CN108726517A - The method for improving rice husk base capacitance carbon volumetric capacitance - Google Patents
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- 235000007164 Oryza sativa Nutrition 0.000 title claims abstract description 83
- 235000009566 rice Nutrition 0.000 title claims abstract description 83
- 239000010903 husk Substances 0.000 title claims abstract description 82
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 80
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 66
- 238000000034 method Methods 0.000 title claims abstract description 32
- 240000007594 Oryza sativa Species 0.000 title 1
- 241000209094 Oryza Species 0.000 claims abstract description 82
- 239000003990 capacitor Substances 0.000 claims abstract description 54
- 239000002296 pyrolytic carbon Substances 0.000 claims abstract description 28
- 239000003054 catalyst Substances 0.000 claims abstract description 20
- 238000000197 pyrolysis Methods 0.000 claims abstract description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 24
- 238000010438 heat treatment Methods 0.000 claims description 24
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 22
- 239000010426 asphalt Substances 0.000 claims description 22
- 230000003197 catalytic effect Effects 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 14
- 239000003610 charcoal Substances 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 13
- 239000000843 powder Substances 0.000 claims description 12
- 229910052757 nitrogen Inorganic materials 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 238000001816 cooling Methods 0.000 claims description 9
- 239000002904 solvent Substances 0.000 claims description 9
- 230000007935 neutral effect Effects 0.000 claims description 8
- 239000012065 filter cake Substances 0.000 claims description 7
- 238000005470 impregnation Methods 0.000 claims description 7
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 7
- 239000000725 suspension Substances 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 6
- 239000012535 impurity Substances 0.000 claims description 6
- 239000011812 mixed powder Substances 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 6
- 239000002585 base Substances 0.000 claims description 5
- 238000010992 reflux Methods 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 4
- 238000003763 carbonization Methods 0.000 claims description 4
- 239000002243 precursor Substances 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 239000008367 deionised water Substances 0.000 claims description 2
- 229910021641 deionized water Inorganic materials 0.000 claims description 2
- 238000007654 immersion Methods 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- 229960000935 dehydrated alcohol Drugs 0.000 claims 1
- 230000018044 dehydration Effects 0.000 abstract description 8
- 238000006297 dehydration reaction Methods 0.000 abstract description 8
- 239000002028 Biomass Substances 0.000 abstract description 7
- 238000002309 gasification Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 238000002715 modification method Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 8
- 239000002245 particle Substances 0.000 description 6
- 238000001994 activation Methods 0.000 description 3
- 239000007772 electrode material Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 230000004913 activation Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000000967 suction filtration Methods 0.000 description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000007233 catalytic pyrolysis Methods 0.000 description 1
- 230000006690 co-activation Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- H—ELECTRICITY
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- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
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- H01G11/34—Carbon-based characterised by carbonisation or activation of carbon
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/84—Processes for the manufacture of hybrid or EDL capacitors, or components thereof
- H01G11/86—Processes for the manufacture of hybrid or EDL capacitors, or components thereof specially adapted for electrodes
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Abstract
本发明公开了提高稻壳基电容炭体积比电容的方法,属于生物质能源化工领域,采用三种方法提高振实密度,提高体积比电容;具体涉及:(1)采用脱水固炭催化剂浸渍处理,控温热解增加固定炭含量;(2)热解炭水热脱硅后,模板炭利用浸渍沥青处理,填充气化带来的微孔隙,提高振实密度;(3)用电极沥青修饰改性电容炭表面,提高导电性和振实密度。与现有技术相比,本发明通过不同改性处理方法制备稻壳基电容炭,提高了电容炭的振实密度、体积比电容、循环稳定性及电容炭收率。
The invention discloses a method for increasing the volume specific capacitance of rice husk-based capacitor carbon, which belongs to the field of biomass energy chemical industry. Three methods are used to increase the tap density and volume specific capacitance; specifically, it involves: (1) impregnating treatment with a dehydration carbon-fixing catalyst , temperature-controlled pyrolysis to increase the fixed carbon content; (2) After hydrothermal desiliconization of the pyrolytic carbon, the template carbon is treated with impregnated pitch to fill the micropores caused by gasification and increase the tap density; (3) Modified with electrode pitch Modified capacitor carbon surface to improve conductivity and tap density. Compared with the prior art, the invention prepares the rice husk-based capacitor carbon through different modification methods, and improves the tap density, volume specific capacitance, cycle stability and yield of the capacitor carbon.
