CN1402273A - Process for preparing high specific capacitance electrode material - Google Patents
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- 239000007772 electrode material Substances 0.000 title claims abstract description 27
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 79
- 239000000203 mixture Substances 0.000 claims abstract description 23
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000004964 aerogel Substances 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 12
- 239000005011 phenolic resin Substances 0.000 claims abstract description 10
- 229920001568 phenolic resin Polymers 0.000 claims abstract description 10
- 238000002360 preparation method Methods 0.000 claims abstract description 7
- 239000011230 binding agent Substances 0.000 claims abstract description 5
- 239000002994 raw material Substances 0.000 claims abstract description 5
- 239000002006 petroleum coke Substances 0.000 claims abstract description 4
- 239000012190 activator Substances 0.000 claims abstract description 3
- 239000011334 petroleum pitch coke Substances 0.000 claims abstract description 3
- 239000000839 emulsion Substances 0.000 claims description 8
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 8
- 239000004966 Carbon aerogel Substances 0.000 abstract description 25
- 239000003990 capacitor Substances 0.000 abstract description 19
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 abstract description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 10
- 239000003054 catalyst Substances 0.000 abstract description 10
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 abstract description 9
- 239000003208 petroleum Substances 0.000 abstract description 9
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 abstract description 9
- 238000005516 engineering process Methods 0.000 abstract description 3
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 abstract 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 description 14
- 239000002245 particle Substances 0.000 description 10
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 8
- -1 polytetrafluoroethylene Polymers 0.000 description 7
- 239000004810 polytetrafluoroethylene Substances 0.000 description 7
- 238000003756 stirring Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 239000004020 conductor Substances 0.000 description 4
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 3
- 229920000049 Carbon (fiber) Polymers 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000002041 carbon nanotube Substances 0.000 description 2
- 229910021393 carbon nanotube Inorganic materials 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 235000015842 Hesperis Nutrition 0.000 description 1
- 235000012633 Iberis amara Nutrition 0.000 description 1
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
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- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 230000006386 memory function Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052987 metal hydride Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- RCHKEJKUUXXBSM-UHFFFAOYSA-N n-benzyl-2-(3-formylindol-1-yl)acetamide Chemical compound C12=CC=CC=C2C(C=O)=CN1CC(=O)NCC1=CC=CC=C1 RCHKEJKUUXXBSM-UHFFFAOYSA-N 0.000 description 1
- 239000007783 nanoporous material Substances 0.000 description 1
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- 238000012827 research and development Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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Abstract
本发明提供了一种制备高比电容电极材料的方法。该方法是以石油焦或沥青焦为原料、KOH为活化剂制备高比表面积粉状活性炭,以及用酚醛树脂、糠醛按重量比1∶1.2~1.8的比例配成7~15g/100ml浓度的丙醇溶液,催化剂用量为7~15mmol/ml,在60~100℃下反应4~7天形成醇凝胶,在250~300℃、6~8MPa超临界石油醚中干燥1-3小时形成酚醛气凝胶,将该气凝胶在600~1000℃炭化1-3小时产生碳气凝胶;将二者以1∶0.05~1(重量比)的比例混合,加入2-10%粘结剂,混合均匀制得高比电容电极材料。该方法制得的电极材料(AC∶A=1∶0.2)在常温下比电容高达330F/g。该电极材料具有制备方法简单,比电容高、导电性好等优点,为双电层电容器技术的大规模应用提供了良好的前景。The invention provides a method for preparing high specific capacitance electrode material. The method uses petroleum coke or pitch coke as raw material and KOH as activator to prepare powdered activated carbon with high specific surface area, and uses phenolic resin and furfural to prepare acrylic acid with a concentration of 7 to 15g/100ml in a weight ratio of 1:1.2 to 1.8. Alcohol solution, the amount of catalyst is 7-15mmol/ml, react at 60-100°C for 4-7 days to form alcohol gel, dry in 250-300°C, 6-8MPa supercritical petroleum ether for 1-3 hours to form phenolic gas Gel, the aerogel is carbonized at 600-1000°C for 1-3 hours to produce carbon aerogel; the two are mixed in a ratio of 1:0.05-1 (weight ratio), and 2-10% binder is added, Mix evenly to prepare high specific capacitance electrode material. The specific capacitance of the electrode material (AC:A=1:0.2) prepared by the method is as high as 330F/g at normal temperature. The electrode material has the advantages of simple preparation method, high specific capacitance, good conductivity, etc., and provides good prospects for large-scale application of electric double layer capacitor technology.
