CN105161724B - Porous carbon sphere for lithium-sulfur battery and preparation method and application of porous carbon sphere - Google Patents
Porous carbon sphere for lithium-sulfur battery and preparation method and application of porous carbon sphere Download PDFInfo
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 135
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 91
- JDZCKJOXGCMJGS-UHFFFAOYSA-N [Li].[S] Chemical compound [Li].[S] JDZCKJOXGCMJGS-UHFFFAOYSA-N 0.000 title claims abstract description 85
- 238000002360 preparation method Methods 0.000 title claims abstract description 37
- 239000002245 particle Substances 0.000 claims abstract description 65
- 229910002804 graphite Inorganic materials 0.000 claims abstract description 43
- 239000010439 graphite Substances 0.000 claims abstract description 43
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000007774 positive electrode material Substances 0.000 claims abstract description 10
- 238000004804 winding Methods 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims description 37
- 238000004518 low pressure chemical vapour deposition Methods 0.000 claims description 19
- 229920003257 polycarbosilane Polymers 0.000 claims description 17
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 14
- 229910052710 silicon Inorganic materials 0.000 claims description 14
- 239000010703 silicon Substances 0.000 claims description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- 238000000151 deposition Methods 0.000 claims description 6
- 230000008021 deposition Effects 0.000 claims description 6
- 239000011261 inert gas Substances 0.000 claims description 5
- 238000002309 gasification Methods 0.000 claims description 3
- 229910052717 sulfur Inorganic materials 0.000 abstract description 14
- 239000011593 sulfur Substances 0.000 abstract description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 13
- 238000000034 method Methods 0.000 description 13
- 238000004458 analytical method Methods 0.000 description 12
- 229910010271 silicon carbide Inorganic materials 0.000 description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 8
- 238000010586 diagram Methods 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 230000005540 biological transmission Effects 0.000 description 5
- 239000002131 composite material Substances 0.000 description 5
- 238000001000 micrograph Methods 0.000 description 5
- 229920001021 polysulfide Polymers 0.000 description 5
- 239000005077 polysulfide Substances 0.000 description 5
- 150000008117 polysulfides Polymers 0.000 description 5
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Inorganic materials [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 5
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 4
- 229910002091 carbon monoxide Inorganic materials 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- 239000002803 fossil fuel Substances 0.000 description 4
- 229910001416 lithium ion Inorganic materials 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 238000001228 spectrum Methods 0.000 description 4
- 229910018540 Si C Inorganic materials 0.000 description 3
- 229910018557 Si O Inorganic materials 0.000 description 3
- 239000010406 cathode material Substances 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 229910018091 Li 2 S Inorganic materials 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- 239000003575 carbonaceous material Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 229910052987 metal hydride Inorganic materials 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- -1 nickel metal hydride Chemical class 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910012851 LiCoO 2 Inorganic materials 0.000 description 1
- 229910010707 LiFePO 4 Inorganic materials 0.000 description 1
- 229910014689 LiMnO Inorganic materials 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005234 chemical deposition Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 229910021389 graphene Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000003446 memory effect Effects 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 230000007847 structural defect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910000314 transition metal oxide Inorganic materials 0.000 description 1
- 238000005019 vapor deposition process Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 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
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
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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
- H01M10/36—Accumulators not provided for in groups H01M10/05-H01M10/34
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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
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/133—Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
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- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
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- 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
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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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
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Abstract
本发明公开了一种锂硫电池用多孔碳球及其制备方法和应用,该锂硫电池用多孔碳球是由带状石墨无序缠绕而成。制备方法包括以下步骤:(1)制备Si‑C‑O颗粒;(2)制备多孔碳球。该锂硫电池用多孔碳球适合制备锂硫电池正极材料,且能提高锂硫电池容量和循环稳定性及硫电极的导电性。制备方法简单、产率较高且可批量生产。
The invention discloses a porous carbon sphere for a lithium-sulfur battery, a preparation method and an application thereof. The porous carbon sphere for a lithium-sulfur battery is formed by disorderly winding ribbon graphite. The preparation method comprises the following steps: (1) preparing Si-C-O particles; (2) preparing porous carbon spheres. The porous carbon sphere for the lithium-sulfur battery is suitable for preparing the positive electrode material of the lithium-sulfur battery, and can improve the capacity and cycle stability of the lithium-sulfur battery and the conductivity of the sulfur electrode. The preparation method is simple, the yield is high and it can be produced in batches.
Description
技术领域technical field
本发明属于二次动力锂电池领域,特别涉及一种锂硫电池用正极材料及其制备方法和应用。The invention belongs to the field of secondary power lithium batteries, and in particular relates to a positive electrode material for a lithium-sulfur battery and a preparation method and application thereof.
背景技术Background technique
社会的发展对石油、天然气等化石燃料的需求日益扩大,然而随着化石燃料消耗量的增大,这些不可再生化石燃料的耗竭趋势日益受到广泛的关注,同时化石燃料在燃烧过程中所导致的空气污染和温室效应也正成为全球性问题。为了解决以燃油为动力的交通运输工具所产生的能源短缺和环境污染问题,动力电池逐渐成为人们关注的热点。动力电池包括燃料电池、铅酸电池、镍氢电池和锂离子电池等。燃料电池需要使用稀缺的贵金属铂作为催化剂和价格高昂的质子交换膜,同时燃料氢的制取和储运困难。铅酸电池质量比能量和比功率较低,循环寿命较短,同时铅酸电池的制造污染性较大。镍氢电池虽然已实现商品化,但是其充放电效率低、循环寿命差、比能量低等缺点。相比之下锂离子电池具有能量密度高(是铅酸电池和镍氢电池的2~3倍),循环寿命长,能量密度高,自放电小,无记忆效应、工作温度范围宽等特点,是目前综合性能最好的一种电池。因此,锂离子电池也被认为是在未来较长时期内最好的动力电池解决方案之一。The development of society has an increasing demand for fossil fuels such as oil and natural gas. However, with the increase in the consumption of fossil fuels, the depletion trend of these non-renewable fossil fuels has attracted more and more attention. At the same time, the burning of fossil fuels caused Air pollution and the greenhouse effect are also becoming global problems. In order to solve the energy shortage and environmental pollution problems caused by fuel-powered vehicles, power batteries have gradually become a focus of attention. Power batteries include fuel cells, lead-acid batteries, nickel metal hydride batteries and lithium-ion batteries. Fuel cells need to use the scarce precious metal platinum as a catalyst and expensive proton exchange membranes, and at the same time, it is difficult to prepare, store and transport fuel hydrogen. The mass specific energy and specific power of lead-acid batteries are lower, and the cycle life is shorter. At the same time, the manufacture of lead-acid batteries is more polluting. Although nickel-hydrogen batteries have been commercialized, they have disadvantages such as low charge and discharge efficiency, poor cycle life, and low specific energy. In contrast, lithium-ion batteries have the characteristics of high energy density (2 to 3 times that of lead-acid batteries and nickel-metal hydride batteries), long cycle life, high energy density, small self-discharge, no memory effect, and wide operating temperature range. It is the battery with the best comprehensive performance at present. Therefore, lithium-ion batteries are also considered to be one of the best power battery solutions for a long time to come.