Description
技术领域technical field
本发明属于生物质能源化工领域,公开了一种提高稻壳基电容炭体积比电容的方法,具体涉及脱水固炭催化剂浸渍稻壳、浸渍沥青处理模板炭、电极沥青修饰改性电容炭提高稻壳炭体积比电容的方法。The invention belongs to the field of biomass energy chemical industry, and discloses a method for increasing the volume specific capacitance of rice husk-based capacitor carbon, in particular to impregnating rice husk with a dehydration carbon-fixing catalyst, impregnating asphalt to treat template carbon, and modifying electrode pitch to modify capacitor carbon to improve rice Shell carbon volume specific capacitance method.
背景技术Background technique
生物质材料具有来源广泛、环境友好等特点。近年来,利用生物质为原料制备电容炭得到了广泛的关注。稻壳是一种价格低廉、产量巨大的可再生生物质资源,以稻壳为原料制备的电容炭具有多级孔道的结构以及较大的比表面积,但是稻壳基电容炭作为超级电容器电极材料的主要问题是稻壳固定炭含量低,作为超级电容器的体积比电容小,在存储单位质量的电容时需要更大的体积,使其商业性较低,不利于实际应用。Biomass materials have the characteristics of wide sources and environmental friendliness. In recent years, the use of biomass as raw material to prepare capacitor carbon has received extensive attention. Rice husk is a renewable biomass resource with low price and huge output. Capacitor carbon prepared from rice husk has a multi-level pore structure and a large specific surface area. However, rice husk-based capacitor carbon is used as a supercapacitor electrode material The main problem is that the fixed carbon content of rice husk is low, the volume specific capacitance as a supercapacitor is small, and a larger volume is required to store the capacitance per unit mass, making it less commercial and not conducive to practical applications.
为了提高稻壳基电容炭的体积比电容,本发明使用脱水固炭催化剂处理稻壳后热解,再用浸渍沥青对脱硅热解炭改性,活化后,再用电极沥青处理。沥青是一种固定炭含量较高且导电性较好的材料,利用沥青对脱硅热解炭和活性炭改性可以提高材料的振实密度,提高体积比电容,还增加了材料的导电性,从而提升电化学性能,如公告号为“CN107364863A”的中国专利文献,公开了改性稻壳基活性炭的制备方法,有效地提高了稻壳基活性炭作为电极材料的体积比电容与循环稳定性。脱水固炭催化剂在热解过程对稻壳催化脱水,控制温度增加稻壳在热解过程中脱水时间,减少气相和液相的生成,从而增大固相的含量,进而提升稻壳炭的收率,提升电容炭的体积比电容。In order to improve the volume specific capacitance of the rice husk-based capacitor carbon, the present invention uses a dehydration carbon-fixing catalyst to treat the rice husk and then pyrolyzes it, then uses impregnated pitch to modify the desiliconized pyrolytic carbon, and after activation, treats it with electrode pitch. Asphalt is a material with high fixed carbon content and good electrical conductivity. Using asphalt to modify desiliconized pyrolytic carbon and activated carbon can increase the tap density of the material, increase the volume specific capacitance, and increase the electrical conductivity of the material. In order to improve the electrochemical performance, such as the Chinese patent document with the notification number "CN107364863A", which discloses the preparation method of modified rice husk-based activated carbon, which effectively improves the volume specific capacitance and cycle stability of rice husk-based activated carbon as an electrode material. The dehydration carbon-fixing catalyst catalyzes the dehydration of rice husks during the pyrolysis process. Controlling the temperature increases the dehydration time of rice husks during the pyrolysis process, reduces the formation of gas and liquid phases, thereby increasing the content of solid phases, thereby increasing the yield of rice husk charcoal. The rate increases the volume specific capacitance of the capacitor carbon.
目前稻壳基电容炭存在的问题:The current problems of rice husk-based capacitor carbon:
1、稻壳在热解过程中大量的碳以气态和液态流失,固定炭含量少;1. During the pyrolysis process of rice husk, a large amount of carbon is lost in gaseous and liquid states, and the content of fixed carbon is small;
2、稻壳电容炭的导电性较差,使得电解质离子运输困难;2. The conductivity of rice husk capacitor carbon is poor, which makes it difficult to transport electrolyte ions;
3、振实密度低,影响体积比电容。3. The tap density is low, which affects the volume specific capacitance.
