CN112209375B - Purification method of graphitized carbon - Google Patents
Purification method of graphitized carbon Download PDFInfo
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 67
- 238000000034 method Methods 0.000 title claims abstract description 19
- 238000000746 purification Methods 0.000 title abstract description 5
- 239000002253 acid Substances 0.000 claims abstract description 33
- 239000002131 composite material Substances 0.000 claims abstract description 25
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 23
- 229910003481 amorphous carbon Inorganic materials 0.000 claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 238000004140 cleaning Methods 0.000 claims abstract description 9
- 238000005530 etching Methods 0.000 claims abstract description 6
- 238000002791 soaking Methods 0.000 claims abstract description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 17
- 229910017604 nitric acid Inorganic materials 0.000 claims description 17
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 7
- 239000012153 distilled water Substances 0.000 claims description 7
- 125000000524 functional group Chemical group 0.000 claims description 7
- 239000007789 gas Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 229910052786 argon Inorganic materials 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 5
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 238000005516 engineering process Methods 0.000 abstract description 4
- 239000013014 purified material Substances 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- 150000002500 ions Chemical class 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 238000001179 sorption measurement Methods 0.000 description 6
- 229920000049 Carbon (fiber) Polymers 0.000 description 5
- 239000004917 carbon fiber Substances 0.000 description 5
- 229910002804 graphite Inorganic materials 0.000 description 5
- 239000010439 graphite Substances 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- NPYPAHLBTDXSSS-UHFFFAOYSA-N Potassium ion Chemical compound [K+] NPYPAHLBTDXSSS-UHFFFAOYSA-N 0.000 description 4
- 239000003990 capacitor Substances 0.000 description 4
- 229910001385 heavy metal Inorganic materials 0.000 description 4
- 238000001027 hydrothermal synthesis Methods 0.000 description 4
- 239000002086 nanomaterial Substances 0.000 description 4
- 229910001414 potassium ion Inorganic materials 0.000 description 4
- 229940037179 potassium ion Drugs 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 3
- 239000002134 carbon nanofiber Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 229910001416 lithium ion Inorganic materials 0.000 description 3
- 238000011056 performance test Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 238000005087 graphitization Methods 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 229910001415 sodium ion Inorganic materials 0.000 description 2
- 229910013870 LiPF 6 Inorganic materials 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000002194 amorphous carbon material Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001523 electrospinning Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000013538 functional additive Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007773 negative electrode material Substances 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000002195 soluble material Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/20—Graphite
- C01B32/21—After-treatment
- C01B32/215—Purification; Recovery or purification of graphite formed in iron making, e.g. kish graphite
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- General Life Sciences & Earth Sciences (AREA)
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Abstract
本发明涉及一种石墨化碳提纯方法。该方法包括如下步骤:1)配置浓度为0.5~10 mol/L的酸溶液;2)复合碳浸泡在酸溶液中得复合碳/酸溶液,其中复合碳占酸溶液重量的1~80%;3)将所得的复合碳/酸溶液在高温高压下进行反应,通过酸选择性刻蚀复合碳进而去除留在复合碳中的无定型碳,得到石墨化碳;4)将获得的石墨化碳先后进行清洗和热处理,获得纯石墨化碳材料。本发明具有以下有益效果:提纯技术具有高效、快速、选择性高等优点,且不受提纯材料形貌的约束;本发明方法制备的石墨化碳材料具有广泛的应用。The invention relates to a method for purifying graphitized carbon. The method includes the following steps: 1) preparing an acid solution with a concentration of 0.5-10 mol/L; 2) soaking the composite carbon in the acid solution to obtain a composite carbon/acid solution, wherein the composite carbon accounts for 1-80% of the weight of the acid solution; 3) The obtained composite carbon/acid solution is reacted under high temperature and high pressure, and the amorphous carbon left in the composite carbon is removed by selective etching of the composite carbon by acid to obtain graphitized carbon; 4) The obtained graphitized carbon is obtained Cleaning and heat treatment are successively performed to obtain pure graphitized carbon materials. The invention has the following beneficial effects: the purification technology has the advantages of high efficiency, rapidity, high selectivity, and is not restricted by the morphology of the purified material; the graphitized carbon material prepared by the method of the invention has a wide range of applications.
Description
技术领域technical field
本发明涉及一种石墨化碳提纯方法,更具体地说,涉及一种酸选择性刻蚀无定型碳提纯石墨化碳材料方法。The invention relates to a method for purifying graphitized carbon, in particular to a method for purifying graphitized carbon material by acid selective etching of amorphous carbon.