目前商品化的锂离子电池的正极材料主要是过渡金属氧化物如LiCoO2、LiMnO2、LiFePO4等,其比容量难以满足动力电池的需求。单质硫因为理论比容量(1672 mAh/g)和比能量高(2600 Wh/kg),同时还具有低成本、低毒性、环境友好等优点,是一种具有很高开发价值和应用前景的二次动力锂电池正极材料。但是,单质硫作为正极材料也存在着一些问题,一方面单质硫所固有的电子绝缘性使其表现为电化学钝性;另一方面硫电极的放电中间产物多硫化物具有较高的溶解性,易造成活性物质的损失,并且破坏电池体系的循环稳定性。At present, the positive electrode materials of commercial lithium-ion batteries are mainly transition metal oxides such as LiCoO 2 , LiMnO 2 , LiFePO 4 , etc., whose specific capacity cannot meet the needs of power batteries. Elemental sulfur has the advantages of low cost, low toxicity, and environmental friendliness because of its theoretical specific capacity (1672 mAh/g) and high specific energy (2600 Wh/kg). Secondary power lithium battery cathode material. However, elemental sulfur also has some problems as a positive electrode material. On the one hand, the inherent electronic insulation of elemental sulfur makes it electrochemically inactive; on the other hand, the discharge intermediate product of sulfur electrode, polysulfide, has high solubility , it is easy to cause the loss of active materials and destroy the cycle stability of the battery system.
为了改善单质硫在电池中的电化学性能,目前大多数研究者尝试将硫与具有高表面积和高导电性的多孔碳材料作为硫的载体与单质硫复合,从而增加正极材料的导电性、提供电化学反应活性点和抑制放电产物 Li2Sx(x>2)的溶解扩散。这样不但可以提高阴极的电子离子传递能力,并且使还原过程产生的中间体多聚硫化物能保持在阴极中,避免其溶于有机电解液中,从而提高锂硫电池的容量保持率。目前常用的多孔碳材料多为碳纳米管、石墨烯等,这些纳米材料与硫复合后制成电池后,在电极循环充放电过程中容易发生破坏,因此循环稳定性较差。In order to improve the electrochemical performance of elemental sulfur in the battery, most researchers currently try to compound sulfur with porous carbon materials with high surface area and high conductivity as the carrier of sulfur and elemental sulfur, thereby increasing the conductivity of the positive electrode material, providing Electrochemical reaction active sites and inhibit the dissolution and diffusion of discharge products Li 2 Sx (x>2). This can not only improve the electron ion transfer ability of the cathode, but also keep the intermediate polysulfide produced in the reduction process in the cathode, avoiding its dissolution in the organic electrolyte, thereby improving the capacity retention rate of the lithium-sulfur battery. At present, the commonly used porous carbon materials are mostly carbon nanotubes, graphene, etc. After these nanomaterials are compounded with sulfur to make batteries, they are prone to damage during the electrode cycle charge and discharge process, so the cycle stability is poor.
发明内容Contents of the invention
本发明要解决的技术问题是克服现有技术的不足,提供一种适合制备锂硫电池正极材料、能提高锂硫电池容量和循环稳定性、提高硫电极导电性的锂硫电池用多孔碳球,还提供一种方法简单、产率较高、可批量生产的锂硫电池用多孔碳球的制备方法,还相应提供该多孔碳球在制备锂硫电池中的应用。The technical problem to be solved in the present invention is to overcome the deficiencies of the prior art, and provide a porous carbon sphere for lithium-sulfur batteries suitable for preparing lithium-sulfur battery cathode materials, which can improve the capacity and cycle stability of lithium-sulfur batteries, and improve the conductivity of sulfur electrodes. , also provides a method for preparing porous carbon spheres for lithium-sulfur batteries with simple method, high yield and mass production, and correspondingly provides the application of the porous carbon spheres in the preparation of lithium-sulfur batteries.
为解决上述技术问题,本发明采用以下技术方案:In order to solve the problems of the technologies described above, the present invention adopts the following technical solutions:
一种锂硫电池用多孔碳球,所述多孔碳球是由带状石墨无序缠绕而成。A porous carbon sphere for a lithium-sulfur battery, wherein the porous carbon sphere is formed by disorderly winding ribbon graphite.
上述的锂硫电池用多孔碳球中,优选的,所述带状石墨由多层石墨片组成,所述多层石墨片的片层数为10~20层。In the aforementioned porous carbon spheres for lithium-sulfur batteries, preferably, the ribbon-shaped graphite is composed of multilayer graphite sheets, and the number of layers of the multilayer graphite sheets is 10 to 20 layers.