因此现有技术中需要一种新的技术方案解决这一问题。Therefore need a kind of new technical scheme to solve this problem in the prior art.
发明内容Contents of the invention
在稻壳热解过程中,挥发分逸出,形成大量微孔,热解炭的振实密度较低,经脱硅活化后,电容炭的振实密度更低,导致体积比电容低,同体积的电容器贮存能力小,这已经制约了稻壳炭(或生物质炭)在储能电池和超级电容器领域的应用,本发明的目的是提供提高稻壳炭体积比电容的方法,以稻壳为炭源,经过催化剂处理、炭化、沥青改性脱硅热解炭、沥青改性电容炭等步骤制备出改性稻壳基电容炭材料。所制备的材料是具有电化学稳定性好、体积比电容高的超级电容器电极材料特性,而且其成本低、污染小、环境友好,可大规模生产。During the pyrolysis process of rice husk, volatile matter escapes, forming a large number of micropores, and the tap density of pyrolytic carbon is low. After desiliconization and activation, the tap density of capacitor carbon is lower, resulting in low volume specific capacitance. The capacitor storage capacity of volume is little, and this has restricted the application of rice husk charcoal (or biomass charcoal) in the field of energy storage batteries and supercapacitors, and the purpose of the present invention is to provide the method for improving rice husk charcoal volume specific capacitance, with rice husk charcoal As a carbon source, the modified rice husk-based capacitor carbon material was prepared through the steps of catalyst treatment, carbonization, asphalt-modified desiliconization pyrolytic carbon, and asphalt-modified capacitor carbon. The prepared material has the characteristics of a supercapacitor electrode material with good electrochemical stability and high volume specific capacitance, and has low cost, little pollution, and environmental friendliness, and can be mass-produced.
为了达到上述目的,本发明采用如下的技术方案:提高稻壳基电容炭体积比电容的方法,其特征在于,该方法包括如下步骤:In order to achieve the above object, the present invention adopts following technical scheme: improve the method for rice husk base capacitor carbon volume specific capacitance, it is characterized in that, this method comprises the steps:
步骤一、将稻壳筛分除杂,粉碎,得到稻壳粉,稻壳粉与催化剂溶液混合后进行浸渍处理,浸渍处理完毕后,降至室温进行抽滤,将滤饼置于80℃~100℃下烘干,得到预处理稻壳;Step 1. Sieve the rice husk to remove impurities and crush it to obtain rice husk powder. Mix the rice husk powder with the catalyst solution and perform impregnation treatment. drying at 100°C to obtain pretreated rice husk;
步骤二、将步骤一所制备的预处理稻壳置于管式炉中,先升温至200℃~300℃,热解0.5h,再升温至500℃~600℃在氮气保护下热解1h,降至室温,得到热解炭;Step 2. Put the pretreated rice husk prepared in step 1 in a tube furnace, first heat up to 200°C-300°C, pyrolyze for 0.5h, then heat up to 500°C-600°C, and pyrolyze for 1h under nitrogen protection. Be down to room temperature, obtain pyrolysis charcoal;
步骤三、按固液比1Kg:10L的比例将步骤二中得到的热解炭和浓度为5wt%的NaOH溶液加入到反应釜中,加热回流反应2h,降温,过滤分离,将滤饼洗至中性,烘干,得到脱硅热解炭;Step 3: Add the pyrolytic charcoal obtained in Step 2 and the NaOH solution with a concentration of 5wt% into the reaction kettle according to the ratio of solid-to-liquid ratio 1Kg: 10L, heat and reflux for 2 hours, cool down, filter and separate, and wash the filter cake until Neutral, dried to obtain desiliconized pyrolytic carbon;
步骤四、将步骤三得到的脱硅热解炭与浸渍沥青混合均匀,置于反应釜中,升温至150℃~250℃,在压力为0.1MPa~0.6MPa的条件下浸渍2h~5h,冷却后,得到沥青浸渍前驱体;Step 4. Mix the desiliconized pyrolytic carbon obtained in step 3 with the impregnated pitch evenly, place it in a reaction kettle, raise the temperature to 150°C-250°C, impregnate it for 2h-5h under the pressure of 0.1MPa-0.6MPa, and cool After that, the asphalt impregnated precursor is obtained;
步骤五、将步骤四得到的沥青浸渍前驱体转移到管式炉中,升温到600℃~1000℃炭化1h~2h,制备出沥青浸渍热解炭;Step 5. Transfer the pitch-impregnated precursor obtained in step 4 to a tube furnace, heat up to 600°C-1000°C for carbonization for 1h-2h, and prepare pitch-impregnated pyrolytic carbon;
步骤六、将步骤五所制备的沥青浸渍热解炭进行处理得到炭粉,炭粉与碱按照炭碱比1:(2.0~2.5)混合均匀,置于管式炉中,先以5℃/min的升温速率升温至450℃,保持0.5h,再继续以5℃/min的升温速率升温至700℃,保持1h,降至室温后取出,用热去离子水洗至中性,于120℃烘干,制备出催化稻壳/沥青基电容炭。Step 6. Treat the asphalt-impregnated pyrolytic carbon prepared in step 5 to obtain carbon powder. Mix the carbon powder and alkali evenly according to the carbon-alkali ratio of 1: (2.0-2.5), place it in a tube furnace, and first heat it at 5°C/min The heating rate is raised to 450°C, kept for 0.5h, and then continued to rise to 700°C at a heating rate of 5°C/min, kept for 1h, and taken out after cooling down to room temperature, washed with hot deionized water until neutral, and dried at 120°C , prepared catalytic rice husk/pitch-based capacitive carbon.
