CN1583550A - Preparing method for porous carbon with high specific surface area - Google Patents
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 title claims abstract description 27
- 239000011148 porous material Substances 0.000 claims abstract description 39
- 230000004913 activation Effects 0.000 claims abstract description 28
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000002994 raw material Substances 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000000376 reactant Substances 0.000 claims abstract description 3
- 239000011331 needle coke Substances 0.000 claims description 6
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 4
- 239000003830 anthracite Substances 0.000 claims description 4
- 239000002006 petroleum coke Substances 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 4
- 238000011282 treatment Methods 0.000 claims description 4
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 3
- 239000002802 bituminous coal Substances 0.000 claims description 3
- 239000004917 carbon fiber Substances 0.000 claims description 3
- 239000003077 lignite Substances 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims 1
- 239000011257 shell material Substances 0.000 claims 1
- 238000009826 distribution Methods 0.000 abstract description 2
- 238000001994 activation Methods 0.000 description 33
- 238000010438 heat treatment Methods 0.000 description 7
- 239000011261 inert gas Substances 0.000 description 7
- 238000005470 impregnation Methods 0.000 description 6
- 238000003763 carbonization Methods 0.000 description 4
- 239000007833 carbon precursor Substances 0.000 description 3
- 239000002010 green coke Substances 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 240000007049 Juglans regia Species 0.000 description 1
- 235000009496 Juglans regia Nutrition 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000003361 porogen Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920003987 resole Polymers 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 235000020234 walnut Nutrition 0.000 description 1
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Abstract
一种高比表面积中孔炭的制备方法是将KOH加水溶解至KOH完全溶解,其浓度为500g-1000gKOH/L水,按碱炭质量比为1~10∶1将微孔炭浸入KOH溶液中,在室温下浸渍1-48小时;将浸渍后的微孔炭在惰性气氛中以2-20℃的速率升到600℃-900℃,然后恒温反应10-150min,之后自然冷却;取出反应物,用水洗涤至无OH-检出。本发明具有KOH二次活化法原料来源丰富,工艺简单,成本低廉,用该方法制得的多孔炭中孔极为丰富,孔径分布窄,比表面积高的优点。A method for preparing mesoporous carbon with a high specific surface area is to dissolve KOH in water until the KOH is completely dissolved, the concentration of which is 500g-1000gKOH/L water, and immerse the microporous carbon in the KOH solution according to the alkali-carbon mass ratio of 1-10:1 , impregnated at room temperature for 1-48 hours; raise the impregnated microporous carbon to 600-900°C at a rate of 2-20°C in an inert atmosphere, then react at a constant temperature for 10-150min, and then cool naturally; take out the reactant , washed with water until no OH - was detected. The invention has the advantages of abundant raw material source, simple process and low cost in the KOH secondary activation method, and the porous carbon prepared by the method has extremely rich mesopores, narrow pore diameter distribution and high specific surface area.
Description
技术领域technical field
本发明属于一种多孔炭的制备方法,具体地说涉及一种高比表面积中孔炭的制备方法。The invention belongs to a method for preparing porous carbon, in particular to a method for preparing mesoporous carbon with high specific surface area.
背景技术Background technique
多孔炭由于其原料来源丰富、价格低廉,而被应用到环境、医学、能源等许多领域。然而不同的应用领域,对多孔炭的技术参数要求也不尽相同。作为超级电容器电极材料,微孔炭虽然有着超高的比表面积,但由于其孔径小(2nm以下)而不利于电解液的迅速渗透和自由出入,从而严重影响了超级电容器的功率特性,而且也使得相当一部分微孔得不到有效利用。为此需开发一种既具有高的比表面积又有丰富中孔的多孔炭的制备方法。Porous carbons have been applied in many fields, such as environment, medicine, energy, etc., due to their abundant raw material sources and low price. However, different application fields have different requirements for technical parameters of porous carbon. As a supercapacitor electrode material, although microporous carbon has an ultra-high specific surface area, its small pore size (below 2nm) is not conducive to the rapid penetration and free entry and exit of the electrolyte, which seriously affects the power characteristics of the supercapacitor. So that a considerable part of the micropores can not be effectively used. Therefore, it is necessary to develop a method for the preparation of porous carbons with both high specific surface area and abundant mesopores.