背景技术Background technique
石墨化碳材料由于其独特的结构和物理化学特性在电子器件、传感器、能源储存等领域引发关注。模板法、静电纺丝技术等技术能够将材料纳米化,已广泛用于制备有序介孔碳、碳纳米纤维、碳纳米管等功能材料。例如,在700度高温煅烧电纺聚丙烯腈可得到碳纳米纤维,但是得到的碳为无定型碳材料。催化剂(镍,钴,铁等)可催化无定型碳转化为石墨化碳,获得石墨化碳。但这些催化剂有效催化范围为周围5纳米左右的无定型碳,催化范围有限,催化能力固定,最终只能获得无定型碳和石墨化碳的复合材料。由于无定型碳的存在,减低了碳材料的导电率等,影响了碳材料的应用。因此开发一种简易、成本低廉的石墨化碳提纯方法是众多科研工作者倾力攻克的难题。Graphitized carbon materials have attracted attention in the fields of electronic devices, sensors, and energy storage due to their unique structural and physicochemical properties. Techniques such as template method and electrospinning technology can nanosize materials and have been widely used to prepare functional materials such as ordered mesoporous carbon, carbon nanofibers, and carbon nanotubes. For example, carbon nanofibers can be obtained by calcining electrospun polyacrylonitrile at a high temperature of 700 degrees, but the obtained carbon is an amorphous carbon material. Catalysts (nickel, cobalt, iron, etc.) can catalyze the transformation of amorphous carbon into graphitized carbon to obtain graphitized carbon. However, the effective catalytic range of these catalysts is about 5 nanometers around amorphous carbon, the catalytic range is limited, and the catalytic ability is fixed, and finally only a composite material of amorphous carbon and graphitized carbon can be obtained. Due to the existence of amorphous carbon, the electrical conductivity of carbon materials is reduced, which affects the application of carbon materials. Therefore, the development of a simple and low-cost method for purifying graphitized carbon is a difficult problem for many scientific researchers to overcome.
发明内容SUMMARY OF THE INVENTION
本发明要解决的技术问题在于,针对现有留在石墨化碳中的无定型碳分离困难的问题,提供一种成本低廉的石墨化碳提纯方法及其应用,用此方法可选择性地将无定型碳从石墨化碳中去除,最终获得纯石墨化碳,制备的石墨化碳材料在能源储存、环境处理、功能塑料等领域表现出优异的性能。The technical problem to be solved by the present invention is to provide a low-cost method for purifying graphitized carbon and its application in view of the difficulty of separating the amorphous carbon left in the graphitized carbon. Amorphous carbon is removed from graphitized carbon, and finally pure graphitized carbon is obtained. The prepared graphitized carbon material exhibits excellent performance in the fields of energy storage, environmental treatment, and functional plastics.
为实现本发明的目的采用技术方案如下:本发明提供了一种石墨化碳提纯的方法,依序包括如下步骤:For realizing the purpose of the present invention, the technical scheme is adopted as follows: the present invention provides a method for purifying graphitized carbon, which comprises the following steps in sequence:
(1)配置酸溶液:配置浓度为0.5~10 mol/L的酸溶液;(1) Prepare an acid solution: configure an acid solution with a concentration of 0.5 to 10 mol/L;
(2)碳材料与酸复配:将复合碳浸泡在步骤(1)配置的酸溶液中得复合碳/酸溶液,其中复合碳占酸溶液重量的1~80%;(2) Compounding of carbon material and acid: soaking the compound carbon in the acid solution prepared in step (1) to obtain a compound carbon/acid solution, wherein the compound carbon accounts for 1-80% of the weight of the acid solution;
(3)高温高压处理:将步骤(2)所得复合碳/酸溶液在高温高压下进行反应,通过酸选择性刻蚀复合碳进而去除留在复合碳中的无定型碳,得到石墨化碳;(3) high temperature and high pressure treatment: react the composite carbon/acid solution obtained in step (2) under high temperature and high pressure, and selectively etch the composite carbon by acid to remove the amorphous carbon left in the composite carbon to obtain graphitized carbon;
(4)清洗和热处理:将步骤(3)获得的石墨化碳先后进行清洗和热处理除去石墨化碳表面的氧化功能基团,从而获得纯石墨化碳材料。(4) Cleaning and heat treatment: The graphitized carbon obtained in step (3) is cleaned and heat treated successively to remove the oxidized functional groups on the surface of the graphitized carbon, thereby obtaining a pure graphitized carbon material.