提高稻壳基电容炭体积比电容的方法,采用上述步骤一至步骤六所述的方法,其特征在于,还包括:The method for improving the volume specific capacitance of rice husk-based capacitor carbon adopts the method described in the above steps 1 to 6, and is characterized in that it also includes:
步骤七、沥青改性电容炭的制备:Step 7, preparation of asphalt modified capacitor carbon:
(1)将步骤六所制备的催化稻壳/沥青基电容炭加入到沥青悬浊液中,搅拌分散0.5h~2h,加热回收溶剂,固体置于干燥箱中,85℃干燥5h~12h,制备出沥青/电容炭混合粉末;(1) Add the catalytic rice husk/pitch-based capacitor carbon prepared in step 6 into the asphalt suspension, stir and disperse for 0.5h-2h, heat to recover the solvent, put the solid in a drying oven, and dry at 85°C for 5h-12h, Prepare pitch/capacitor carbon mixed powder;
(2)将步骤(1)制备的沥青/电容炭混合粉末转移至管式炉中,在氮气保护下,升温至150℃~250℃恒温热处理1h~2h,再升温至600℃~1000℃恒温热处理1h~2h,降温,打散,制备出沥青改性电容炭。(2) Transfer the pitch/capacitor carbon mixed powder prepared in step (1) to a tube furnace, and under the protection of nitrogen, raise the temperature to 150°C-250°C for 1h-2h constant temperature heat treatment, and then raise the temperature to 600°C-1000°C constant temperature Heat treatment for 1h-2h, cool down, break up, and prepare pitch-modified capacitor carbon.
步骤一中所述的浸渍处理过程如下:将稻壳粉与催化剂溶液加入反应釜,密封,利用蒸汽加热,加热温度为120℃~130℃,加压浸渍1h;或加热体系的温度为30℃~50℃,恒温浸渍24h。The impregnation treatment process described in step 1 is as follows: add rice husk powder and catalyst solution to the reactor, seal it, and heat it with steam at a heating temperature of 120°C to 130°C, and pressurize and impregnate for 1 hour; or the temperature of the heating system is 30°C ~50°C, constant temperature immersion for 24h.
所述步骤一中的催化剂是NH4Cl、NH4OH、HCl、H2SO4、H3PO4其中的一种或二种以上的混合物。The catalyst in the first step is one or a mixture of NH 4 Cl, NH 4 OH, HCl, H 2 SO 4 , H 3 PO 4 .
所述步骤一的催化剂溶液的质量浓度为0%~20%。The mass concentration of the catalyst solution in the step 1 is 0%-20%.
所述步骤一的稻壳粉与催化剂溶液的固液比为1Kg:(5~20)L。The solid-to-liquid ratio of the rice husk powder and the catalyst solution in the step 1 is 1Kg:(5-20)L.
所述步骤七中的沥青悬浊液的制备方法是:将沥青粉末加入溶剂中,搅拌分散0.5~2h,得到沥青悬浊液。The preparation method of the asphalt suspension in the step 7 is: adding the asphalt powder into the solvent, stirring and dispersing for 0.5-2 hours to obtain the asphalt suspension.