关于中孔炭的制备研究目前已有不少报道,其思路主要有三个方向:There have been many reports on the preparation of mesoporous carbons, and there are three main directions of thinking:
(1)原料直接活化法。如采用水蒸气活化、ZnCl2活化等所得中孔所占比例虽然较高,但其比表面积却不高(大多小于1000m2/g)。(1) Raw material direct activation method. For example, the proportion of mesopores obtained by steam activation and ZnCl 2 activation is relatively high, but the specific surface area is not high (mostly less than 1000m 2 /g).
(2)有机前躯体中加入致孔剂或催化剂再炭化活化。美国人加德卡埃和希克曼等人申请的题为《制造中孔炭的方法》的发明专利所用的方法是在高炭产率的炭前体可熔性酚醛树脂加入金属有机或无机化合物,经一系列处理后进行炭化、水蒸气活化,所得的中孔炭只有较低的比表面积(450-800m2/g)。(2) Add porogen or catalyst to the organic precursor and activate it by carbonization. The method used in the invention patent entitled "Method for Manufacturing Mesoporous Carbon" applied by Americans Gadkae and Hickman et al. is to add metal organic or inorganic compounds to the carbon precursor resole resin with high carbon yield , carbonization and steam activation after a series of treatments, the resulting mesoporous carbon has only a low specific surface area (450-800m 2 /g).
(3)在多孔分子筛模板上沉积有机原料,经炭化处理后再除去模板。典型的例子如韩国人吴承模等以无机模板(如硅石)与炭前体混合形成模板/炭前体复合材料,通过炭化处理后得到炭/模板材料,再除去模板后制得中孔炭。该中孔炭虽然可以控制孔径和形状,但其比表面积却不高,而且原料适应范围窄、工艺繁琐、成本较高。(3) Deposit organic raw materials on the porous molecular sieve template, and then remove the template after carbonization treatment. Typical examples, such as Korean Wu Chengmo, mixed inorganic templates (such as silica) and carbon precursors to form template/carbon precursor composite materials, obtained carbon/template materials after carbonization, and then obtained mesoporous carbon after removing the template. Although the mesoporous carbon can control the pore size and shape, its specific surface area is not high, and the raw material adaptability is narrow, the process is cumbersome, and the cost is high.
上述各类方法除了本身的缺憾之外(比如成本高、原料适用范围窄等等),都难以满足超级电容器所要求的高比表面积活性炭。In addition to the shortcomings of the above-mentioned methods (such as high cost, narrow application range of raw materials, etc.), it is difficult to meet the high specific surface area activated carbon required by supercapacitors.
发明内容Contents of the invention
本发明的目的就是提供一种既具有高的比表面积又具有丰富中孔的多孔炭的制备方法。The object of the present invention is to provide a method for preparing porous carbon with high specific surface area and abundant mesopores.
本发明它是以各种植物躯壳、无烟煤、烟煤、褐煤、石油焦、针状焦、炭纤维等为原料,经活化处理得到活性炭后,再以得到的活性炭为原料,用适量的KOH进行二次活化,其原理就在于KOH与炭反应时,可插入到C的层面中,撑开炭层从而制造微孔,这样可获得较高的比表面积。另外,KOH也可渗透到已有的微孔中,通过反应使部分微孔塌陷,从而制造出中孔。由于一次活化所得多孔炭孔隙率已很高,所以二次活化时不会有大量的新孔产生,此时的活化剂几乎全部用来扩孔。因此,得到多孔炭既具有高的比表面积、又具有丰富中孔。The present invention uses various plant shells, anthracite, bituminous coal, lignite, petroleum coke, needle coke, carbon fiber, etc. as raw materials. The principle of secondary activation is that when KOH reacts with carbon, it can be inserted into the C layer, and the carbon layer can be stretched to create micropores, so that a higher specific surface area can be obtained. In addition, KOH can also penetrate into the existing micropores and cause some micropores to collapse through the reaction, thereby creating mesopores. Since the porosity of the porous carbon obtained by the first activation is already very high, a large number of new pores will not be generated during the second activation, and almost all the activators at this time are used to expand the pores. Therefore, the obtained porous carbon has both high specific surface area and abundant mesopores.