获得石墨化碳材料,1)可直接用作锂离子电池负极、钠离子电池负极、钾离子电池负极或超级电容器电极,电池电极可逆容量为100~1500 mAh/g;所述超级电容器的可逆容量为50~200 F/g;2)一种功能助剂,增强塑料电学功能,获得优异电磁屏蔽性能;3)一种吸附剂,制得的石墨化碳材料对废水中的重金属离子具有良好的吸附效果,其中,对铅离子的吸附容量可到50 mg/g,对Hg(2+)吸附量可达到600 mg/g等。To obtain the graphitized carbon material, 1) it can be directly used as negative electrode of lithium ion battery, negative electrode of sodium ion battery, negative electrode of potassium ion battery or electrode of super capacitor, and the reversible capacity of battery electrode is 100-1500 mAh/g; the reversible capacity of said super capacitor 50-200 F/g; 2) a functional additive to enhance the electrical function of plastics and obtain excellent electromagnetic shielding performance; 3) an adsorbent, the prepared graphitized carbon material has good properties for heavy metal ions in wastewater. Among them, the adsorption capacity of lead ions can reach 50 mg/g, and the adsorption capacity of Hg(2+) can reach 600 mg/g.
步骤(1)中所述酸溶液是指硝酸、盐酸或硫酸的混合酸,其中硝酸、盐酸和硫酸的摩尔比为:9~10:0~0.5:0~0.5。The acid solution in step (1) refers to a mixed acid of nitric acid, hydrochloric acid or sulfuric acid, wherein the molar ratio of nitric acid, hydrochloric acid and sulfuric acid is: 9-10:0-0.5:0-0.5.
步骤(2)中所述的复合碳是指由无特定形貌,无特定大小尺寸的无定型碳和石墨化碳组成的任何碳材料。The composite carbon described in step (2) refers to any carbon material composed of amorphous carbon and graphitized carbon with no specific morphology and no specific size.
步骤(2)中所述的复合碳中也可含有其它可溶于酸的金属或氧化物,通过提纯过程可在提纯石墨化碳材料中引入孔性结构。The composite carbon described in step (2) may also contain other acid-soluble metals or oxides, and a porous structure can be introduced into the purified graphitized carbon material through the purification process.
步骤(3)中所述的高温高压处理,温度为120~300℃,压力为1~100 MPa,处理时间为1~20h。In the high temperature and high pressure treatment described in step (3), the temperature is 120-300° C., the pressure is 1-100 MPa, and the treatment time is 1-20 h.
步骤(4)中所述的清洗是指用蒸馏水和95%酒精顺序清洗,清洗至pH值 在6.5~7.0之间。The cleaning described in step (4) refers to sequentially cleaning with distilled water and 95% alcohol until the pH value is between 6.5 and 7.0.
步骤(4)中所述的热处理,热处理温度在500~1000℃之间,热处理时间为0.5~1h,热处理过程边通氢气/氩气,或氢气/氮气还原气体,边抽真空至真空度在-100~-1000torr。For the heat treatment described in step (4), the heat treatment temperature is between 500 and 1000°C, and the heat treatment time is 0.5 to 1 h. During the heat treatment, hydrogen/argon gas or hydrogen/nitrogen reducing gas is passed through, and the vacuum is evacuated until the vacuum degree is between -100~-1000torr.
本发明具有以下有益效果:The present invention has the following beneficial effects:
(1)本发明提纯技术具有高效、快速、选择性高等优点,获得的碳材料石墨化纯度高、导电率高、可循环使用,结构稳定,抵抗外界破坏能力强。(1) The purification technology of the present invention has the advantages of high efficiency, rapidity and high selectivity, and the obtained carbon material has high graphitization purity, high electrical conductivity, can be recycled, has stable structure and strong resistance to external damage.
(2)本发明报道的一种提纯石墨化碳方法,不受提纯材料形貌的约束,不受提纯材料尺度大小的影响,最终所得到的石墨化碳材料其形貌可以是零维颗粒,一维纤维或二维薄膜等等,石墨化纯度高。如提纯材料中含有可溶于酸的材料,通过提纯过程可在材料中引入多孔结构。(2) A method for purifying graphitized carbon reported in the present invention is not restricted by the morphology of the purified material, and is not affected by the size of the purified material, and the morphology of the finally obtained graphitized carbon material can be zero-dimensional particles, One-dimensional fibers or two-dimensional films, etc., have high graphitization purity. If the purified material contains an acid-soluble material, a porous structure can be introduced into the material through the purification process.