作为一个总的技术构思,本发明还提供一种锂硫电池用多孔碳球的制备方法,包括以下步骤:As a general technical concept, the present invention also provides a preparation method of porous carbon spheres for lithium-sulfur batteries, comprising the following steps:
(1)制备Si-C-O颗粒:将低分子聚碳硅烷加热气化,然后在惰性气体保护下采用低压化学气相沉积制备Si-C-O颗粒;(1) Preparation of Si-C-O particles: heat and vaporize low-molecular polycarbosilane, and then prepare Si-C-O particles by low-pressure chemical vapor deposition under the protection of inert gas;
(2)制备多孔碳球:将步骤(1)所得Si-C-O颗粒在惰性气体保护下进行高温热处理,以去除所述Si-C-O颗粒中的氧元素和硅元素,得到锂硫电池用多孔碳球。(2) Preparation of porous carbon spheres: the Si-C-O particles obtained in step (1) are subjected to high-temperature heat treatment under the protection of an inert gas to remove the oxygen and silicon elements in the Si-C-O particles to obtain porous carbon for lithium-sulfur batteries ball.
上述的制备方法中,优选的,所述步骤(1)中,所述低分子聚碳硅烷中硅元素和碳元素的原子比为1∶2,所述低分子聚碳硅烷的数均分子量为500~2000。In the above preparation method, preferably, in the step (1), the atomic ratio of silicon and carbon in the low-molecular polycarbosilane is 1:2, and the number-average molecular weight of the low-molecular polycarbosilane is 500-2000.
上述的制备方法中,优选的,所述步骤(2)中,所述高温热处理的温度为2600℃~2700℃,保温时间为1h~3h。In the above preparation method, preferably, in the step (2), the temperature of the high-temperature heat treatment is 2600°C-2700°C, and the holding time is 1h-3h.
上述的制备方法中,优选的,所述步骤(1)中,所述低压化学气相沉积的温度为1000℃~1200℃,沉积时间为0.5h~3h,所述低压化学气相沉积的压力不高于1000 Pa。In the above preparation method, preferably, in the step (1), the temperature of the low-pressure chemical vapor deposition is 1000°C-1200°C, the deposition time is 0.5h-3h, and the pressure of the low-pressure chemical vapor deposition is not high at 1000 Pa.
上述的制备方法中,优选的,所述步骤(1)中,所述低分子聚碳硅烷加热气化的温度为120℃~180℃。In the above preparation method, preferably, in the step (1), the heating and gasification temperature of the low-molecular polycarbosilane is 120°C-180°C.
作为一个总的技术构思,本发明还提供一种上述的锂硫电池用多孔碳球或者上述制备方法制得的锂硫电池用多孔碳球在锂硫电池中的应用。As a general technical idea, the present invention also provides an application of the above-mentioned porous carbon spheres for lithium-sulfur batteries or the porous carbon spheres for lithium-sulfur batteries prepared by the above preparation method in lithium-sulfur batteries.
上述的应用中,优选的,所述应用包括将所述锂硫电池用多孔碳球与硫粉混合,制备锂硫电池的正极材料。In the above application, preferably, the application includes mixing the porous carbon spheres for the lithium-sulfur battery with sulfur powder to prepare a positive electrode material for the lithium-sulfur battery.
上述的应用中,优选的,所述锂硫电池用多孔碳球与所述硫粉的质量比为3∶2。In the above application, preferably, the mass ratio of the porous carbon spheres for the lithium-sulfur battery to the sulfur powder is 3:2.
本发明制备方法的步骤(1)中,惰性气体可优选氮气,步骤(2)中,高温热处理的保护介质可优选氩气。In step (1) of the preparation method of the present invention, the inert gas may preferably be nitrogen, and in step (2), the protective medium for high-temperature heat treatment may preferably be argon.
与现有技术相比,本发明的优点在于:Compared with the prior art, the present invention has the advantages of:
(1)本发明的锂硫电池用多孔碳球,其结构上为由10~20层石墨片组成的石墨带无序缠绕而成的多孔结构,由于石墨带所含石墨片的片层数较高,稳定性较高,因而应用于电池时,在电池的充放电过程中能够较长时间的保持完整,因此循环稳定性较高。(1) The porous carbon spheres for lithium-sulfur batteries of the present invention are structurally a porous structure in which graphite ribbons composed of 10 to 20 layers of graphite flakes are wound in disorder. High, high stability, so when it is applied to the battery, it can maintain integrity for a long time during the charging and discharging process of the battery, so the cycle stability is high.
(2)本发明的锂硫电池用多孔碳球的制备方法,设备投入小,操作简单,制备成本低,产率高,容易实现批量生产。(2) The preparation method of the porous carbon spheres for lithium-sulfur batteries of the present invention has the advantages of small investment in equipment, simple operation, low preparation cost, high yield, and easy realization of mass production.
(3)本发明的锂硫电池用多孔碳球的制备方法,由于多孔碳球的制备温度较高,结构上的缺陷较少,后续制备的锂硫电池性能更优异。(3) In the method for preparing porous carbon spheres for lithium-sulfur batteries of the present invention, since the porous carbon spheres are prepared at a higher temperature and have fewer structural defects, the subsequently prepared lithium-sulfur batteries have better performance.
附图说明Description of drawings
图1为本发明低压化学气相沉积制备Si-C-O颗粒的原理示意图。Fig. 1 is a schematic diagram of the principle of preparing Si-C-O particles by low-pressure chemical vapor deposition of the present invention.
图2为本发明实施例1步骤(1)所制备的Si-C-O颗粒的SEM微观形貌图。Fig. 2 is a SEM microscopic image of Si-C-O particles prepared in step (1) of Example 1 of the present invention.
图3为本发明实施例1步骤(1)所制备的Si-C-O颗粒的XRD物相分析图。Fig. 3 is an XRD phase analysis diagram of Si-C-O particles prepared in step (1) of Example 1 of the present invention.
图4为本发明实施例1步骤(2)所制备的锂硫电池用多孔碳球的SEM微观形貌图。Fig. 4 is a SEM microscopic image of the porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 1 of the present invention.
图5为本发明实施例1步骤(2)所制备的锂硫电池用多孔碳球的XRD物相分析图。Fig. 5 is an XRD phase analysis diagram of the porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 1 of the present invention.