Description
所属领域:Field:
本发明属于一种双电层电容器用高比电容电极材料的制备方法。具体涉及一种以高比表面积活性炭和碳气凝胶为原料制备双电层电容器电极材料的方法。The invention belongs to a preparation method of a high specific capacitance electrode material for an electric double layer capacitor. In particular, it relates to a method for preparing electrode materials of electric double layer capacitors by using activated carbon with high specific surface area and carbon aerogel as raw materials.
背景技术:Background technique:
双电层电容器是一种新型储能器件,是利用在电极和电解液界面上形成的双电层制成的,具有法拉级电容量和电压记忆功能等特点,其功率密度远高于普通电池,能量密度远高于传统电容,因而填补了这两个传统技术间的空白。双电层电容器在军用、民用均有着很广泛的应用前景。小电流放电的双电层电容器可作微机等的备用电源或小型装置如玩具、报警器、信号灯等的一次电源;安培级大电流放电双电层电容器可单独或与蓄电池一起构成电源系统,既可作起动电源且可作小型负载的驱动电源,如用于坦克、飞机、火箭、导弹等做起动电源等。双电层电容器比传统的可充电电池(包括镍氢电池和锂离子电池)具有更高的比功率和更长的循环寿命,其比功率达到每公斤千瓦数量级以上,循环寿命在万次以上(使用年限5年以上)。大功率双电层电容器对于电动汽车的启动、加速和上坡行驶具有特别重要的意义;对于电动汽车的电池能量系统的管理,延长电池的循环寿命和最优化使用,以及燃料电池电动汽车的启动更是必不可少的。鉴于双电层电容器的重要性,各工业发达国家都给予了高度的重视,并作为国家重点的战略研究和开发项目。The electric double layer capacitor is a new type of energy storage device, which is made of the electric double layer formed on the interface between the electrode and the electrolyte. It has the characteristics of farad level capacitance and voltage memory function, and its power density is much higher than that of ordinary batteries. , the energy density is much higher than traditional capacitors, thus filling the gap between these two traditional technologies. Electric double layer capacitors have broad application prospects in both military and civilian applications. Electric double-layer capacitors with small current discharge can be used as backup power for microcomputers or primary power for small devices such as toys, alarms, signal lights, etc.; ampere-level high-current discharge electric double-layer capacitors can be used alone or together with batteries to form a power system. It can be used as starting power supply and driving power supply for small loads, such as starting power supply for tanks, airplanes, rockets, missiles, etc. Electric double layer capacitors have higher specific power and longer cycle life than traditional rechargeable batteries (including nickel-metal hydride batteries and lithium-ion batteries). service life of more than 5 years). High-power electric double-layer capacitors are of special significance for the starting, acceleration and uphill driving of electric vehicles; for the management of battery energy systems of electric vehicles, prolonging the cycle life and optimal use of batteries, and the starting of fuel cell electric vehicles It is even more essential. In view of the importance of electric double layer capacitors, all industrialized countries have attached great importance to them, and made them a national key strategic research and development project.