(3)本发明方法制备的石墨化碳材料具有广泛的应用,直接作为电极组装锂离子电池、钠离子电池、钾离子电池或超级电容器等具有能量密度高、稳定性好、寿命长等优点;可作为填充剂,增强塑料电学功能,获得优异电磁屏蔽性能;直接作为吸附剂,对废水中的重金属离子具有良好的吸附效果。(3) The graphitized carbon material prepared by the method of the present invention has a wide range of applications, Assembling lithium-ion batteries, sodium-ion batteries, potassium-ion batteries or supercapacitors directly as electrodes has the advantages of high energy density, good stability and long life; It can be used as a filler to enhance the electrical function of plastics and obtain excellent electromagnetic shielding performance; As an adsorbent directly, it has a good adsorption effect on heavy metal ions in wastewater.
(4)本发明一种提纯石墨碳的方法,技术简单,操作容易,可大量制备。(4) The method for purifying graphitic carbon of the present invention is simple in technology, easy in operation, and can be prepared in large quantities.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合实施例,对本发明进行进一步详细说明。In order to make the objectives, technical solutions and advantages of the present invention clearer, the present invention will be further described in detail below with reference to the embodiments.
本发明是根据特定实施例进行描述的,但本领域的技术人员应明白在不脱离本发明范围时,可进行各种变化和等同替换。此外,为适应本发明技术的特定场合或材料,可对本发明进行诸多修改而不脱离其保护范围。因此,本发明并不限于在此公开的特定实施例,而包括所有落入到权利要求保护范围的实施例。The present invention has been described in terms of specific embodiments, but it will be understood by those skilled in the art that various changes and equivalents may be made without departing from the scope of the invention. In addition, many modifications may be made to adapt the present invention to a particular situation or material to which it is intended without departing from its scope. Therefore, the present invention is not limited to the specific embodiments disclosed herein, but includes all embodiments falling within the scope of the claims.
实施例1Example 1
1、将浓硝酸稀释配置4 mol/L硝酸溶液;1. Dilute concentrated nitric acid to prepare 4 mol/L nitric acid solution;
2、将10 mg一维复合碳纤维浸泡在25 mL 4 mol/L硝酸溶液中;2. Soak 10 mg of one-dimensional composite carbon fiber in 25 mL of 4 mol/L nitric acid solution;
3、将上述步骤2溶液转移到50 mL水热反应釜在170 ℃温度下,反应15 h,待反应釜冷却过滤获得一维石墨碳纤维;3. Transfer the solution of the above step 2 to a 50 mL hydrothermal reaction kettle at a temperature of 170 °C, and react for 15 h. After the reaction kettle is cooled and filtered to obtain one-dimensional graphite carbon fibers;
4、将获得的一维石墨碳纤维用蒸馏水和95%酒精顺序清洗3次,清洗后pH值为6.5,烘干;4. Wash the obtained one-dimensional graphite carbon fiber with distilled water and 95% alcohol for 3 times in sequence, after washing, the pH value is 6.5, and dry;
5、将烘干后的一维石墨碳纤维在边通氢气/氩气混合气体边抽真空至真空度-100torr条件下500 ℃热处理30 min,去除氧化官能团;5. Heat treatment at 500 °C for 30 min under the condition of vacuum degree -100torr while passing hydrogen/argon mixed gas through the dried one-dimensional graphite carbon fiber to remove the oxidized functional groups;
6、按常规方法制备锂离子电极:以制备的上述石墨碳纤维为工作电极,锂片为对电极,Celgard 2400为隔膜,以1mol/L LiPF6 in EC: DMC: EMC (1:1:1体积比)为电解液,制备成扣式电池。测试电压范围为0~3V。当电流密度为50 mA/g进行充放电性能测试时,质量比容量为900 mAh/g。6. Prepare a lithium ion electrode by a conventional method: take the prepared above-mentioned graphite carbon fiber as the working electrode, the lithium sheet as the counter electrode, and Celgard 2400 as the separator, with 1mol/L LiPF 6 in EC: DMC: EMC (1:1:1 volume) ratio) is the electrolyte, and is prepared into a button battery. The test voltage range is 0~3V. When the current density was 50 mA/g for the charge-discharge performance test, the mass specific capacity was 900 mAh/g.