本发明制备中孔炭的方法,其整个制备过程如下:The present invention prepares the method for mesoporous carbon, and its whole preparation process is as follows:
(1)将KOH加水溶解至KOH完全溶解(浓度为500g-1000gKOH/L水)按碱炭质量比为1~10∶1将微孔炭浸入KOH溶液中,在室温下浸渍1-48小时;(1) Dissolve KOH with water until KOH is completely dissolved (concentration is 500g-1000gKOH/L water). Immerse the microporous carbon in the KOH solution according to the alkali-carbon mass ratio of 1-10:1, and immerse at room temperature for 1-48 hours;
(2)将浸渍后的微孔炭在惰性气氛中以2-20℃的速率升到600-900℃,然后恒温反应10-150min,之后自然冷却;(2) Raise the impregnated microporous carbon to 600-900°C at a rate of 2-20°C in an inert atmosphere, then react at a constant temperature for 10-150min, and then cool naturally;
(3)取出反应物,用水洗涤至无OH-检出,干燥即得产品。(3) Take out the reactant, wash with water until no OH- is detected, and dry to obtain the product.
如上所述的微孔炭是以植物躯壳、无烟煤、烟煤、褐煤、石油焦、针状焦、或炭纤维等为原料,经活化处理得到,该活性炭的比表面积虽然达到2700-3500m2/g,但85%以上的孔孔径在2nm以下。The above-mentioned microporous carbon is obtained from plant shells, anthracite, bituminous coal, lignite, petroleum coke, needle coke, or carbon fiber through activation treatment. Although the specific surface area of the activated carbon reaches 2700-3500m 2 /g , but more than 85% of the pores have a diameter below 2nm.
而经过二次活化扩孔后,得到的多孔炭比表面积虽然有不同程度的下降,但其中孔却大幅增加,中孔孔容占总的孔容约65-85%。After secondary activation and pore expansion, although the specific surface area of the obtained porous carbon has decreased to varying degrees, the mesopores have increased significantly, and the mesopore volume accounts for about 65-85% of the total pore volume.
本发明具有如下优点The present invention has the following advantages
1、KOH二次活化法原料来源丰富,工艺简单,成本低廉;1. KOH secondary activation method has rich sources of raw materials, simple process and low cost;
2、用该方法制得的多孔炭中孔极为丰富,孔径分布窄,比表面积高。2. The porous carbon prepared by this method has extremely rich mesopores, narrow pore size distribution and high specific surface area.
具体实施方式Detailed ways
实施例1Example 1
将KOH加水溶解,以碱炭比5∶1的质量比取以石油焦为原料制备的活性炭(比表面积为3024m2,孔径≤2nm的微孔占总孔孔容的86%)浸入KOH溶液中,在室温下充分浸渍18h。然后将上述浸渍物转入活化炉中进行活化,升温速率为20℃/min,在900℃下活化0.5h,活化过程通惰性气体保护。所制备的活性炭的BET比表面积约2700m2,孔容为1.9cm3/g,中孔孔容占总孔孔容的70%。Dissolve KOH in water, take petroleum coke as raw material with the mass ratio of alkali-carbon ratio of 5:1 (the specific surface area is 3024m 2 , the micropores with pore diameter ≤ 2nm account for 86% of the total pore volume) and immerse in the KOH solution , fully soaked at room temperature for 18h. Then transfer the above-mentioned impregnation into an activation furnace for activation, the heating rate is 20°C/min, and it is activated at 900°C for 0.5h, and the activation process is protected by an inert gas. The BET specific surface area of the prepared activated carbon is about 2700m 2 , the pore volume is 1.9cm 3 /g, and the mesopore volume accounts for 70% of the total pore volume.