双电层电容器的核心是电极材料的制造技术,其性能的好坏关键取决于电极材料性能的优劣。比表面积较大的材料如活性炭、活性炭纤维、碳气凝胶等都曾被作为活性电极材料研究并且部分材料(如活性炭)已经工业化。目前用得较多的电极材料是活性炭和活性炭纤维布,普通活性炭的比电容一般在150F/g以下,能量密度小于3Wh/Kg。由于活性炭材料导电性很差,在使用时需要加入一些高导电性物质如石墨、碳纤维、金属纤维等以提高导电性,降低电极的内部阻抗。这些导电材料在电极中的唯一作用就是增加活性炭颗粒之间的导电性,由于其比表面积很小,对炭电极的储能没有贡献。导电材料的添加量一般为炭电极质量的10~20%,因此,导电材料的加入在很大程度上降低了电容器的能量密度和功率密度。如制造同样容量的双电层电容器,由于导电材料的添加,使电容器质量和制造成本都大大增加,造成在实际应用过程中的不便。因此,开发具有良好导电性的电极材料是目前人们感兴趣的热点问题,这些材料一般包括碳气凝胶、炭纳米管等。炭纳米管由于昂贵的价格、比表面积及比电容较小的缺点,使电容器的制造成本成倍增加,限制了其应用。而碳气凝胶是一种纳米多孔材料,具有比表面积大及导电性能好等特点,对碳气凝胶的电学性能测试结果表明,碳气凝胶的电导率很高(约25Scm-1),且在一个很宽的温度范围(-30~100℃)保持基本不变,因此用碳气凝胶作为电极材料制作的双电层电容器可在一个很宽的温度范围内使用。但是,碳气凝胶由于比表面积较小,一般在1000m2/g以下,因此储存的能量也较少,在大规模应用时影响双电层电容器的能量密度和功率密度。The core of an electric double layer capacitor is the manufacturing technology of the electrode material, and its performance depends critically on the performance of the electrode material. Materials with large specific surface area such as activated carbon, activated carbon fiber, carbon aerogel, etc. have been studied as active electrode materials and some materials (such as activated carbon) have been industrialized. At present, activated carbon and activated carbon fiber cloth are widely used electrode materials. The specific capacitance of ordinary activated carbon is generally below 150F/g, and the energy density is less than 3Wh/Kg. Due to the poor conductivity of activated carbon materials, it is necessary to add some high-conductivity substances such as graphite, carbon fiber, metal fiber, etc. to improve the conductivity and reduce the internal impedance of the electrode. The only function of these conductive materials in the electrode is to increase the conductivity between the activated carbon particles, which does not contribute to the energy storage of carbon electrodes due to their small specific surface area. The amount of conductive material added is generally 10-20% of the mass of the carbon electrode. Therefore, the addition of conductive material reduces the energy density and power density of the capacitor to a large extent. For example, to manufacture an electric double layer capacitor with the same capacity, due to the addition of conductive materials, the quality and manufacturing cost of the capacitor will be greatly increased, causing inconvenience in the actual application process. Therefore, the development of electrode materials with good conductivity is a hot issue that people are currently interested in, and these materials generally include carbon aerogels, carbon nanotubes, etc. Due to the high price, specific surface area and small specific capacitance of carbon nanotubes, the manufacturing cost of capacitors is doubled, which limits its application. Carbon aerogel is a kind of nanoporous material, which has the characteristics of large specific surface area and good electrical conductivity. The electrical performance test results of carbon aerogel show that the electrical conductivity of carbon aerogel is very high (about 25Scm -1 ) , and remain basically unchanged in a wide temperature range (-30 ~ 100 ° C), so the electric double layer capacitor made of carbon aerogel as electrode material can be used in a wide temperature range. However, due to the small specific surface area, generally below 1000m 2 /g, carbon aerogels store less energy, which affects the energy density and power density of electric double layer capacitors in large-scale applications.
发明内容:Invention content:
本发明的目的在于开发一种高比电容且方法简单的双电层电容器电极材料的制备方法。The purpose of the present invention is to develop a high specific capacitance and simple method for preparing an electric double layer capacitor electrode material.
高比表面积活性炭的比表面积在3000m2/g以上,能够提供最大的活性表面来形成双电层存储电荷;碳气凝胶导电性较好,且本身所具有的较大的比表面积和中孔结构又能够储存相当的能量。因此,高比表面积活性炭和碳气凝胶混合制作电极可以充分发挥二者的优势,一方面利用高比表面积活性炭的微孔,另一方面利用碳气凝胶的中孔和高导电性来提高电极材料的比电容及能量密度。The specific surface area of activated carbon with high specific surface area is more than 3000m 2 /g, which can provide the largest active surface to form an electric double layer to store charges; carbon airgel has good conductivity, and it has a large specific surface area and mesopores The structure can store a considerable amount of energy. Therefore, the high specific surface area activated carbon and carbon aerogel mixed to make electrodes can give full play to the advantages of both. Specific capacitance and energy density of electrode materials.