实施例2Example 2
1、将浓硝酸稀释配置6 mol/L硝酸溶液;1. Dilute concentrated nitric acid to prepare 6 mol/L nitric acid solution;
2、将10 mg 嵌有镍颗粒的复合碳纳米纤维浸泡在20 mL 6 mol/L硝酸溶液中;2. Soak 10 mg of composite carbon nanofibers embedded with nickel particles in 20 mL of 6 mol/L nitric acid solution;
3、将上述步骤2溶液转移到50 mL水热反应釜在150 ℃温度下,反应12 h,待反应釜冷却过滤获得空心碳纳米材料;3. Transfer the solution of the above step 2 to a 50 mL hydrothermal reaction kettle at a temperature of 150 °C, and react for 12 h. After the reaction kettle is cooled and filtered to obtain hollow carbon nanomaterials;
4、将获得的空心碳纳米材料用蒸馏水和95%酒精顺序清洗3次,清洗后pH值 为6.8,烘干;4. The hollow carbon nanomaterials obtained were sequentially cleaned 3 times with distilled water and 95% alcohol, and the pH value after cleaning was 6.8, and dried;
5、将烘干后的空心石墨化碳纳米材料边通氢气/氮气混合气体边抽真空至真空度-200 torr条件下600 ℃热处理30 min去除氧化官能团;5. The dried hollow graphitized carbon nanomaterials are evacuated to a vacuum degree of -200 torr while being passed through a hydrogen/nitrogen gas mixture, and then heat-treated at 600 °C for 30 min to remove the oxidized functional groups;
6、按常规方法制备电容器电极:以制备的上述空心石墨化碳纳米材料为工作电极,Pt为对电极,Hg/HgO电极为参比电极组成三电极系统,并将其浸泡在2 mol/L N2SO4或KOH的电解液中,组装成电容器单元。测试电压范围为0~0.9V。当电流密度为500 mA/g进行充分电性能测试时,比电容值为85 F/g。6. Prepare capacitor electrodes by conventional methods: use the prepared hollow graphitized carbon nanomaterials as the working electrode, Pt as the counter electrode, and Hg/HgO electrode as the reference electrode to form a three-electrode system, and soak it in 2 mol/LN 2 SO 4 or KOH electrolyte, assembled into capacitor units. The test voltage range is 0~0.9V. When the current density is 500 mA/g for the full electrical performance test, the specific capacitance value is 85 F/g.
实施例3Example 3
1、将浓硝酸稀释配置7 mol/L混合酸,其中硝酸比盐酸摩尔比9.5:0.5;1. Dilute concentrated nitric acid to prepare 7 mol/L mixed acid, wherein the molar ratio of nitric acid to hydrochloric acid is 9.5:0.5;
2、将10 mg二维复合碳膜浸泡在25 mL 7 mol/L混酸溶液中;2. Soak 10 mg of two-dimensional composite carbon film in 25 mL of 7 mol/L mixed acid solution;
3、将上述步骤2溶液转移到50 mL水热反应釜在180 ℃温度下,反应10 h,待反应釜冷却过滤获得二维超薄石墨化碳膜;3. Transfer the solution of the above step 2 to a 50 mL hydrothermal reaction kettle at a temperature of 180 °C for 10 h. After the reaction kettle is cooled and filtered to obtain a two-dimensional ultra-thin graphitized carbon film;
4、将获得的二维超薄石墨化碳膜用蒸馏水和95 %酒精顺序清洗3次,清洗后pH值为6.5,烘干;4. The obtained two-dimensional ultra-thin graphitized carbon film is sequentially cleaned 3 times with distilled water and 95% alcohol, and the pH value is 6.5 after cleaning, and dried;
5、将烘干后的二维超薄石墨化碳膜在边通氢气/氩气混合气体边抽真空至真空度-300 torr条件下在700 ℃热处理30 min去除杂质官能团;5. The dried two-dimensional ultra-thin graphitized carbon film was evacuated to a vacuum degree of -300 torr while passing hydrogen/argon mixed gas, and heat-treated at 700 °C for 30 min to remove impurity functional groups;
6、将所制备的材料放入含有重金属离子的废水中,所制备二维超薄石墨化碳膜对废水中的重金属离子具有良好的吸附效果,其中,对铅离子的吸附容量可到50 mg/g,对Hg(2+)吸附量可达到500 mg/g。6. Put the prepared material into wastewater containing heavy metal ions, and the prepared two-dimensional ultrathin graphitized carbon film has a good adsorption effect on heavy metal ions in wastewater, among which, the adsorption capacity of lead ions can reach 50 mg /g, the adsorption capacity of Hg(2+) can reach 500 mg/g.