实施例2Example 2
以无烟煤细粉为原料所制备的活性炭(比表面积为2840m2,孔径≤2nm的微孔占总孔孔容的82%)与KOH以1∶8的质量比配料,方法同实施例1,在室温下浸渍6h。然后将上述浸渍物转入活化炉中进行活化,升温速率10℃/min,在800℃下活化1h,活化过程通惰性气体保护。所制备活性炭的BET比表面积约2580m2,孔容为1.8cm3/g,中孔孔容占总孔孔容的72%。Activated carbon (the specific surface area is 2840m 2 , and micropores with a pore diameter ≤ 2nm account for 82% of the total pore volume) prepared from anthracite fine powder as a raw material is mixed with KOH at a mass ratio of 1:8. The method is the same as in Example 1. Immerse at room temperature for 6h. Then transfer the above-mentioned impregnation into an activation furnace for activation, the heating rate is 10°C/min, and the activation is at 800°C for 1 hour, and the activation process is protected by an inert gas. The BET specific surface area of the prepared activated carbon is about 2580m 2 , the pore volume is 1.8cm 3 /g, and the mesopore volume accounts for 72% of the total pore volume.
实施例3Example 3
以粘胶基活性碳纤维(比表面积为2680m2,孔径≤2nm的微孔占总孔孔容的90%)为原料,与KOH以1∶1的质量比配料,方法同实施例1,在室温下浸渍48h。然后将上述浸渍物转入活化炉中进行活化,升温速率2℃/min,在600℃下活化1.5h,活化过程通惰性气体保护。所制备活性炭纤维的BET比表面积约1880m2,孔容为1.4cm3/g,中孔孔容占总孔孔容的68%。Viscose-based activated carbon fiber (with a specific surface area of 2680m 2 , and micropores with a pore diameter of ≤2nm accounting for 90% of the total pore volume) is used as a raw material, mixed with KOH at a mass ratio of 1:1, the method is the same as in Example 1, at room temperature Dipping for 48h. Then transfer the above-mentioned impregnation into an activation furnace for activation, the heating rate is 2°C/min, and it is activated at 600°C for 1.5h, and the activation process is protected by an inert gas. The BET specific surface area of the prepared activated carbon fiber is about 1880m 2 , the pore volume is 1.4cm 3 /g, and the mesopore volume accounts for 68% of the total pore volume.
实施例4Example 4
核桃壳为原料制备的活性炭(比表面积为3105m2,孔径≤2nm的微孔占总孔孔容的92%)与KOH按1∶6的质量比配料,方法同实施例1,在室温下浸渍24h。然后将上述浸渍物转入活化炉中进行活化,升温速率8℃/min,在750℃活化2.5h,活化过程通惰性气体保护。所制备活性炭的BET比表面积约2760m2,孔容为2.1cm3/g,中孔孔容占总孔孔容的83%。Activated carbon prepared from walnut shells (the specific surface area is 3105m 2 , and micropores with a pore diameter≤2nm account for 92% of the total pore volume) and KOH are mixed in a mass ratio of 1:6. The method is the same as in Example 1. 24h. Then transfer the impregnated material into the activation furnace for activation, the heating rate is 8°C/min, activate at 750°C for 2.5h, and the activation process is protected by inert gas. The BET specific surface area of the prepared activated carbon is about 2760m 2 , the pore volume is 2.1cm 3 /g, and the mesopore volume accounts for 83% of the total pore volume.