本发明中电极材料的制备方法是以高比表面积活性炭和碳气凝胶为原料,加入粘结剂,按一定比例混合制得的。The preparation method of the electrode material in the present invention is prepared by using activated carbon with high specific surface area and carbon aerogel as raw materials, adding binder and mixing according to a certain ratio.
本发明的制备方法包括如下步骤:The preparation method of the present invention comprises the steps:
(1)醛树脂基碳气凝胶的制备(1) Preparation of aldehyde resin-based carbon airgel
将酚醛树脂、糠醛按重量比1∶1.2~1.8的比例配成7~15g/100ml浓度的丙醇溶液,催化剂用量为7~15mmol/ml,在60~100℃下反应4~7天形成醇凝胶,在250~300℃、6~8MPa超临界石油醚中干燥1-3小时形成酚醛气凝胶,将该气凝胶在600~1000℃炭化1-3小时产生碳气凝胶;The phenolic resin and furfural are formulated into a propanol solution with a concentration of 7-15g/100ml in a ratio of 1:1.2-1.8 by weight, and the catalyst dosage is 7-15mmol/ml, and react at 60-100°C for 4-7 days to form alcohol Gel, dry in supercritical petroleum ether at 250-300°C and 6-8MPa for 1-3 hours to form phenolic airgel, and carbonize the airgel at 600-1000°C for 1-3 hours to produce carbon aerogel;
(2)比电容电极材料的制备(2) Preparation of specific capacitance electrode material
将粒度小于50m、比表面积大于3000m2/g的活性炭和碳气凝胶按1∶0.05~1重量比混合,球磨1-3小时,使混合物的粒度<50m,然后在混合物中添加2-5%的聚四氟乙烯乳液,搅拌均匀,干燥后在5-10MPa压力下成型。Mix activated carbon and carbon airgel with a particle size of less than 50m and a specific surface area of more than 3000m 2 /g at a weight ratio of 1:0.05~1, ball mill for 1-3 hours to make the particle size of the mixture <50m, and then add 2-5 % polytetrafluoroethylene emulsion, stirred evenly, and molded under the pressure of 5-10MPa after drying.
如上所述的高比表面积活性炭的制备方法是以石油焦或沥青焦为原料,以KOH为活化剂,在700~1000℃活化0.5~2.0hr制得的。The above-mentioned high specific surface area activated carbon is prepared by using petroleum coke or pitch coke as raw material, KOH as activator, and activating at 700-1000°C for 0.5-2.0 hr.
如上所述的催化剂是5%的盐酸甲醇溶液。The catalyst described above is 5% methanolic hydrochloric acid.
本发明是采用在高比表面积活性炭中加入碳气凝胶的方法,可以在电极充放电过程中利用活性炭的微孔和碳气凝胶的中孔存储电荷,从而大大提高了材料的比电容。另外,碳气凝胶的高导电性可以代替石墨增加活性炭颗粒之间的导电性,避免使用石墨所造成的能量和功率密度下降的状况。该方法制得的电极材料在1mA/cm2充放电电流密度时比电容为230~330F/g。The present invention adopts the method of adding carbon aerogel to the activated carbon with high specific surface area, and can use the micropores of the activated carbon and the mesopores of the carbon aerogel to store charges during the charging and discharging process of the electrode, thereby greatly improving the specific capacitance of the material. In addition, the high conductivity of carbon airgel can replace graphite to increase the conductivity between activated carbon particles, avoiding the decline in energy and power density caused by the use of graphite. The electrode material prepared by the method has a specific capacitance of 230-330 F/g at a charging and discharging current density of 1 mA/cm 2 .