所述步骤七中沥青与催化稻壳/沥青基电容炭固含量的比例为(10~30):100。The ratio of pitch to catalytic rice husk/pitch-based capacitor carbon solid content in step 7 is (10-30):100.
所述步骤七中的溶剂为环己醇、无水乙醇、丙酮、四氢呋喃、环己烷、正己烷中一种或二种的混合物。The solvent in the step seven is one or a mixture of cyclohexanol, absolute ethanol, acetone, tetrahydrofuran, cyclohexane, and n-hexane.
所述沥青与溶剂的固液比为(5Kg~15Kg):100L。The solid-to-liquid ratio of the pitch to the solvent is (5Kg-15Kg):100L.
通过上述设计方案,本发明可以带来如下有益效果:Through the above design scheme, the present invention can bring the following beneficial effects:
1、所用的稻壳是一种可再生的生物质资源,制备的过程无污染且价格低廉;沥青材料来源广泛,低成本,环境友好,可大规模生产。1. The rice husk used is a renewable biomass resource, and the preparation process is non-polluting and low in price; the asphalt material has a wide range of sources, low cost, environmental friendliness, and can be produced on a large scale.
2、固炭催化剂处理稻壳,促进脱水,减少稻壳在炭化过程中气相与液相的流失,增加固定炭含量。2. The carbon-fixing catalyst treats rice husks, promotes dehydration, reduces the loss of gas and liquid phases during the carbonization of rice husks, and increases the content of fixed carbon.
3、沥青在达到软化点温度时可以形成流动态,在活化过程中流动态的沥青可以对改性热解炭修饰,从而有效地提高材料的电化学性能。3. Asphalt can form a flow state when it reaches the softening point temperature, and the flow state of the asphalt can modify the modified pyrolytic carbon during the activation process, thereby effectively improving the electrochemical performance of the material.
4、沥青的固定炭含量较高,与稻壳热解炭共活化可以提高活性炭的振实密度,从而提高材料的体积比电容。4. The fixed carbon content of asphalt is high, and co-activation with rice husk pyrolytic carbon can increase the tap density of activated carbon, thereby increasing the volume specific capacitance of the material.
5、模板炭利用浸渍沥青处理,将细炭粉包裹在颗粒表面统一粒径,并填充气化带来的微孔隙,提高振实密度。5. The template carbon is treated with impregnated asphalt, and the fine carbon powder is wrapped on the particle surface with a uniform particle size, and the micropores caused by gasification are filled to increase the tap density.
附图说明Description of drawings
图1为本发明实施例1与实施例2在电流密度为1A/g时恒流充放电20000次的比电容与循环圈数示意图。Fig. 1 is a schematic diagram of the specific capacitance and the number of cycles of the embodiment 1 and the embodiment 2 of the present invention when the current density is 1A/g and the constant current is charged and discharged 20,000 times.
具体实施方式Detailed ways
为了更清楚地表明本发明,下面结合优选实施例对本发明做进一步的说明。本领域技术人员应当理解,下面所具体描述的内容是说明性的而非限制性的,不应以此限制本发明的保护范围。为了避免混淆本发明的实质,公知的方法和过程并没有详细的叙述。In order to show the present invention more clearly, the present invention will be further described below in conjunction with preferred embodiments. Those skilled in the art should understand that the content specifically described below is illustrative rather than restrictive, and should not limit the protection scope of the present invention. In order not to obscure the essence of the present invention, well-known methods and procedures have not been described in detail.
