CN117623270A - Sodium ion battery hard carbon negative electrode material prepared by biomass-based crosslinking and application thereof - Google Patents
Sodium ion battery hard carbon negative electrode material prepared by biomass-based crosslinking and application thereof Download PDFInfo
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- 229910021385 hard carbon Inorganic materials 0.000 title claims abstract description 75
- 229910001415 sodium ion Inorganic materials 0.000 title claims abstract description 38
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 title claims abstract description 37
- 239000002028 Biomass Substances 0.000 title claims abstract description 27
- 239000007773 negative electrode material Substances 0.000 title claims abstract description 22
- 238000004132 cross linking Methods 0.000 title claims abstract description 13
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 108
- 239000000243 solution Substances 0.000 claims abstract description 74
- 229920001661 Chitosan Polymers 0.000 claims abstract description 73
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims abstract description 66
- 238000003756 stirring Methods 0.000 claims abstract description 42
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 39
- 238000003763 carbonization Methods 0.000 claims abstract description 30
- 238000000197 pyrolysis Methods 0.000 claims abstract description 30
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- 229920002678 cellulose Polymers 0.000 claims abstract description 29
- 239000011259 mixed solution Substances 0.000 claims abstract description 24
- 238000006243 chemical reaction Methods 0.000 claims abstract description 22
- 238000010335 hydrothermal treatment Methods 0.000 claims abstract description 22
- 238000001035 drying Methods 0.000 claims abstract description 21
- 239000012298 atmosphere Substances 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims abstract description 3
- 238000005406 washing Methods 0.000 claims abstract 2
- 238000010438 heat treatment Methods 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 23
- 230000035484 reaction time Effects 0.000 claims description 23
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 239000010405 anode material Substances 0.000 claims description 7
- 239000006230 acetylene black Substances 0.000 claims description 3
- 239000011230 binding agent Substances 0.000 claims description 3
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 claims description 2
- 238000004321 preservation Methods 0.000 claims 2
- 239000001768 carboxy methyl cellulose Substances 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 239000011267 electrode slurry Substances 0.000 claims 1
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 claims 1
- 229920001027 sodium carboxymethylcellulose Polymers 0.000 claims 1
- 238000002360 preparation method Methods 0.000 abstract description 6
- 238000010382 chemical cross-linking Methods 0.000 abstract description 2
- 238000012546 transfer Methods 0.000 description 42
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- 239000013078 crystal Substances 0.000 description 5
- 230000002441 reversible effect Effects 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 5
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 4
- 238000004146 energy storage Methods 0.000 description 4
- 125000005842 heteroatom Chemical group 0.000 description 4
- 229910052744 lithium Inorganic materials 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
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- 229910052708 sodium Inorganic materials 0.000 description 3
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- 230000002195 synergetic effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
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- 235000010777 Arachis hypogaea Nutrition 0.000 description 1
- 235000018262 Arachis monticola Nutrition 0.000 description 1
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- 244000082204 Phyllostachys viridis Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
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- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 229920003123 carboxymethyl cellulose sodium Polymers 0.000 description 1
- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 description 1
- 229940063834 carboxymethylcellulose sodium Drugs 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
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- 229910002804 graphite Inorganic materials 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
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- 235000020232 peanut Nutrition 0.000 description 1
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- 239000004848 polyfunctional curative Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
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- 230000008707 rearrangement Effects 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
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- 238000012360 testing method Methods 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- -1 transition metal salt Chemical class 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/05—Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
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- H—ELECTRICITY
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- 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
- H01M10/054—Accumulators with insertion or intercalation of metals other than lithium, e.g. with magnesium or aluminium
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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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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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- 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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Abstract
Description
技术领域Technical field
本发明属于二次电池技术领域,具体涉及钠离子电池负极技术领域,特别涉及一种生物质基交联制备的钠离子电池硬碳负极材料及其应用。The invention belongs to the technical field of secondary batteries, specifically relates to the technical field of sodium-ion battery negative electrodes, and particularly relates to a sodium-ion battery hard carbon negative electrode material prepared by biomass-based cross-linking and its application.