具体实施方式:Detailed ways:
对比例comparative example
取40克石油焦,与200克KOH浸渍混合,在810℃下活化1hr,制得粉状高比表面积活性炭,其BET比表面积达到3200m2/g,比电容280F/g。Take 40 grams of petroleum coke, mix it with 200 grams of KOH, and activate it at 810°C for 1 hour to prepare powdery activated carbon with high specific surface area. The BET specific surface area reaches 3200m 2 /g, and the specific capacitance is 280F/g.
将酚醛树脂、糠醛以重量比1∶1.6的比例配成10g/100ml的丙醇溶液,催化剂用量为10mmol/100ml,在80℃下反应6天形成醇凝胶,在超临界石油醚中干燥1小时形成酚醛气凝胶,将该气凝胶在800℃炭化3小时产生炭气凝胶。碳气凝胶比表面积597m2/g,比电容153.6F/g。The phenolic resin and furfural were formulated into 10g/100ml propanol solution with a weight ratio of 1:1.6, the catalyst dosage was 10mmol/100ml, reacted at 80°C for 6 days to form alcohol gel, and dried in supercritical petroleum ether for 1 The phenolic aerogel was formed within hours, and the aerogel was carbonized at 800°C for 3 hours to produce carbon aerogel. The carbon airgel has a specific surface area of 597m 2 /g and a specific capacitance of 153.6F/g.
实施例1Example 1
取BET比表面积为3200m2/g的活性炭。将酚醛树脂、糠醛以重量比1∶1.6的比例配成12g/100ml的丙醇溶液,催化剂用量为8mmol/100ml,在80℃下反应6天形成醇凝胶,在超临界石油醚中干燥2小时形成酚醛气凝胶,将该气凝胶在800℃炭化2小时产生碳气凝胶。碳气凝胶比表面积632m2/g。将活性炭、碳气凝胶按1∶0.05重量比混合,球磨3小时,使混合物的粒度<50m,然后在混合物中添加2%的聚四氟乙烯乳液,搅拌均匀,干燥后在10MPa压力下成型。电极材料的比电容为302F/g。Take activated carbon with a BET specific surface area of 3200m 2 /g. The phenolic resin and furfural are formulated into 12g/100ml propanol solution with a weight ratio of 1:1.6, the catalyst dosage is 8mmol/100ml, react at 80°C for 6 days to form alcohol gel, and dry in supercritical petroleum ether for 2 The phenolic aerogel was formed within hours, and the aerogel was carbonized at 800°C for 2 hours to produce carbon aerogel. The specific surface area of carbon airgel is 632m 2 /g. Mix activated carbon and carbon airgel at a weight ratio of 1:0.05, ball mill for 3 hours to make the particle size of the mixture <50m, then add 2% polytetrafluoroethylene emulsion to the mixture, stir evenly, dry and shape under 10MPa pressure . The specific capacitance of the electrode material is 302F/g.
实施例2Example 2
取BET比表面积为3200m2/g的活性炭。将酚醛树脂、糠醛以重量比1∶1.8的比例配成14g/100ml的丙醇溶液,催化剂用量为10mmol/100ml,在80℃下反应6天形成醇凝胶,在超临界石油醚中干燥1小时形成酚醛气凝胶,将该气凝胶在900℃炭化2小时产生碳气凝胶。碳气凝胶比表面积640m2/g。将活性炭、碳气凝胶按1∶0.15重量比混合,球磨2小时,使混合物的粒度<50m,然后在混合物中添加5%的聚四氟乙烯乳液,搅拌均匀,干燥后在10MPa压力下成型。电极材料的比电容为312F/g。Take activated carbon with a BET specific surface area of 3200m 2 /g. Phenolic resin and furfural were formulated into 14g/100ml propanol solution with a weight ratio of 1:1.8, the catalyst dosage was 10mmol/100ml, reacted at 80°C for 6 days to form alcohol gel, and dried in supercritical petroleum ether for 1 The phenolic aerogel was formed within 1 hour, and the aerogel was carbonized at 900° C. for 2 hours to produce carbon aerogel. The specific surface area of carbon airgel is 640m 2 /g. Mix activated carbon and carbon aerogel at a weight ratio of 1:0.15, ball mill for 2 hours to make the particle size of the mixture <50m, then add 5% polytetrafluoroethylene emulsion to the mixture, stir evenly, dry and shape under 10MPa pressure . The specific capacitance of the electrode material is 312F/g.
