chemical reaction principle that magnesium silicide is thermally decomposed into silicon and magnesium, and magnesium can reduce carbon in carbon dioxide. The porous silicon-carbon obtained by pickling afterwards has a high specific capacity when used as a lithium ion negative electrode material and excellent cycle stability. The method is very simple, the operation process is simple and convenient, the instruments and equipment used are common and readily available, the raw materials used are all industrial products, and large-scale industrial production can be easily realized.
本发明中,利用了一种非常简单的工艺得到了多孔硅,多孔硅作为锂离子电池负极材料时,其表面积大,活性面积大,锂离子和电子的传输距离短,充放电效率将会大大提高。而且,多孔的结构有效的提供了硅向内膨胀的空间,这能很好的缓解硅在嵌锂时剧烈的向外的体积膨胀效应,实现高的循环稳定性和安全性。本发明在制备得到多孔硅的同时,将碳与多孔硅成功复合,得到多孔硅-碳的复合材料。在这复合材料中,碳覆盖在硅的表面,一方面极大的提高了体系的导电性,另一方面有效的缓解了硅向外的体积膨胀。In the present invention, a very simple process is used to obtain porous silicon. When porous silicon is used as a lithium-ion battery negative electrode material, its surface area is large, the active area is large, the transmission distance of lithium ions and electrons is short, and the charging and discharging efficiency will be greatly improved. improve. Moreover, the porous structure effectively provides space for silicon to expand inwardly, which can well alleviate the dramatic outward volume expansion effect of silicon during lithium intercalation, and achieve high cycle stability and safety. While preparing porous silicon, the invention successfully composites carbon and porous silicon to obtain a porous silicon-carbon composite material. In this composite material, carbon covers the surface of silicon, which greatly improves the conductivity of the system on the one hand, and effectively alleviates the outward volume expansion of silicon on the other hand.
作为优选,所述的CO2/Ar混合气氛中,CO2的体积分数为20~80%。进一步优选,CO2的体积分数为40~60%。经试验发现,此时,产物中碳含量最高。这可能是因为CO2是一种氧化性比较弱的气体,其与镁的氧化还原反应往往是在浓CO2甚至纯的CO2气氛下才能发生。但是,由于反应生成的C也具有还原性,虽然其还原性并没有金属镁强,但是,还是有可能与浓CO2反应,使得产物中碳的含量减少。当产物中碳含量越高时,碳对硅在脱嵌锂离子时体积变化的缓冲作用就越明显,对整个体系导电性的提高也越强,因此,其作为锂离子电池负极材料使用时,其循环性能也就更加稳定。Preferably, in the CO 2 /Ar mixed atmosphere, the volume fraction of CO 2 is 20-80%. More preferably, the volume fraction of CO 2 is 40-60%. It is found through experiments that at this time, the carbon content in the product is the highest. This may be because CO 2 is a relatively weak oxidizing gas, and its redox reaction with magnesium can only occur in a concentrated CO 2 or even pure CO 2 atmosphere. However, since the C produced by the reaction is also reducible, although its reducibility is not as strong as that of metal magnesium, it is still possible to react with concentrated CO 2 to reduce the carbon content in the product. When the carbon content in the product is higher, the buffering effect of carbon on the volume change of silicon when deintercalating lithium ions is more obvious, and the conductivity of the entire system is also improved. Therefore, when it is used as a negative electrode material for lithium-ion batteries, Its cycle performance is also more stable.
作为优选,所述的热处理时间为10~20h。Preferably, the heat treatment time is 10-20 hours.
作为优选,所述的酸洗采用浓度为0.5~5mol/L的盐酸,处理时间为2~10h。Preferably, the pickling uses hydrochloric acid with a concentration of 0.5-5 mol/L, and the treatment time is 2-10 hours.
作为优选,所述的后处理包括水洗、产物离心及真空干燥。Preferably, the post-treatment includes water washing, product centrifugation and vacuum drying.
本发明还公开了根据上述的方法制备的多孔硅-碳复合材料,及其在锂离子电池中的应用。经试验可知,以本发明制备的多孔硅-碳复合材料作为负极材料用于组装锂离子电池,可以显著提高锂离子电池的循环稳定性。The invention also discloses the porous silicon-carbon composite material prepared according to the above method, and its application in lithium ion batteries. It can be known from experiments that using the porous silicon-carbon composite material prepared by the present invention as a negative electrode material for assembling a lithium ion battery can significantly improve the cycle stability of the lithium ion battery.