背景技术Background technique
随着电动汽车、电子产品以及储能器件的快速发展,锂离子电池由于高能量密度和良好的循环稳定性在储能技术领域一直占主导地位。然而受到锂资源高昂成本和分布不均衡性影响,这大大限制了其在大规模储能电网以及低成本储能器件方面的应用。相比之下,化学性质与锂元素相近的钠元素逐渐进入了人们的视野,钠离子电池由于其成本低廉、钠元素分布广泛以及我国储量丰富,在一定程度上可以缓解锂资源短缺的问题,同时也可以逐步替代具有安全隐患的铅酸电池。With the rapid development of electric vehicles, electronic products, and energy storage devices, lithium-ion batteries have always dominated the field of energy storage technology due to their high energy density and good cycle stability. However, the high cost and uneven distribution of lithium resources have greatly limited its application in large-scale energy storage grids and low-cost energy storage devices. In contrast, sodium, which has similar chemical properties to lithium, has gradually entered people's field of vision. Due to its low cost, wide distribution of sodium and abundant reserves in my country, sodium-ion batteries can alleviate the shortage of lithium resources to a certain extent. At the same time, it can also gradually replace lead-acid batteries with safety hazards.
现阶段实现高性能、低成本的钠离子电池仍然是一项巨大的挑战,尤其是钠离子电池硬碳负极材料被认作是电化学性能、成本控制以及资源可持续发展的最佳选择。硬碳作为非石墨碳之一,具有较大的层间距和丰富的缺陷以及多孔性,可以为Na+提供丰富的活性位点,更为重要的是,硬碳作为钠离子电池负极材料具有较低的工作电压与较高的容量,满足了电池应用的安全性与功能性。At this stage, realizing high-performance, low-cost sodium-ion batteries is still a huge challenge. In particular, hard carbon anode materials for sodium-ion batteries are considered to be the best choice for electrochemical performance, cost control, and sustainable resource development. As one of the non-graphitic carbons, hard carbon has large interlayer spacing and abundant defects and porosity, which can provide abundant active sites for Na + . More importantly, hard carbon has relatively high performance as an anode material for sodium ion batteries. Low operating voltage and high capacity meet the safety and functionality of battery applications.
中国石油大学(华东)在CN115124025A中提供了一种硬碳材料及其制备方法和在钠离子电池中的应用,首先控制碳源粒径确保粒径均匀,然后采用“盐晶水热-闪烧”相协同的方法,通过盐晶水热过程将过渡金属盐渗透到碳源前体中,在闪烧碳化过程中以盐晶为模板精准调控硬碳材料的微观孔隙结构、表面化学成分和石墨化程度,形成更加稳定的有益于提高电化学性能的结构;通过闪烧碳化过程能够使盐晶周围局部温度高于硬碳基体材料,且金属阳离子能够催化碳原子在高温下发生原子重排,使得盐晶周围局部石墨化程度提高,从而瞬时提高硬碳材料的石墨化程度,同时对硬碳材料的缺陷进行限制,提高钠离子电池的比容量。China University of Petroleum (East China) provides a hard carbon material, its preparation method and application in sodium-ion batteries in CN115124025A. First, the particle size of the carbon source is controlled to ensure uniform particle size, and then "salt crystal hydrothermal-flash burning" is used. "In a synergistic approach, the transition metal salt is penetrated into the carbon source precursor through the salt crystal hydrothermal process, and the salt crystal is used as a template to precisely control the microscopic pore structure, surface chemical composition and graphite of the hard carbon material during the flash carbonization process. degree of chemicalization, forming a more stable structure that is beneficial to improving electrochemical performance; through the flash carbonization process, the local temperature around the salt crystal can be higher than that of the hard carbon matrix material, and the metal cations can catalyze the atomic rearrangement of carbon atoms at high temperatures. This increases the degree of local graphitization around the salt crystals, thereby instantly increasing the degree of graphitization of the hard carbon material, while limiting the defects of the hard carbon material and increasing the specific capacity of the sodium-ion battery.