实施例4Example 4
1、将浓硝酸稀释配置5 mol/L混合酸,其中硝酸、盐酸、硫酸摩尔比为9:0.5:0.5;1. Dilute concentrated nitric acid to prepare 5 mol/L mixed acid, wherein the molar ratio of nitric acid, hydrochloric acid and sulfuric acid is 9:0.5:0.5;
2、将20 mg复合碳颗粒浸泡在20 mL 5 mol/L混合酸溶液中;2. Soak 20 mg of composite carbon particles in 20 mL of 5 mol/L mixed acid solution;
3、将上述步骤2溶液转移到50 mL水热反应釜在160 ℃温度下,反应10 h,待反应釜冷却过滤获得石墨化碳颗粒;3. Transfer the solution of the above step 2 to a 50 mL hydrothermal reaction kettle at a temperature of 160 °C, and react for 10 h. After the reaction kettle is cooled and filtered, graphitized carbon particles are obtained;
4、将获得的石墨化碳材料用蒸馏水和95 %酒精顺序清洗3次,并烘干;4. The obtained graphitized carbon material is sequentially washed 3 times with distilled water and 95% alcohol, and dried;
5、将烘干后的墨化碳颗粒在边通氢气/氩气混合气体边抽真空至真空度-500torr条件下在1000 ℃热处理1h除去杂质官能团;5. The dried graphite carbon particles are evacuated to a vacuum degree of -500torr while passing hydrogen/argon mixed gas, and heat treatment at 1000 ℃ for 1h to remove impurity functional groups;
6、制备的墨化碳颗粒材料作为钾离子电池负极材料,按常规方法制备钾离子电极:以制备的石墨化碳为工作电极,钾片为对电极,玻璃纤维为隔膜,以1M KPF6 in DME=100 Vol%为电解液,组装扣式电池。测试电压范围为0~3V。当电流密度为0.1 C进行充分电性能测试时,质量比容量为250 mAh/g。6. The prepared graphitized carbon particle material is used as the negative electrode material of the potassium ion battery, and the potassium ion electrode is prepared according to the conventional method: the prepared graphitized carbon is used as the working electrode, the potassium sheet is used as the counter electrode, the glass fiber is used as the diaphragm, and 1M KPF 6 in DME=100 Vol% is the electrolyte, and the button battery is assembled. The test voltage range is 0~3V. When the current density is 0.1 C for the full electrical performance test, the mass specific capacity is 250 mAh/g.
实施例5Example 5
1、将浓硝酸稀释配置6 mol/L硝酸溶液;1. Dilute concentrated nitric acid to prepare 6 mol/L nitric acid solution;
2、将10 mg二维复合碳膜浸泡在20 mL 6 mol/L硝酸溶液中;2. Soak 10 mg of two-dimensional composite carbon film in 20 mL of 6 mol/L nitric acid solution;
3、将上述步骤2溶液转移到50 mL水热反应釜在200 ℃温度下,反应8 h,待反应釜冷却过滤获得二维石墨化碳膜;3. Transfer the solution of the above step 2 to a 50 mL hydrothermal reactor at 200 °C for 8 h, and then the reactor is cooled and filtered to obtain a two-dimensional graphitized carbon film;
4、将获得的二维石墨化碳膜用蒸馏水和95 %酒精顺序清洗3次,并烘干;4. The obtained two-dimensional graphitized carbon film is sequentially cleaned 3 times with distilled water and 95% alcohol, and dried;
5、将烘干后的二维石墨化碳膜在边通氢气/氩气混合气体边抽真空至真空度-300torr条件下1000 ℃热处理1h除去杂质官能团;5. The two-dimensional graphitized carbon film after drying is evacuated to a vacuum degree of -300torr and heat-treated at 1000 ℃ for 1h while passing hydrogen/argon mixed gas to remove impurity functional groups;
6、制得的二维石墨化碳作为添加剂,添加10-15%石墨化碳跟塑料一起共混,获得的塑料电磁屏蔽性能在20-50 dB。6. The obtained two-dimensional graphitized carbon is used as an additive, and 10-15% graphitized carbon is added to blend together with the plastic, and the electromagnetic shielding performance of the plastic obtained is 20-50 dB.
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