与现有技术相比,本发明具有以下有益的技术效果:Compared with the prior art, the present invention has the following beneficial technical effects:
1)在锂电池负极材料的制备领域,首次提出使用二氧化碳作为碳源来制备硅-碳复合材料。相比较而言,工业上所包覆的碳常常是使用沥青等有机物在惰性气氛下高温裂解得到,在这些碳源裂解过程中,将释放大量的有毒有害的气体,而二氧化碳作为碳源不仅来源丰富,价格便宜,无任何环境污染,而且消耗了大量造成温室效应的气体-二氧化碳,是一种环境友好型碳源。1) In the field of preparation of anode materials for lithium batteries, it was proposed for the first time to use carbon dioxide as a carbon source to prepare silicon-carbon composite materials. In comparison, industrially coated carbon is often obtained by high-temperature cracking of organic matter such as pitch in an inert atmosphere. During the cracking process of these carbon sources, a large amount of toxic and harmful gases will be released, and carbon dioxide as a carbon source is not only a source Abundant, cheap, without any environmental pollution, and consumes a large amount of gas that causes the greenhouse effect-carbon dioxide, it is an environmentally friendly carbon source.
2)在制备多孔硅的同时,巧妙的利用了镁和二氧化碳的反应,从而将包碳的工艺步骤合并到多孔硅的制备过程中,一步法制备得到多孔硅-碳复合材料。现有技术中的包碳工艺需要先和液相或固相的有机物碳源球磨混合,然后干燥,再进行高温热处理,不仅工艺复杂,而且由于液相或固相的有机物和硅的接触往往不均匀,使得包上的碳也难以均匀,甚至出现很多地方包覆不上的情况。与其相比,以二氧化碳作为一种气态的碳源,即可以充分与硅接触,生成的碳也可以更加均匀地包覆在硅的表面,形成一层更加均匀,更加致密的碳膜。将其作为阴极材料应用于锂离子电池中,电池的循环稳定性会更加优异。2) While preparing porous silicon, the reaction of magnesium and carbon dioxide is cleverly used, so that the process steps of carbon coating are incorporated into the preparation process of porous silicon, and the porous silicon-carbon composite material is prepared in one step. The carbon encapsulation process in the prior art needs to be ball-milled and mixed with liquid or solid organic matter carbon sources first, then dried, and then subjected to high-temperature heat treatment. Uniformity makes it difficult for the carbon on the bag to be even, and even many places cannot be covered. In contrast, carbon dioxide as a gaseous carbon source can fully contact with silicon, and the generated carbon can also be more uniformly coated on the surface of silicon, forming a more uniform and denser carbon film. Applying it as a cathode material in a lithium-ion battery will improve the cycle stability of the battery.
3)本工艺简单,易于重复,且原料来源丰富、价格低廉,可实现大规模的工业化生产。3) The process is simple and easy to repeat, and the source of raw materials is abundant and cheap, and large-scale industrial production can be realized.
附图说明Description of drawings
图1为实施例1制备的多孔硅-碳复合材料的测试结果;图1a和图1b为其扫描电镜照片(SEM),图1c为其透射电镜照片(TEM),图1d为其x射线探针能谱(EDS)。Fig. 1 is the test result of the porous silicon-carbon composite material that embodiment 1 prepares; Fig. 1 a and Fig. 1 b are its scanning electron micrograph (SEM), Fig. 1 c is its transmission electron micrograph (TEM), Fig. 1 d is its x-ray probe Needle Energy Spectroscopy (EDS).
图2为分别以实施例1和对比例制备的多孔硅-碳复合材料为负极材料组装的锂离子电池的循环比容量曲线及库伦效率的对比图。其中,实心的是本实施例产物的数据点,空心得为对比例1产物的数据点。Fig. 2 is a comparison chart of the cycle specific capacity curve and Coulombic efficiency of the lithium-ion battery assembled with the porous silicon-carbon composite material prepared in Example 1 and Comparative Example respectively as the negative electrode material. Wherein, the solid ones are the data points of the product of this embodiment, and the hollow ones are the data points of the product of Comparative Example 1.
图3为分别以实施例3和对比例制备的多孔硅-碳复合材料为负极材料组装的锂离子电池的循环比容量曲线及库伦效率的对比图。其中,实心的是本实施例产物的数据点,空心得为对比例1产物的数据点。Fig. 3 is a comparison chart of cycle specific capacity curves and coulombic efficiency of lithium-ion batteries assembled with porous silicon-carbon composite materials prepared in Example 3 and Comparative Example respectively as negative electrode materials. Wherein, the solid ones are the data points of the product of this embodiment, and the hollow ones are the data points of the product of Comparative Example 1.