图6为本发明实施例2步骤(1)所制备的Si-C-O颗粒的SEM微观形貌图。Fig. 6 is a SEM microscopic image of Si-C-O particles prepared in step (1) of Example 2 of the present invention.
图7为本发明实施例2步骤(1)所制备的Si-C-O颗粒的XRD物相分析图。Fig. 7 is an XRD phase analysis diagram of Si-C-O particles prepared in step (1) of Example 2 of the present invention.
图8为本发明实施例2步骤(2)所制备的锂硫电池用多孔碳球的SEM微观形貌图。Fig. 8 is a SEM microscopic image of the porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 2 of the present invention.
图9为本发明实施例2步骤(2)所制备的锂硫电池用多孔碳球的XRD物相分析图。Fig. 9 is an XRD phase analysis chart of the porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 2 of the present invention.
图10为本发明实施例3步骤(1)所制备的Si-C-O颗粒的SEM微观形貌图。Fig. 10 is a SEM microscopic image of Si-C-O particles prepared in step (1) of Example 3 of the present invention.
图11为本发明实施例3步骤(1)所制备的Si-C-O颗粒的XRD物相分析图。Fig. 11 is an XRD phase analysis diagram of Si-C-O particles prepared in step (1) of Example 3 of the present invention.
图12为本发明实施例3步骤(2)所制备的锂硫电池用多孔碳球的SEM微观形貌图。Fig. 12 is a SEM microscopic image of the porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 3 of the present invention.
图13为本发明实施例3步骤(2)所制备的锂硫电池用多孔碳球的XRD物相分析图。Fig. 13 is an XRD phase analysis diagram of porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 3 of the present invention.
图14为本发明实施例3步骤(2)所制备的锂硫电池用多孔碳球的透射电镜图;其中a图为多个颗粒的透射电镜图像,b图为单个颗粒的高分辨透射电镜图像,c图为单个颗粒局部的高分辨透射电镜图像。Figure 14 is a transmission electron microscope image of porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 3 of the present invention; where a is a transmission electron microscope image of multiple particles, and b is a high-resolution transmission electron microscope image of a single particle , c is a high-resolution transmission electron microscope image of a single particle.
图15为本发明实施例3制备的锂硫电池的充放电曲线。Fig. 15 is the charge-discharge curve of the lithium-sulfur battery prepared in Example 3 of the present invention.
图16为本发明实施例3制备的锂硫电池的循环寿命图。Fig. 16 is a diagram of the cycle life of the lithium-sulfur battery prepared in Example 3 of the present invention.
图17为本发明实施例3制备的锂硫电池的倍率性能。Figure 17 shows the rate performance of the lithium-sulfur battery prepared in Example 3 of the present invention.
图例说明:illustration:
1、低分子聚碳硅烷;2、三口烧瓶;3、温度计;4、加热套;5、管式炉;6、石墨舟;7、氮气罐;8、真空泵。1. Low molecular polycarbosilane; 2. Three-neck flask; 3. Thermometer; 4. Heating mantle; 5. Tube furnace; 6. Graphite boat; 7. Nitrogen tank; 8. Vacuum pump.
具体实施方式detailed description
以下结合说明书附图和具体优选的实施例对本发明作进一步描述,但并不因此而限制本发明的保护范围。The present invention will be further described below in conjunction with the accompanying drawings and specific preferred embodiments, but the protection scope of the present invention is not limited thereby.
实施例1:Example 1:
一种本发明的锂硫电池用多孔碳球,是由带状石墨无序缠绕而成。带状石墨由10~20片石墨片组成。A porous carbon sphere for a lithium-sulfur battery of the present invention is formed by disorderly winding strip-shaped graphite. Ribbon graphite is composed of 10-20 graphite flakes.
一种上述本实施例的锂硫电池用多孔碳球的制备方法,包括以下步骤:A preparation method of the porous carbon spheres for lithium-sulfur batteries of the above-mentioned present embodiment, comprising the following steps:
(1)制备Si-C-O颗粒:以低分子聚碳硅烷(数均分子量Mn约700,Si和C的原子比例为1∶2)为原料进行加热气化,在N2气氛保护下通过低压化学气相沉积工艺制备Si-C-O颗粒。低压化学气相沉积所用到的设备原理示意图如图1所示,具体方法如下:将低分子聚碳硅烷1(特种树脂)置于三口烧瓶2中,三口烧瓶2的三个口分别连接氮气罐7的进气管道、管式炉5的一端和温度计3,管式炉5的另一端连接真空泵8,管式炉5中放置有石墨舟6。开启真空泵8,并对管式炉5进行加热,管式炉5加热升温过程中真空泵8一直运行,待管式炉5的温度上升到沉积温度后,接通氮气,并开启三口烧瓶加热套4,将三口烧瓶2中的低分子聚碳硅烷1加热至设定温度。气压差导致三口烧瓶2中挥发出气态低分子聚碳硅烷进入到管式炉5中,这些气态低分子聚碳硅烷在管式炉5的高温区裂解生成Si-C-O颗粒并沉积在石墨舟6上。在该低压化学气相沉积过程中,通入氮气的目的主要有两方面,其一是提供特种树脂裂解所需的保护气氛,其二是将气态特种树脂输运至管式炉5中。因此,氮气的流量也可以根据所要制备的Si-C-O颗粒的量进行调整。低压化学气相沉积工艺结束时,关闭氮气和真空泵,停止加热管式炉,并立即停止加热特种树脂。(1) Preparation of Si-CO particles: use low-molecular polycarbosilane (the number-average molecular weight Mn is about 700, and the atomic ratio of Si and C is 1:2) as raw material for heating and gasification, and under the protection of N2 atmosphere, it is carried out by low-pressure chemical Si-CO particles were prepared by vapor deposition process. The schematic diagram of the equipment used in low-pressure chemical vapor deposition is shown in Figure 1, and the specific method is as follows: put low-molecular polycarbosilane 1 (special resin) in a three-necked flask 2, and the three ports of the three-necked flask 2 are respectively connected to a nitrogen tank 7 One end of the air inlet pipe, the tube furnace 5 and the thermometer 3, the other end of the tube furnace 5 is connected with a vacuum pump 8, and a graphite boat 6 is placed in the tube furnace 5. Turn on the vacuum pump 8, and heat the tube furnace 5. During the heating process of the tube furnace 5, the vacuum pump 8 keeps running. After the temperature of the tube furnace 5 rises to the deposition temperature, turn on nitrogen, and turn on the three-necked flask heating jacket 4 , the low molecular weight polycarbosilane 1 in the three-necked flask 2 was heated to the set temperature. The pressure difference causes the gaseous low-molecular-weight polycarbosilane volatilized in the three-necked flask 2 to enter the tube furnace 5. These gaseous low-molecular-weight polycarbosilanes are cracked in the high-temperature zone of the tube furnace 5 to generate Si-CO particles and deposited on the graphite boat 6. superior. In the low-pressure chemical vapor deposition process, the purpose of introducing nitrogen gas mainly has two aspects, one is to provide the protective atmosphere required for the cracking of special resin, and the other is to transport the gaseous special resin to the tube furnace 5 . Therefore, the flow rate of nitrogen can also be adjusted according to the amount of Si-CO particles to be prepared. At the end of the LPCVD process, turn off the nitrogen and vacuum pumps, stop heating the tube furnace, and immediately stop heating the specialty resin.