惠州亿纬锂能股份有限公司在CN115321514A中提供了一种硬碳材料及其制备方法与应用,所述硬碳材料掺杂有杂原子,所述杂原子包括N原子和M原子,所述M原子包括As、Se、Sb或Te中至少两种的组合。所述硬碳材料能通过简单的合成工艺制备,且掺杂至少三种杂原子,通过杂原子间的协同作用,既能增大硬碳材料的层间距,又能引入缺陷位点,使硬碳材料的结构发生较大畸变,从而增加了钠离子的嵌入容量和吸附容量,使硬碳材料具备高克容量和高倍率性能。Huizhou Yiwei Lithium Energy Co., Ltd. provides a hard carbon material and its preparation method and application in CN115321514A. The hard carbon material is doped with heteroatoms, and the heteroatoms include N atoms and M atoms. The M atoms Atoms include a combination of at least two of As, Se, Sb or Te. The hard carbon material can be prepared through a simple synthesis process and doped with at least three types of heteroatoms. Through the synergistic effect between heteroatoms, it can not only increase the interlayer spacing of the hard carbon material, but also introduce defect sites to make the hard carbon material more durable. The structure of the carbon material is greatly distorted, thereby increasing the insertion capacity and adsorption capacity of sodium ions, making the hard carbon material have high gram capacity and high rate performance.
整体来说,现有技术中使用生物质衍生制备的硬碳材料的方法不多,同时存在硬碳结构控制较低,性能较差的特点。本发明旨在克服以上问题,选取合适的方法,对生物质材料进行交联,合理控制硬碳表面的缺陷,提升硬碳负极材料的可逆容量与首周库伦效率。Generally speaking, there are not many methods for using hard carbon materials derived from biomass in the existing technology. At the same time, the structure control of hard carbon is low and its performance is poor. The present invention aims to overcome the above problems, select appropriate methods to cross-link biomass materials, reasonably control defects on the surface of hard carbon, and improve the reversible capacity and first-cycle Coulombic efficiency of hard carbon negative electrode materials.
发明内容Contents of the invention
本发明目的在于提供制备工艺简单,适用性经济可行,对于大规模工业化生产具有应用前景,具有优异的倍率性能,首周库伦效率高达83.0%的硬碳材料。具体来说,通过水热反应法将两种生物质基材料进行交联处理,使交联的生物质大分子结构能够在热解的过程中阻止小分子气体的释放,减小硬碳表面缺陷的形成,有助于电子的转移,提高硬碳负极材料的可逆容量与首周库伦效率。The purpose of the present invention is to provide a hard carbon material with simple preparation process, economical applicability, application prospects for large-scale industrial production, excellent rate performance, and first-week Coulombic efficiency as high as 83.0%. Specifically, two biomass-based materials are cross-linked through a hydrothermal reaction method, so that the cross-linked biomass macromolecular structure can prevent the release of small molecule gases during the pyrolysis process and reduce hard carbon surface defects. The formation helps the transfer of electrons and improves the reversible capacity and first-cycle Coulombic efficiency of hard carbon anode materials.
本发明所采用的技术方案如下:The technical solutions adopted by the present invention are as follows:
一种生物质基交联制备钠离子电池硬碳负极材料的方法,包括如下步骤:A biomass-based cross-linking method for preparing hard carbon negative electrode materials for sodium ion batteries, including the following steps:
(1)将一定质量的壳聚糖溶于乙酸溶液,搅拌使其充分溶解,配置壳聚糖溶液。(1) Dissolve a certain mass of chitosan in the acetic acid solution, stir to fully dissolve, and prepare the chitosan solution.