图4为分别以实施例5和对比例制备的多孔硅-碳复合材料为负极材料组装的锂离子电池的循环比容量曲线及库伦效率的对比图。其中,实心的是本实施例产物的数据点,空心得为对比例1产物的数据点。Fig. 4 is a comparison chart of cycle specific capacity curves and coulombic efficiency of lithium-ion batteries assembled with porous silicon-carbon composite materials prepared in Example 5 and Comparative Example respectively as negative electrode materials. Wherein, the solid ones are the data points of the product of this embodiment, and the hollow ones are the data points of the product of Comparative Example 1.
具体实施方式Detailed ways
下面通过具体实施例对本发明作进一步说明,但本发明的保护范围不局限于以下实施例。The present invention will be further described below through specific examples, but the protection scope of the present invention is not limited to the following examples.
实施例1Example 1
1)将硅化镁在700℃热处理20h,热处理过程通以过量的CO2体积分数为80%的CO2/Ar混合气作为反应气。1) Magnesium silicide is heat-treated at 700° C. for 20 hours, and an excess CO 2 /Ar mixed gas with a volume fraction of 80% of CO 2 is used as a reaction gas during the heat treatment.
2)将步骤1)所得产物在一定浓度的盐酸溶液中处理10h,其中盐酸浓度为0.5摩尔/升,酸处理后再使用去离子水清洗5遍,然后离心,最后进行真空干燥。2) The product obtained in step 1) was treated for 10 hours in a certain concentration of hydrochloric acid solution, wherein the concentration of hydrochloric acid was 0.5 mol/liter, after the acid treatment, it was washed 5 times with deionized water, then centrifuged, and finally vacuum-dried.
本实施例制备得到的多孔硅-碳复合材料的相关表征结果如图1所示。由图可见,本实施例产物为具有大量均匀分布的纳米级孔洞的多孔结构,其碳的质量分数约为40%,并以不定型碳膜的形式均匀包覆在硅的表面,形成具有核-壳结构特点的硅-碳复合材料。The relevant characterization results of the porous silicon-carbon composite material prepared in this example are shown in FIG. 1 . It can be seen from the figure that the product of this example is a porous structure with a large number of uniformly distributed nanoscale pores, the mass fraction of carbon is about 40%, and it is uniformly coated on the surface of silicon in the form of an amorphous carbon film, forming a porous structure with a core. -Silicon-carbon composite material with shell structure characteristics.
将本实施例制备得到的多孔硅-碳复合材料做成扣式电池进行性能测试,得到其循环容量曲线以及每轮循环的库伦效率。The porous silicon-carbon composite material prepared in this example was made into a button battery for performance testing, and its cycle capacity curve and Coulombic efficiency of each cycle were obtained.
就循环比容量和库伦效率与对比例制备的多孔硅-碳复合材料进行对比,结果如图2所示。由图可见,50个循环后本工艺制备的多孔硅-碳容量远高于对比材料,循环稳定性更加优异,其性能的优越性非常明显。The cycle specific capacity and coulombic efficiency were compared with the porous silicon-carbon composite material prepared in the comparative example, and the results are shown in Figure 2. It can be seen from the figure that after 50 cycles, the capacity of the porous silicon-carbon prepared by this process is much higher than that of the comparison material, the cycle stability is more excellent, and the superiority of its performance is very obvious.
实施例2Example 2
制备过程与实施例1完全相同,区别仅在于CO2/Ar混合气中,CO2体积分数为60%。制备得到的多孔硅-碳复合材料的形貌与实施例1类似,但碳的质量分数约为45%。The preparation process is exactly the same as that of Example 1, except that in the CO 2 /Ar gas mixture, the volume fraction of CO 2 is 60%. The morphology of the prepared porous silicon-carbon composite material is similar to that of Example 1, but the mass fraction of carbon is about 45%.
实施例3Example 3
1)将硅化镁在800℃热处理15h,热处理过程通以过量的CO2体积分数为50%的CO2/Ar混合气作为反应气。1) Magnesium silicide is heat-treated at 800° C. for 15 hours, and an excess CO 2 /Ar mixed gas with a volume fraction of 50% of CO 2 is used as a reaction gas during the heat treatment.
2)将步骤1)所得产物在一定浓度的盐酸溶液中处理5h,其中盐酸浓度为2.0摩尔/升,酸处理后再使用去离子水清洗7遍,然后离心,最后进行真空干燥。2) The product obtained in step 1) was treated for 5 hours in a certain concentration of hydrochloric acid solution, wherein the concentration of hydrochloric acid was 2.0 mol/liter, after the acid treatment, it was washed 7 times with deionized water, then centrifuged, and finally vacuum-dried.