实施例3Example 3
取BET比表面积为3600m2/g的活性炭。将酚醛树脂、糠醛以重量比1∶1.4的比例配成15g/100ml的丙醇溶液,催化剂用量为15mmol/100ml,在90℃下反应5天形成醇凝胶,在超临界石油醚中干燥1小时形成酚醛气凝胶,将该气凝胶在700℃炭化3小时产生碳气凝胶。碳气凝胶比表面积578m2/g。将活性炭、碳气凝胶按1∶0.15重量比混合,球磨3小时,使混合物的粒度<50m,然后在混合物中添加2%的聚四氟乙烯乳液,搅拌均匀,干燥后在5MPa压力下成型。电极材料的比电容为320F/g。Take activated carbon with a BET specific surface area of 3600m 2 /g. Phenolic resin and furfural were formulated into 15g/100ml propanol solution with a weight ratio of 1:1.4, the catalyst dosage was 15mmol/100ml, reacted at 90°C for 5 days to form alcohol gel, dried in supercritical petroleum ether for 1 The phenolic aerogel was formed within hours, and the aerogel was carbonized at 700°C for 3 hours to produce carbon aerogel. The specific surface area of carbon airgel is 578m 2 /g. Mix activated carbon and carbon aerogel in a weight ratio of 1:0.15, ball mill for 3 hours to make the particle size of the mixture <50m, then add 2% polytetrafluoroethylene emulsion to the mixture, stir evenly, dry and shape under 5MPa pressure . The specific capacitance of the electrode material is 320F/g.
实施例4Example 4
取BET比表面积为3600m2/g的活性炭。将酚醛树脂、糠醛以重量比1∶1.2的比例配成10g/100ml的丙醇溶液,催化剂用量为12mmol/100ml,在70℃下反应7天形成醇凝胶,在超临界石油醚中干燥2小时形成酚醛气凝胶,将该气凝胶在850℃炭化2小时产生碳气凝胶。碳气凝胶比表面积682m2/g。将活性炭、碳气凝胶按1∶0.2重量比混合,球磨3小时,使混合物的粒度<50m,然后在混合物中添加3%的聚四氟乙烯乳液,搅拌均匀,干燥后在7MPa压力下成型。电极材料的比电容为330F/g。Take activated carbon with a BET specific surface area of 3600m 2 /g. Phenolic resin and furfural were formulated into 10g/100ml propanol solution in a ratio of 1:1.2 by weight, and the amount of catalyst used was 12mmol/100ml, reacted at 70°C for 7 days to form alcohol gel, dried in supercritical petroleum ether for 2 The phenolic aerogel was formed within hours, and the aerogel was carbonized at 850° C. for 2 hours to produce carbon aerogel. The specific surface area of carbon airgel is 682m 2 /g. Mix activated carbon and carbon aerogel at a weight ratio of 1:0.2, ball mill for 3 hours to make the particle size of the mixture <50m, then add 3% polytetrafluoroethylene emulsion to the mixture, stir evenly, dry and shape under 7MPa pressure . The specific capacitance of the electrode material is 330F/g.