(2)将一定质量的纤维素加入壳聚糖溶液中,搅拌使其两者混合均匀。(2) Add a certain mass of cellulose to the chitosan solution and stir to mix the two evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理一定时间,待反应釜冷却至室温后,对水热产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment for a certain period of time. After the reaction kettle is cooled to room temperature, the hydrothermal product is centrifuged, washed and dried.
(4)将上述处理后的水热产物转移到高温管式炉中,在惰性气氛下进行高温热解碳化处理,得到硬碳材料。(4) Transfer the hydrothermal product after the above treatment to a high-temperature tube furnace, and perform high-temperature pyrolysis and carbonization treatment under an inert atmosphere to obtain hard carbon materials.
进一步地,所述的乙酸溶液为1-2g/L,壳聚糖溶液浓度为5-12g/L。Further, the acetic acid solution is 1-2g/L, and the chitosan solution concentration is 5-12g/L.
进一步地,加入纤维素与壳聚糖质量之比为3:1-6:1。Further, the mass ratio of added cellulose to chitosan is 3:1-6:1.
进一步地,纤维素与壳聚糖质量比为5:1。Further, the mass ratio of cellulose to chitosan was 5:1.
进一步地,纤维素与壳聚糖混合溶液水热反应温度为180-250℃,水热反应时间为12-48h。Further, the hydrothermal reaction temperature of the mixed solution of cellulose and chitosan is 180-250°C, and the hydrothermal reaction time is 12-48 hours.
进一步地,纤维素与壳聚糖混合溶液水热反应温度为200-240℃,水热反应时间为24-36h。Further, the hydrothermal reaction temperature of the mixed solution of cellulose and chitosan is 200-240°C, and the hydrothermal reaction time is 24-36 hours.
进一步地,高温热解碳化温度为1000-1800℃,升温速率为2-10℃/min,保温时间为2-10h。Further, the high-temperature pyrolysis carbonization temperature is 1000-1800°C, the heating rate is 2-10°C/min, and the holding time is 2-10h.
进一步地,高温热解碳化温度为1300-1500℃,升温速率为5℃/min,保温时间为3-5h。Further, the high-temperature pyrolysis carbonization temperature is 1300-1500°C, the heating rate is 5°C/min, and the holding time is 3-5h.
根据上述方法所制备的钠离子电池硬碳负极材料。The hard carbon negative electrode material for sodium ion batteries prepared according to the above method.
一种制备钠离子电池硬碳电极材料的方法,包括如下步骤:A method for preparing hard carbon electrode materials for sodium ion batteries, including the following steps:
将上述生物质基交联制备钠离子电池硬碳负极材料与导电剂乙炔黑、粘结剂羧甲基纤维素钠按照质量比8:1:1研磨成均匀的浆料,通过涂布器刮涂在铜箔上,保证活性物质质量1-1.5mg/cm2,得到钠离子电池硬碳负极电极片。The above biomass-based cross-linked hard carbon negative electrode material for sodium ion batteries is ground into a uniform slurry with the conductive agent acetylene black and the binder carboxymethyl cellulose sodium according to a mass ratio of 8:1:1, and scraped with a coater Coat it on the copper foil to ensure the mass of the active material is 1-1.5 mg/cm 2 to obtain a hard carbon negative electrode sheet for a sodium ion battery.
与现有技术相比,有益效果在于:Compared with existing technology, the beneficial effects are:
(1)本发明采用的原材料均为生物质基材料,具有来源广泛、价格低廉和绿色环保等优点,采用的方法制备工艺简单,适用性经济可行,对于大规模工业化生产具有应用前景。(1) The raw materials used in the present invention are all biomass-based materials, which have the advantages of wide sources, low prices, green environmental protection, etc. The method used has simple preparation process, applicability and economic feasibility, and has application prospects for large-scale industrial production.