本实施例中,低分子聚碳硅烷1加热的设定温度为120℃(即加热气化温度),低压化学气相沉积温度为1000℃,压力为1000 Pa,沉积时间为1h。本实施例所制备的Si-C-O颗粒的SEM微观形貌如图2所示,可见1000℃低压化学气相沉积所制备的Si-C-O颗粒表面呈球状,颗粒表面光滑,颗粒之间彼此相连。所制备的Si-C-O颗粒的元素含量如表1所示,可知1000℃低压化学气相沉积所制备的颗粒主要由硅、碳、氧三种元素组成。所制备的Si-C-O颗粒的XRD物相分析如图3所示,在XRD谱图中只能观察到石墨相对应的衍射峰,而无法观察到SiC相对应的衍射峰,这主要是由于制备温度低,SiC相难以结晶,硅原子只能在局部与碳原子成键和/或与氧原子成键,不足以形成单独的相。In this embodiment, the low-molecular polycarbosilane 1 is heated at a set temperature of 120° C. (ie, the heating vaporization temperature), the low-pressure chemical vapor deposition temperature is 1000° C., the pressure is 1000 Pa, and the deposition time is 1 h. The SEM microscopic morphology of the Si-C-O particles prepared in this example is shown in Figure 2. It can be seen that the surface of the Si-C-O particles prepared by low-pressure chemical vapor deposition at 1000°C is spherical, the surface of the particles is smooth, and the particles are connected to each other. The element content of the prepared Si-C-O particles is shown in Table 1. It can be seen that the particles prepared by LPCVD at 1000°C are mainly composed of three elements: silicon, carbon and oxygen. The XRD phase analysis of the prepared Si-C-O particles is shown in Figure 3. In the XRD spectrum, only the diffraction peaks corresponding to graphite can be observed, but the diffraction peaks corresponding to SiC cannot be observed. This is mainly due to the preparation The temperature is low, the SiC phase is difficult to crystallize, and the silicon atoms can only bond with carbon atoms and/or bond with oxygen atoms locally, which is not enough to form a separate phase.
表1:实施例1步骤(1)所制备的Si-C-O颗粒的元素含量表Table 1: Element content table of Si-C-O particles prepared in step (1) of Example 1
(2)制备多孔碳球:将盛装有步骤(1)所得Si-C-O颗粒的石墨坩埚置于石墨加热炉中,在氩气保护下进行高温热处理,以去除Si-C-O颗粒中的硅元素和氧元素,得到锂硫电池用多孔碳球。本实施例中,高温热处理温度为2700℃,保温时间为1h。所制备的锂硫电池用多孔碳球的SEM微观形貌如图4所示,可见2700℃热处理后的Si-C-O颗粒表面依然光滑,且呈球状。所制备的锂硫电池用多孔碳球的物相分析如图5所示,2700℃热处理后所得颗粒的XRD衍射结果表明其只含石墨相。所制备的锂硫电池用多孔碳球的含量如表2所示,可知2700℃热处理后所得颗粒只含有碳元素。这说明Si-C-O颗粒在2700℃高温热处理过程中,Si-C和Si-O键断裂,硅元素和氧元素以气态SiO、CO、CO2等形式逸出,继而产生原子级尺寸孔洞,残余的C元素结晶形成带状石墨并呈现出缠绕在一起的多孔结构。(2) Preparation of porous carbon spheres: place the graphite crucible containing the Si-CO particles obtained in step (1) in a graphite heating furnace, and perform high-temperature heat treatment under the protection of argon to remove silicon and oxygen element to obtain porous carbon spheres for lithium-sulfur batteries. In this embodiment, the high temperature heat treatment temperature is 2700° C., and the holding time is 1 h. The SEM microscopic morphology of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Figure 4. It can be seen that the surface of Si-CO particles after heat treatment at 2700 °C is still smooth and spherical. The phase analysis of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Figure 5. The XRD diffraction results of the particles obtained after heat treatment at 2700°C show that they only contain graphite phase. The content of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Table 2. It can be seen that the particles obtained after heat treatment at 2700°C only contain carbon elements. This shows that during the high-temperature heat treatment of Si-CO particles at 2700 °C, the Si-C and Si-O bonds are broken, and silicon and oxygen elements escape in the form of gaseous SiO, CO, CO 2 , etc., and then produce atomic-scale holes, and the remaining The C element crystallizes to form ribbon-shaped graphite and presents an intertwined porous structure.