实施例5Example 5
取BET比表面积为3600m2/g的活性炭。将酚醛树脂、糠醛以重量比1∶1.6的比例配成10g/100ml的丙醇溶液,催化剂用量为7mmol/100ml,在90℃下反应7天形成醇凝胶,在超临界石油醚中干燥2小时形成酚醛气凝胶,将该气凝胶在850℃炭化2小时产生碳气凝胶。碳气凝胶比表面积582m2/g。将活性炭、碳气凝胶按1∶0.4重量比混合,球磨3小时,使混合物的粒度<50m,然后在混合物中添加2%的聚四氟乙烯乳液,搅拌均匀,干燥后在10MPa压力下成型。电极材料的比电容为284F/g。Take activated carbon with a BET specific surface area of 3600m 2 /g. The phenolic resin and furfural are formulated into 10g/100ml propanol solution with a weight ratio of 1:1.6, the catalyst dosage is 7mmol/100ml, react at 90°C for 7 days to form alcohol gel, and dry in supercritical petroleum ether for 2 The phenolic aerogel was formed within hours, and the aerogel was carbonized at 850° C. for 2 hours to produce carbon aerogel. The specific surface area of carbon airgel is 582m 2 /g. Mix activated carbon and carbon airgel at a weight ratio of 1:0.4, ball mill for 3 hours to make the particle size of the mixture <50m, then add 2% polytetrafluoroethylene emulsion to the mixture, stir evenly, dry and shape under 10MPa pressure . The specific capacitance of the electrode material is 284F/g.
实施例6Example 6
取BET比表面积为3600m2/g的活性炭。将酚醛树脂、糠醛以重量比1∶1.5的比例配成7g/100ml的丙醇溶液,催化剂用量为12mmol/100ml,在90℃下反应7天形成醇凝胶,在超临界石油醚中干燥2小时形成酚醛气凝胶,将该气凝胶在850℃炭化2小时产生碳气凝胶。碳气凝胶比表面积652m2/g。将活性炭、碳气凝胶按1∶1重量比混合,球磨3小时,使混合物的粒度<50m,然后在混合物中添加2%的聚四氟乙烯乳液,搅拌均匀,干燥后在10MPa压力下成型。电极材料的比电容为238F/g。Take activated carbon with a BET specific surface area of 3600m 2 /g. Phenolic resin and furfural were formulated into a 7g/100ml propanol solution with a weight ratio of 1:1.5, and the catalyst dosage was 12mmol/100ml, reacted at 90°C for 7 days to form an alcohol gel, and dried in supercritical petroleum ether for 2 The phenolic aerogel was formed within hours, and the aerogel was carbonized at 850° C. for 2 hours to produce carbon aerogel. The specific surface area of carbon airgel is 652m 2 /g. Mix activated carbon and carbon aerogel at a weight ratio of 1:1, ball mill for 3 hours to make the particle size of the mixture <50m, then add 2% polytetrafluoroethylene emulsion to the mixture, stir evenly, dry and shape under 10MPa pressure . The specific capacitance of the electrode material is 238F/g.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100364021C (en) * | 2003-11-11 | 2008-01-23 | 石油大学(北京) | Electric double-layer capacitor and its preparation method |
| US20110002085A1 (en) * | 2009-07-06 | 2011-01-06 | Samsung Electro-Mechanics Co., Ltd. | Electrode for capacitor and electric double layer capacitor having the same |
| CN102035265A (en) * | 2010-12-06 | 2011-04-27 | 无锡索垠飞科技有限公司 | Wireless charging system of capacitor storage battery |
| CN103723726B (en) * | 2013-11-26 | 2015-07-15 | 广东华博企业管理咨询有限公司 | Preparation method of porous carbon for high-capacitance super capacitor |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100364021C (en) * | 2003-11-11 | 2008-01-23 | 石油大学(北京) | Electric double-layer capacitor and its preparation method |
| US20110002085A1 (en) * | 2009-07-06 | 2011-01-06 | Samsung Electro-Mechanics Co., Ltd. | Electrode for capacitor and electric double layer capacitor having the same |
| CN102035265A (en) * | 2010-12-06 | 2011-04-27 | 无锡索垠飞科技有限公司 | Wireless charging system of capacitor storage battery |
| CN102035265B (en) * | 2010-12-06 | 2013-11-20 | 南京科孚纳米技术有限公司 | Wireless charging system of capacitor storage battery |
| CN103723726B (en) * | 2013-11-26 | 2015-07-15 | 广东华博企业管理咨询有限公司 | Preparation method of porous carbon for high-capacitance super capacitor |
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