(2)本发明通过将生物质基进行化学交联处理,高温热解碳化后制备的硬碳材料具有优异的倍率性能,首周库伦效率高达83.0%。(2) The present invention chemically cross-links the biomass base and prepares hard carbon materials after high-temperature pyrolysis and carbonization. It has excellent rate performance, and the Coulombic efficiency in the first week is as high as 83.0%.
附图说明Description of drawings
为了更清楚地说明本发明实施例中的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the description of the embodiments will be briefly introduced below. Obviously, the drawings in the following description are only some embodiments of the present invention. For those of ordinary skill in the art, other drawings can also be obtained based on these drawings without exerting creative efforts.
图1为实施例2所制备的生物质基交联制备钠离子电池硬碳负极材料的SEM图。Figure 1 is an SEM image of the biomass-based cross-linked hard carbon negative electrode material for sodium ion batteries prepared in Example 2.
图2为实施例2所制备的生物质基交联制备钠离子电池硬碳负极材料在50mA/g电流密度下的充放电曲线。Figure 2 is the charge and discharge curve of the biomass-based cross-linked hard carbon negative electrode material for sodium ion batteries prepared in Example 2 at a current density of 50 mA/g.
图3为实施例2所制备的生物质基交联制备钠离子电池硬碳负极材料在0.05A/g-1A/g电流密度下的倍率性能图。Figure 3 is a rate performance diagram of the biomass-based cross-linked hard carbon negative electrode material for sodium ion batteries prepared in Example 2 at a current density of 0.05A/g-1A/g.
图4为实施例2所制备的生物质基交联制备钠离子电池硬碳负极材料在0.05A/g-1A/g电流密度下的充放电曲线。Figure 4 is the charge and discharge curve of the biomass-based cross-linked hard carbon negative electrode material for sodium ion batteries prepared in Example 2 at a current density of 0.05A/g-1A/g.
图5为实施例2所制备的生物质基交联制备钠离子电池硬碳负极材料在1A/g电流密度下的长循环图。Figure 5 is a long cycle diagram of the biomass-based cross-linked hard carbon negative electrode material for sodium ion batteries prepared in Example 2 at a current density of 1 A/g.
具体实施方式Detailed ways
为了使本技术领域的人员更好地理解本发明实施例中的技术方案,并使本发明的上述目的、特征和优点能够更加明显易懂,下面对本发明的具体实施方式作进一步的说明。In order to enable those skilled in the art to better understand the technical solutions in the embodiments of the present invention and to make the above objects, features and advantages of the present invention more obvious and understandable, specific implementation modes of the present invention are further described below.
在本文中所披露的范围的端点和任何值都不限于该精确的范围或值,这些范围或值应当理解为包含接近这些范围或值的值。对于数值范围来说,各个范围的端点值之间、各个范围的端点值和单独的点值之间,以及单独的点值之间可以彼此组合而得到一个或多个新的数值范围,这些数值范围应该被视为在本文中具体公开。The endpoints of ranges and any values disclosed herein are not limited to the precise range or value, but these ranges or values are to be understood to include values approaching such ranges or values. For numerical ranges, the endpoint values of each range, the endpoint values of each range and individual point values, and the individual point values can be combined with each other to obtain one or more new numerical ranges. These values The scope should be deemed to be specifically disclosed herein.
实施例1Example 1
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1100℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1100°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例2Example 2
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例3Example 3
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1500℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1500°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例4Example 4
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为180℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 180°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例5Example 5
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将1.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 1.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix the two evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例6Example 6
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为250℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 250°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例7Example 7
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为200℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 200°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例8Example 8
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为240℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 240°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例9Example 9
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1000℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1000°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例10Example 10
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1800℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1800°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例11Example 11
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.0g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.0g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix the two evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例12Example 12
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将3.0g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 3.0g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix the two evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例13Example 13
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将1.0g纤维素加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 1.0g of cellulose to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例2Example 2
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g竹粉加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of bamboo powder to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例15Example 15
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g木粉加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of wood powder to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
实施例16Example 16
(1)将0.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 0.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将2.5g花生壳粉加入上述壳聚糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of peanut shell powder to the above chitosan solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
对比例1Comparative example 1
(1)将2.5g纤维素加入去离子水溶液,在80℃下搅拌3h使其分散均匀。(1) Add 2.5g of cellulose to the deionized water solution and stir at 80°C for 3 hours to disperse evenly.