表2:实施例1步骤(2)所制备的锂硫电池用多孔碳球的元素含量表Table 2: Element content table of porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 1
实施例2:Example 2:
一种本发明的锂硫电池用多孔碳球,是由带状石墨无序缠绕而成。带状石墨由10~20片石墨片组成。A porous carbon sphere for a lithium-sulfur battery of the present invention is formed by disorderly winding strip-shaped graphite. Ribbon graphite is composed of 10-20 graphite flakes.
一种上述本实施例的锂硫电池用多孔碳球的制备方法,包括以下步骤:A preparation method of the porous carbon spheres for lithium-sulfur batteries of the above-mentioned present embodiment, comprising the following steps:
(1)制备Si-C-O颗粒:本实施例制备Si-C-O颗粒的原材料及方法与实施例1基本相同,其不同仅在于:本实施例中,低分子聚碳硅烷加热的设定温度为150℃,低压化学气相沉积温度为1100℃,压力为1000Pa,沉积时间为1h。所制备的Si-C-O颗粒的SEM微观形貌如图6所示,可见1100℃低压化学气相沉积所制备的Si-C-O颗粒表面呈球状,颗粒表面分布着少量粒状凸起,球状颗粒彼此相连。所制备的Si-C-O颗粒的元素含量如表3所示,可知1100℃低压化学气相沉积所制备的颗粒主要由硅、碳、氧三种元素组成。所制备的Si-C-O颗粒的物相分析如图7所示,在XRD谱图中只能观察到石墨相对应的衍射峰,而无法观察到SiC相对应的衍射峰,这主要是由于制备温度低,SiC相难以结晶,因而难以观察到SiC相对应的衍射峰。(1) Preparation of Si-C-O particles: The raw materials and method for preparing Si-C-O particles in this example are basically the same as in Example 1, the only difference being that in this example, the set temperature for heating low-molecular polycarbosilane is 150 °C, the low pressure chemical vapor deposition temperature is 1100 °C, the pressure is 1000 Pa, and the deposition time is 1 h. The SEM microscopic morphology of the prepared Si-C-O particles is shown in Figure 6. It can be seen that the surface of the Si-C-O particles prepared by low-pressure chemical vapor deposition at 1100 °C is spherical, with a small amount of granular protrusions distributed on the surface of the particles, and the spherical particles are connected to each other. The element content of the prepared Si-C-O particles is shown in Table 3. It can be seen that the particles prepared by low-pressure chemical vapor deposition at 1100°C are mainly composed of three elements: silicon, carbon and oxygen. The phase analysis of the prepared Si-C-O particles is shown in Figure 7. In the XRD spectrum, only the diffraction peaks corresponding to graphite can be observed, but the diffraction peaks corresponding to SiC cannot be observed. This is mainly due to the preparation temperature Low, the SiC phase is difficult to crystallize, so it is difficult to observe the corresponding diffraction peaks of SiC.
表3:实施例2步骤(1)所制备的Si-C-O颗粒的元素含量表Table 3: Element content table of Si-C-O particles prepared in step (1) of Example 2
(2)制备多孔碳球:将盛装有步骤(1)所得Si-C-O颗粒的石墨坩埚置于石墨加热炉中,在氩气保护下进行高温热处理,以去除Si-C-O颗粒中的硅元素和氧元素,得到锂硫电池用多孔碳球。本实施例中,高温热处理温度为2600℃,保温时间为1h。所制备的锂硫电池用多孔碳球的SEM微观形貌如图8所示,可见2600℃热处理后的Si-C-O颗粒表面光滑,且呈球状。所制备的锂硫电池用多孔碳球的物相分析如图9所示,2600℃热处理后所得颗粒的XRD衍射结果表明其只含石墨相对应的衍射峰。所制备的锂硫电池用多孔碳球的含量如表4所示,可知2600℃热处理后所得颗粒只含有碳元素。这说明Si-C-O颗粒在2700℃高温热处理过程中,Si-C和Si-O键断裂,硅元素和氧元素以气态SiO、CO、CO2等形式逸出,继而产生原子级尺寸孔洞,残余的C元素结晶形成带状石墨并呈现出缠绕在一起的多孔结构。(2) Preparation of porous carbon spheres: place the graphite crucible containing the Si-CO particles obtained in step (1) in a graphite heating furnace, and perform high-temperature heat treatment under the protection of argon to remove silicon and oxygen element to obtain porous carbon spheres for lithium-sulfur batteries. In this embodiment, the high temperature heat treatment temperature is 2600° C., and the holding time is 1 h. The SEM microscopic morphology of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Figure 8. It can be seen that the Si-CO particles after heat treatment at 2600 °C have a smooth surface and a spherical shape. The phase analysis of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Figure 9. The XRD diffraction results of the particles obtained after heat treatment at 2600°C show that they only contain diffraction peaks corresponding to graphite. The content of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Table 4. It can be seen that the particles obtained after heat treatment at 2600°C only contain carbon elements. This shows that during the high-temperature heat treatment of Si-CO particles at 2700 °C, the Si-C and Si-O bonds are broken, and silicon and oxygen elements escape in the form of gaseous SiO, CO, CO 2 , etc., and then produce atomic-scale holes, and the remaining The C element crystallizes to form ribbon-shaped graphite and presents an intertwined porous structure.
表4:实施例2步骤(2)所制备的锂硫电池用多孔碳球的元素含量表Table 4: Element content table of porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 2
实施例3:Example 3:
一种本发明的锂硫电池用多孔碳球,是由带状石墨无序缠绕而成。带状石墨由10~20片石墨片组成。A porous carbon sphere for a lithium-sulfur battery of the present invention is formed by disorderly winding strip-shaped graphite. Ribbon graphite is composed of 10-20 graphite flakes.