本实施例制备制备得到的多孔硅-碳复合材料的形貌与实施例1类似,但碳的质量分数约为46%。The morphology of the porous silicon-carbon composite material prepared in this example is similar to that of Example 1, but the mass fraction of carbon is about 46%.
将本实施例制备得到的多孔硅-碳复合材料做成扣式电池进行性能测试,就循环比容量和库伦效率与对比例制备的多孔硅-碳复合材料进行对比,如图3所示。由图可见,50个循环后本工艺制备的多孔硅-碳容量远高于对比材料,循环稳定性更加优异,其性能的优越性非常明显。The porous silicon-carbon composite material prepared in this example was made into a button battery for performance testing, and the cycle specific capacity and coulombic efficiency were compared with the porous silicon-carbon composite material prepared in the comparative example, as shown in FIG. 3 . It can be seen from the figure that after 50 cycles, the capacity of the porous silicon-carbon prepared by this process is much higher than that of the comparison material, the cycle stability is more excellent, and the superiority of its performance is very obvious.
实施例4Example 4
制备过程与实施例1完全相同,区别仅在于CO2/Ar混合气中,CO2体积分数为40%。制备得到的多孔硅-碳复合材料的形貌与实施例1类似,但碳的质量分数约为46%。The preparation process is exactly the same as that of Example 1, except that in the CO 2 /Ar gas mixture, the volume fraction of CO 2 is 40%. The morphology of the prepared porous silicon-carbon composite material is similar to that of Example 1, but the mass fraction of carbon is about 46%.
实施例5Example 5
1)将硅化镁在900℃热处理10h,热处理过程通以过量的CO2体积分数为20%的CO2/Ar混合气作为反应气。1) Magnesium silicide is heat-treated at 900° C. for 10 h, and an excess CO 2 /Ar mixed gas with a volume fraction of 20% of CO 2 is used as a reaction gas during the heat treatment.
2)将步骤1)所得产物在一定浓度的盐酸溶液中处理2h,其中盐酸浓度为5摩尔/升,酸处理后再使用去离子水清洗8遍,然后离心,最后进行真空干燥。得到的多孔硅的相关测试结果如图1所示。2) The product obtained in step 1) was treated for 2 hours in a certain concentration of hydrochloric acid solution, wherein the concentration of hydrochloric acid was 5 mol/liter, after the acid treatment, it was washed 8 times with deionized water, then centrifuged, and finally vacuum-dried. The relevant test results of the obtained porous silicon are shown in FIG. 1 .
本实施例制备得到的多孔硅-碳复合材料的形貌与实施例1类似,但碳的质量分数约为41%。The morphology of the porous silicon-carbon composite material prepared in this example is similar to that of Example 1, but the mass fraction of carbon is about 41%.
将本实施例制备得到的多孔硅-碳复合材料做成扣式电池进行性能测试,就循环比容量和库伦效率与对比例制备的多孔硅-碳复合材料进行对比,如图4所示。由图可见,50个循环后本工艺制备的多孔硅-碳容量远高于对比材料,循环稳定性更加优异,其性能的优越性非常明显。The porous silicon-carbon composite material prepared in this example was made into a button battery for performance testing, and the cycle specific capacity and coulombic efficiency were compared with the porous silicon-carbon composite material prepared in the comparative example, as shown in FIG. 4 . It can be seen from the figure that after 50 cycles, the capacity of the porous silicon-carbon prepared by this process is much higher than that of the comparison material, the cycle stability is more excellent, and the superiority of its performance is very obvious.
对比例comparative example
采用公开号为CN103779544A的专利文献中的制备方法,具体为:Adopting the preparation method in the patent document whose publication number is CN103779544A, specifically:
首先,将质量比1:2的硅化镁和聚乙烯醇球磨混合。然后,先350℃热处理5h,再700℃热处理15h,热处理气氛为氩气和空气的混合气,氩气体积分数为90%。最后,将热处理产物在盐酸和氢氟酸的混酸溶液中处理5h,再离心,烘干得到以有机物为碳源(此处为聚乙烯醇)的多孔硅-碳颗粒。First, ball mill and mix magnesium silicide and polyvinyl alcohol with a mass ratio of 1:2. Then, heat treatment at 350° C. for 5 hours, and then heat treatment at 700° C. for 15 hours. The heat treatment atmosphere is a mixture of argon and air, and the fraction of argon gas is 90%. Finally, the heat-treated product was treated in a mixed acid solution of hydrochloric acid and hydrofluoric acid for 5 hours, then centrifuged, and dried to obtain porous silicon-carbon particles with organic matter as the carbon source (here, polyvinyl alcohol).
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