(2)将上述溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(2) Transfer the above solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged, washed and Drying process.
(3)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到纤维素基硬碳材料。(3) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain fibers. Plain hard carbon material.
对比例2Comparative example 2
(1)将2.5g壳聚糖溶于2g/L的50mL乙酸溶液,在80℃下搅拌1h使其充分溶解,配置10g/L的壳聚糖溶液。(1) Dissolve 2.5g chitosan in 2g/L 50mL acetic acid solution, stir at 80°C for 1 hour to fully dissolve, and prepare a 10g/L chitosan solution.
(2)将上述溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(2) Transfer the above solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged, washed and Drying process.
(3)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到纤维素基硬碳材料。(3) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain fibers. Plain hard carbon material.
对比例3Comparative example 3
(1)将0.5g葡萄糖溶于50mL去离子水溶液,常温下搅拌1h使其充分溶解。(1) Dissolve 0.5g glucose in 50mL deionized water solution and stir for 1 hour at room temperature to fully dissolve.
(2)将2.5g纤维素加入上述葡萄糖溶液,在80℃下搅拌3h使其两者混合均匀。(2) Add 2.5g of cellulose to the above glucose solution and stir at 80°C for 3 hours to mix evenly.
(3)将上述混合溶液转移到水热反应釜中进行水热处理,水热反应温度为220℃,水热反应时间为24h,待反应完成冷却至室温后,对水热反应产物进行离心、洗涤和干燥处理。(3) Transfer the above mixed solution to a hydrothermal reaction kettle for hydrothermal treatment. The hydrothermal reaction temperature is 220°C and the hydrothermal reaction time is 24 hours. After the reaction is completed and cooled to room temperature, the hydrothermal reaction product is centrifuged and washed. and drying treatment.
(4)将上述处理后的水热反应产物转移到高温管式炉中,在氩气气氛下进行高温热解碳化处理,以5℃/min的升温速率升温到1300℃,保温3h,得到生物质基交联硬碳材料。(4) Transfer the hydrothermal reaction product after the above treatment to a high-temperature tube furnace, perform high-temperature pyrolysis carbonization treatment under an argon atmosphere, raise the temperature to 1300°C at a heating rate of 5°C/min, and keep it for 3 hours to obtain the product. Material-based cross-linked hard carbon materials.
以上所述仅为一种生物质基交联制备钠离子电池硬碳负极材料的方法优选实例,本发明的保护范围不仅限实例。本发明技术方案是在同等条件下对硬碳材料的制备条件进行改进和优化替代,再次基础上均为本发明的保护范围。The above is only a preferred example of a biomass-based cross-linking method for preparing hard carbon negative electrode materials for sodium ion batteries, and the scope of protection of the present invention is not limited to the examples. The technical solution of the present invention is to improve and optimize the preparation conditions of hard carbon materials under the same conditions, which again basically fall within the protection scope of the present invention.