一种上述本实施例的锂硫电池用多孔碳球的制备方法,包括以下步骤:A preparation method of the porous carbon spheres for lithium-sulfur batteries of the above-mentioned present embodiment, comprising the following steps:
(1)制备Si-C-O颗粒:本实施例制备Si-C-O颗粒的原材料及方法与实施例1基本相同,其不同仅在于:本实施例中,低分子聚碳硅烷加热的设定温度为180℃,低压化学气相沉积温度为1200℃,压力为1000 Pa,沉积时间为1h。所制备的Si-C-O颗粒的SEM微观形貌如图10所示,可见1200℃低压化学气相沉积合成的Si-C-O颗粒依然呈球状,但是其表面片状凸起。所制备的Si-C-O颗粒的元素含量如表5所示,可知1200℃低压化学气相沉积所制备的颗粒主要由硅、碳、氧三种元素组成。所制备的Si-C-O颗粒的物相分析如图11所示,1200℃低压化学沉积所制备的Si-C-O颗粒的XRD谱图中可以明显观察到石墨相的衍射峰和SiC相的衍射峰。(1) Preparation of Si-C-O particles: The raw materials and method for preparing Si-C-O particles in this example are basically the same as in Example 1, the only difference is that in this example, the set temperature for heating low-molecular polycarbosilane is 180 °C, the low pressure chemical vapor deposition temperature is 1200 °C, the pressure is 1000 Pa, and the deposition time is 1 h. The SEM microscopic morphology of the prepared Si-C-O particles is shown in Figure 10. It can be seen that the Si-C-O particles synthesized by low-pressure chemical vapor deposition at 1200 °C are still spherical, but their surface is flaky and convex. The element content of the prepared Si-C-O particles is shown in Table 5. It can be seen that the particles prepared by LPCVD at 1200°C are mainly composed of three elements: silicon, carbon and oxygen. The phase analysis of the prepared Si-C-O particles is shown in Figure 11. The diffraction peaks of the graphite phase and the SiC phase can be clearly observed in the XRD spectrum of the Si-C-O particles prepared by low-pressure chemical deposition at 1200 °C.
表5:实施例3步骤(1)所制备的Si-C-O颗粒的元素含量表Table 5: Element content table of Si-C-O particles prepared in step (1) of Example 3
(2)制备多孔碳球:将盛装有步骤(1)所得Si-C-O颗粒的石墨坩埚置于石墨加热炉中,在氩气保护下进行高温热处理,以去除Si-C-O颗粒中的硅元素和氧元素,得到锂硫电池用多孔碳球。本实施例中,高温热处理温度为2700℃,保温时间为1h。所制备的锂硫电池用多孔碳球的SEM微观形貌如图12所示,可见经过2700℃热处理后,颗粒依然呈球状,而且颗粒表面片层状凸起依然存在。图14是所制备的锂硫电池用多孔碳球的透射电镜图,其中b图和C图可清晰的看出,所得锂硫电池用多孔碳球是一种由带状石墨无序缠绕而形成的多孔结构,带状石墨之间的间隙构成了多孔碳球的孔隙。所制备的锂硫电池用多孔碳球的含量如表6所示,可知2700℃热处理后所得颗粒只含有碳元素。所制备的锂硫电池用多孔碳球的物相分析如图13所示,经过2700℃热处理后所得颗粒的XRD谱图中只存在石墨相对应的衍射峰,说明Si-C-O颗粒在2700℃高温热处理过程中,Si-C和Si-O键断裂,硅元素和氧元素逸出,继而产生原子级尺寸孔洞,残余的C元素结晶形成带状石墨并呈现出缠绕在一起的多孔结构。(2) Preparation of porous carbon spheres: place the graphite crucible containing the Si-C-O particles obtained in step (1) in a graphite heating furnace, and perform high-temperature heat treatment under the protection of argon to remove silicon and oxygen element to obtain porous carbon spheres for lithium-sulfur batteries. In this embodiment, the high temperature heat treatment temperature is 2700° C., and the holding time is 1 h. The SEM microscopic morphology of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Figure 12. It can be seen that after heat treatment at 2700 °C, the particles are still spherical, and the lamellar protrusions on the surface of the particles still exist. Figure 14 is a transmission electron microscope image of the prepared porous carbon spheres for lithium-sulfur batteries, in which b and c can clearly see that the obtained porous carbon spheres for lithium-sulfur batteries are formed by the disordered winding of ribbon graphite The porous structure of the graphite ribbons constitutes the pores of the porous carbon spheres. The content of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Table 6. It can be seen that the particles obtained after heat treatment at 2700°C only contain carbon elements. The phase analysis of the prepared porous carbon spheres for lithium-sulfur batteries is shown in Figure 13. In the XRD spectrum of the particles obtained after heat treatment at 2700 °C, there are only diffraction peaks corresponding to graphite, indicating that Si-C-O particles are exposed to high temperatures at 2700 °C. During the heat treatment, the Si-C and Si-O bonds are broken, silicon and oxygen elements escape, and then atomic-scale pores are generated, and the remaining C elements crystallize to form ribbon graphite and present an intertwined porous structure.
表6:实施例3步骤(2)所制备的锂硫电池用多孔碳球的元素含量表Table 6: Element content table of porous carbon spheres for lithium-sulfur batteries prepared in step (2) of Example 3
一种本实施例的锂硫电池用多孔碳球在锂硫电池制备中的应用,该应用是指将上述本实施例的锂硫电池用多孔碳球和硫粉混合用于制备锂硫电池的正极材料,锂硫电池用多孔碳球与硫粉的质量比为3∶2。该正极材料的制备方法如下:首先将多孔碳球研磨碎,并与硫粉末以质量比为3∶2的比例混合;随后,将混合粉末加热至155℃,然后保温10h,得到多孔碳球-硫复合材料;最后,将80wt%的多孔碳球-硫复合材料,10wt%超导碳和10wt%的PVDF混合均匀成浆料,涂附在铝箔上,在60℃真空下干燥24h,得到该正极材料。An application of the porous carbon spheres for lithium-sulfur batteries of this embodiment in the preparation of lithium-sulfur batteries, which refers to mixing the porous carbon spheres for lithium-sulfur batteries of this embodiment with sulfur powder to prepare lithium-sulfur batteries The positive electrode material, the mass ratio of porous carbon spheres for lithium-sulfur batteries to sulfur powder is 3:2. The preparation method of the positive electrode material is as follows: firstly, the porous carbon spheres are pulverized, and mixed with the sulfur powder at a mass ratio of 3:2; subsequently, the mixed powder is heated to 155° C., and then kept for 10 hours to obtain the porous carbon spheres- Sulfur composite material; finally, 80wt% porous carbon sphere-sulfur composite material, 10wt% superconducting carbon and 10wt% PVDF were mixed uniformly to form a slurry, coated on aluminum foil, and dried under vacuum at 60°C for 24h to obtain the Cathode material.