实施例5Example 5
以针状焦(生焦)为原料制备的活性炭(比表面积为3496m2,孔径≤2nm的微孔占总孔孔容的89%)与KOH按1∶1质量比配料,方法同实施例1,在室温下浸渍36h。然后将上述浸渍物转入活化炉中进行活化,升温速率15℃/min,在900℃下活化1h,活化过程通惰性气体保护。所制备的活性炭的BET比表面积约3010m2,孔容为2.4cm3/g,中孔孔容占总孔孔容的65%。Activated carbon prepared from needle coke (green coke) (with a specific surface area of 3496m 2 and micropores with a pore diameter of ≤2nm accounting for 89% of the total pore volume) was mixed with KOH at a mass ratio of 1:1, and the method was the same as in Example 1. , soaked at room temperature for 36h. Then transfer the above-mentioned impregnation into an activation furnace for activation at a heating rate of 15°C/min, and activate at 900°C for 1 hour, and the activation process is protected by an inert gas. The BET specific surface area of the prepared activated carbon is about 3010m 2 , the pore volume is 2.4cm 3 /g, and the mesopore volume accounts for 65% of the total pore volume.
实施例6Example 6
以针状焦(生焦)为原料制备的活性炭(比表面积为3293m2,孔径≤2nm的微孔占总孔孔容的88%)与KOH按1∶5质量比配料,方法同实施例1,在室温下浸渍24h。然后将上述浸渍物转入活化炉中进行活化,升温速率5℃/min,在800℃下活化1.5h,活化过程通惰性气体保护。所制备的活性炭的BET比表面积约2800m2,孔容为2.2cm3/g,中孔孔容占总孔孔容的81%。Activated carbon prepared from needle coke (green coke) (with a specific surface area of 3293m 2 and micropores with a pore diameter of ≤2nm accounting for 88% of the total pore volume) was mixed with KOH at a mass ratio of 1:5, and the method was the same as in Example 1. , soaked at room temperature for 24h. Then transfer the above-mentioned impregnation into an activation furnace for activation, the heating rate is 5°C/min, and the activation is at 800°C for 1.5h, and the activation process is protected by an inert gas. The BET specific surface area of the prepared activated carbon is about 2800m 2 , the pore volume is 2.2cm 3 /g, and the mesopore volume accounts for 81% of the total pore volume.
实施例7Example 7
以针状焦(生焦)为原料制备的活性炭(比表面积为2751m2,孔径≤2nm的微孔占总孔孔容的81%)与KOH按1∶10质量比配料,方法同实施例1,在室温下浸渍1h。然后将上述浸渍物转入活化炉中进行活化,升温速率10℃/min,在850℃活化2h,活化过程通惰性气体保护。所制备活性炭的BET比表面积约2350m2,孔容为1.6cm3/g,中孔孔容占总孔孔容的83%。Activated carbon prepared from needle coke (green coke) (with a specific surface area of 2751 m 2 , micropores with a pore diameter of ≤2 nm accounting for 81% of the total pore volume) and KOH are mixed in a mass ratio of 1:10, and the method is the same as in Example 1. , soaked at room temperature for 1h. Then transfer the above-mentioned impregnation into an activation furnace for activation, the heating rate is 10°C/min, activate at 850°C for 2h, and the activation process is protected by inert gas. The BET specific surface area of the prepared activated carbon is about 2350m 2 , the pore volume is 1.6cm 3 /g, and the mesopore volume accounts for 83% of the total pore volume.
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Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
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CN100528747C (en) * | 2007-02-07 | 2009-08-19 | 中国科学院山西煤炭化学研究所 | Method for preparing medium pore carbon of narrow aperture and high degree of graphitization |
CN101948106A (en) * | 2010-09-28 | 2011-01-19 | 华东理工大学 | Preparation method of blocky porous carbon with high specific surface area |
CN101475168B (en) * | 2009-01-19 | 2011-04-20 | 中国科学院山西煤炭化学研究所 | Method for washing active carbon |
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