应用及性能测试Application and performance testing
通过以上所述实施例和对比例所制备的硬碳材料做为钠离子电池负极活性物质制备极片,具体方法如下:将钠离子电池硬碳负极材料与导电剂乙炔黑、粘结剂羧甲基纤维素钠按照质量比8:1:1研磨成均匀的浆料,通过涂布器刮涂在铜箔上,保证活性物质面载量为1-1.5g/cm2,得到钠离子电池硬碳负极电极片,并在手套箱中制备钠离子扣式电池,并对扣式电池进行电化学性能检测。The hard carbon material prepared by the above-mentioned examples and comparative examples is used as the negative active material of the sodium ion battery to prepare the pole piece. The specific method is as follows: combine the hard carbon negative electrode material of the sodium ion battery with the conductive agent acetylene black and the binder carboxymethyl Grind sodium cellulose into a uniform slurry according to the mass ratio of 8:1:1, and apply it on the copper foil with an applicator to ensure that the active material surface loading is 1-1.5g/cm 2 to obtain a sodium ion battery hardener. Carbon negative electrode sheets were prepared, and sodium-ion button batteries were prepared in the glove box, and the electrochemical performance of the button batteries was tested.
表1为各实施例和对比例制备的钠离子电池硬碳负极材料电池性能,实施例与对比例相比较,具有较高的可逆容量与首周库伦效率,这是因为作为大分子的生物质基通过化学交联延长了分子链结构,可以在高温热解的过程中有效阻止小分子气体的释放,极小化硬碳表面缺陷的形成,促进了电子的转移,使其拥有出色的倍率性能。表2为实施例2不同电流密度(50-1000mA/g)的电化学性能,如表2所示,实施例2在500mA/g的电流密度下仍具有227mAh/g的可逆容量,在1000mA/g的电流密度下仍具有209mAh/g的可逆容量,显示本发明在大电流密度下的优异性。图1表明实施例2的扫描电镜图为无定形状,图2和图4表明本发明制备的电池拥有较长的平台区,图3为实施例2的倍率性能,表明本发明在不同电流密度下良好的循环稳定性。图5表明实施例2在较大电流密度(1A/g)下的长循环性能,即使在经过750圈后仍然保持80%的容量,证明了其优异的循环稳定性。Table 1 shows the battery performance of the sodium ion battery hard carbon negative electrode materials prepared in various examples and comparative examples. Compared with the comparative examples, the examples have higher reversible capacity and first-week Coulombic efficiency. This is because biomass as a macromolecule The base extends the molecular chain structure through chemical cross-linking, which can effectively prevent the release of small molecular gases during high-temperature pyrolysis, minimize the formation of hard carbon surface defects, and promote the transfer of electrons, giving it excellent rate performance . Table 2 shows the electrochemical properties of Example 2 at different current densities (50-1000mA/g). As shown in Table 2, Example 2 still has a reversible capacity of 227mAh/g at a current density of 500mA/g. It still has a reversible capacity of 209mAh/g at a current density of g, which shows the excellence of the present invention under high current density. Figure 1 shows that the scanning electron microscope image of Example 2 is amorphous. Figures 2 and 4 show that the battery prepared by the present invention has a longer plateau area. Figure 3 shows the rate performance of Example 2, indicating that the present invention operates at different current densities. Excellent cycling stability. Figure 5 shows the long cycle performance of Example 2 at a larger current density (1A/g). It still maintains 80% of the capacity even after 750 cycles, proving its excellent cycle stability.
表1实施例与对比例的电化学性能(电流密度50mAg-1)Table 1 Electrochemical properties of Examples and Comparative Examples (current density 50mAg -1 )
表2实施例2不同电流密度(50-1000mA/g)的电化学性能Table 2 Electrochemical properties of different current densities (50-1000mA/g) in Example 2
上对本发明的实施方式作出详细说明,但本发明不局限于所描述的实施方式。对本领域的技术人员而言,在不脱离本发明的原理和精神的情况下对这些实施例进行的多种变化、修改、替换和变型均仍落入在本发明的保护范围之内。The embodiments of the present invention are described in detail above, but the present invention is not limited to the described embodiments. For those skilled in the art, various changes, modifications, substitutions and modifications to these embodiments without departing from the principle and spirit of the invention will still fall within the protection scope of the invention.
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