将上述正极材料作为正极片组装在锂硫电池上,该锂硫电池在0.2C (1C=1672mA/g)的第1次、第2次、第3次和第50次充放电曲线如图15所示,从图中可以看出,首次放电曲线显示两个稳定的放电平台,分别对应Ss向多硫离子Li2Sx的转化,和多硫离子向Li2S的进一步还原。本实施例的以多孔碳球-硫复合材料为正极的锂硫电池首次放电容量高达950mAh/g,而目前商用锂硫电池的首次放电容量一般只有700~800mAh/g,因此,本实施例的锂硫电池具有比较好的首次放电容量。该锂硫电池在0.2C (1C=1672mA/g)的循环寿命如图16所示,从图中可以看出,经过100周期后电池的容量能够保持在93.9%(相对于第5次充放电容量,下同),经200周期后电池的容量能够保持在83%,经300周期后电池的容量能够保持在71.1%,经400周期后电池的容量能够保持在65%,经500周期后电池的容量能够保持在55%。而目前商用锂硫电池经过100次循环后,其容量保留率只有60%~70%,说明本实施例的以多孔碳球-硫复合材料为正极的锂硫电池具有较好的循环稳定性。在多孔碳球-硫复合物中,多孔碳球不但能够为硫电极提供有效的导电通道,并且能够缓冲硫电极充放电过程中引起的体积变化,并且多孔碳球中的微孔结构能够有效的抑制充放电过程中产生的多硫化物在电解液中的溶解,因此电池容量保持率得到很大提高。本实施例的锂硫电池用多孔碳球是由石墨带无序缠绕而成的多孔结构,其石墨带是由多层(10~20层)石墨片组成,由于石墨带所含石墨片的片层数较多,稳定性较高,因而在电池的充放电过程中不易破损,能够较长时间的保持完整,因此循环稳定性较目前商用锂硫电池更高。图 17是由多孔碳球-硫复合材料组成正极的倍率性能,从图中可以看出多孔碳球-硫复合材料组成的正极具有较好的倍率性能,在0.1C下容量为750 mAh/g,在不同倍率下30次循环后,在4C下放电容量仍然能够达到500 mAh/g,这说明多孔碳球能够较大的提高硫电极的导电性。The above-mentioned positive electrode material is assembled on a lithium-sulfur battery as a positive electrode sheet. The charge-discharge curves of the lithium-sulfur battery at 0.2C (1C=1672mA/g) for the first, second, third and 50th times are shown in Figure 15 It can be seen from the figure that the first discharge curve shows two stable discharge plateaus, corresponding to the conversion of S s to polysulfide ions Li 2 S x and the further reduction of polysulfide ions to Li 2 S, respectively. The initial discharge capacity of the lithium-sulfur battery using the porous carbon sphere-sulfur composite material as the positive electrode in this embodiment is as high as 950mAh/g, while the initial discharge capacity of current commercial lithium-sulfur batteries is generally only 700-800mAh/g. Therefore, the lithium-sulfur battery of this embodiment Lithium-sulfur batteries have relatively good initial discharge capacity. The cycle life of the lithium-sulfur battery at 0.2C (1C=1672mA/g) is shown in Figure 16. It can be seen from the figure that the capacity of the battery can be maintained at 93.9% after 100 cycles (relative to the 5th charge and discharge Capacity, the same below), after 200 cycles, the capacity of the battery can be maintained at 83%, after 300 cycles, the capacity of the battery can be maintained at 71.1%, after 400 cycles, the capacity of the battery can be maintained at 65%, after 500 cycles The capacity can be maintained at 55%. However, the current commercial lithium-sulfur battery has a capacity retention rate of only 60% to 70% after 100 cycles, indicating that the lithium-sulfur battery in this example with the porous carbon sphere-sulfur composite material as the positive electrode has better cycle stability. In the porous carbon sphere-sulfur composite, the porous carbon sphere can not only provide an effective conductive channel for the sulfur electrode, but also buffer the volume change caused by the charging and discharging process of the sulfur electrode, and the microporous structure in the porous carbon sphere can effectively Inhibit the dissolution of polysulfides in the electrolyte during charging and discharging, so the battery capacity retention rate is greatly improved. The porous carbon spheres for lithium-sulfur batteries in this embodiment are porous structures formed by disorderly winding of graphite ribbons, and the graphite ribbons are composed of multi-layer (10-20 layers) graphite sheets. There are more layers and higher stability, so it is not easy to be damaged during the charging and discharging process of the battery, and can remain intact for a long time, so the cycle stability is higher than that of the current commercial lithium-sulfur battery. Figure 17 is the rate performance of the positive electrode composed of porous carbon spheres-sulfur composites. It can be seen from the figure that the positive electrode composed of porous carbon spheres-sulfur composites has good rate performance, with a capacity of 750 mAh/g at 0.1C , after 30 cycles at different rates, the discharge capacity can still reach 500 mAh/g at 4C, which shows that the porous carbon spheres can greatly improve the conductivity of the sulfur electrode.
以上所述仅是本发明的优选实施方式,本发明的保护范围并不仅局限于上述实施例。凡属于本发明思路下的技术方案均属于本发明的保护范围。应该指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下的改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above descriptions are only preferred implementations of the present invention, and the scope of protection of the present invention is not limited to the above examples. All technical solutions under the idea of the present invention belong to the protection scope of the present invention. It should be pointed out that for those skilled in the art, improvements and modifications without departing from the principle of the present invention should also be regarded as the protection scope of the present invention.
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