实施例1Example 1
(1)将原料稻壳筛分除杂,粉碎至粒径为10mm~20mm,得到稻壳粉,备用;(1) The raw material rice husk is screened to remove impurities, and crushed to a particle size of 10 mm to 20 mm to obtain rice husk powder, which is set aside;
(2)将步骤(1)得到的稻壳粉置于管式炉中,在氮气保护下,以5℃/min的升温速率升温至200℃,热解脱水0.5h,再以5℃/min的升温速率升温至500℃,热解1h,得到热解炭;(2) Place the rice husk powder obtained in step (1) in a tube furnace, and under the protection of nitrogen, heat up to 200°C at a heating rate of 5°C/min, pyrolysis and dehydration for 0.5h, and then heat up to 200°C at a heating rate of 5°C/min The heating rate is increased to 500°C, pyrolyzed for 1 hour, and pyrolytic charcoal is obtained;
(3)将步骤(2)得到的热解炭和浓度为5wt%的NaOH溶液按照固液比1Kg:10L混合,加热回流2h,降至室温后抽滤,滤饼水洗至中性,烘干,得到脱硅稻壳热解炭;(3) Mix the pyrolytic carbon obtained in step (2) with the NaOH solution with a concentration of 5wt% according to the solid-to-liquid ratio of 1Kg:10L, heat and reflux for 2h, suction filter after cooling down to room temperature, wash the filter cake with water until neutral, and dry , to obtain desiliconized rice husk pyrolytic carbon;
(4)将步骤(3)得到的脱硅稻壳热解炭与氢氧化钠按照质量比1:2.5加入到高混机中混匀,转移到氮气保护的管式炉中,先以5℃/min的升温速率升温至450℃保持0.5h,再以5℃/min的升温速率升温至700℃,保持1h,降至室温后洗至中性,于120℃下烘干,得到稻壳基电容炭AC1。(4) Add the desiliconized rice husk pyrolytic carbon and sodium hydroxide obtained in step (3) into the high-mixer and mix evenly according to the mass ratio of 1:2.5, then transfer to the tube furnace protected by nitrogen, and first heat the mixture at 5°C Raise the temperature to 450°C at a heating rate of 5°C/min and keep it for 0.5h, then raise the temperature to 700°C at a heating rate of 5°C/min, keep it for 1h, wash to neutral after cooling down to room temperature, and dry at 120°C to obtain rice husk base Capacitor carbon AC1.
实施例2Example 2
(1)将原料稻壳筛分除杂,粉碎至粒径为10mm~20mm,与浓度为5wt%的NH4OH溶液按照固液比1Kg:10L加入到反应釜中,密封加热至120℃,加压浸渍1h,降至室温后抽滤,滤液调整浓度后循环利用,滤饼在100℃下烘干,得到催化剂处理稻壳,备用;(1) Sieve the raw rice husk to remove impurities, crush it to a particle size of 10mm-20mm, and add NH 4 OH solution with a concentration of 5wt% into the reaction kettle according to the solid-to-liquid ratio of 1Kg:10L, seal and heat to 120°C, Pressure impregnation for 1 hour, suction filtration after cooling down to room temperature, the filtrate is recycled after adjusting the concentration, and the filter cake is dried at 100°C to obtain catalyst-treated rice husks for later use;
(2)将步骤(1)得到的催化剂处理稻壳置于管式炉中,在氮气保护下,以5℃/min的升温速率升温至200℃,热解0.5h,再以5℃/min的升温速率升温至500℃,热解1h,得到热解炭;(2) Place the catalyst-treated rice husk obtained in step (1) in a tube furnace, and under the protection of nitrogen, heat up to 200°C at a heating rate of 5°C/min, pyrolyze for 0.5h, and then heat up to 200°C at a heating rate of 5°C/min. The heating rate is increased to 500°C, pyrolyzed for 1 hour, and pyrolytic charcoal is obtained;
(3)将步骤(2)得到的热解炭按照固液比1Kg:10L与浓度为5wt%的NaOH溶液混合,加热回流2h,降至室温后抽滤,将滤饼水洗至中性,烘干,得到脱硅热解炭;(3) The pyrolytic charcoal obtained in step (2) is mixed with a NaOH solution having a concentration of 5wt% according to a solid-to-liquid ratio of 1Kg:10L, heated to reflux for 2h, suction filtered after being down to room temperature, and the filter cake is washed to neutrality, dried dry to obtain desiliconized pyrolytic carbon;
(4)按照炭碱质量比1:2.5,将步骤(3)得到的脱硅热解炭与氢氧化钠加入置于氮气保护的管式炉中,先以5℃/min的升温速率升温至450℃保持0.5h,再以5℃/min的升温速率升温至700℃,保持1h,降至室温后洗至中性,于120℃下烘干,得到催化稻壳基电容炭AC2。(4) According to the carbon-alkali mass ratio of 1:2.5, add the desiliconized pyrolytic carbon and sodium hydroxide obtained in step (3) into a tube furnace protected by nitrogen, and first heat up to Keep at 450°C for 0.5h, then raise the temperature to 700°C at a rate of 5°C/min, keep for 1h, wash to neutral after cooling down to room temperature, and dry at 120°C to obtain catalytic rice husk-based capacitor carbon AC2.
实施例3Example 3
(1)将原料稻壳筛分除杂,粉碎至粒径为10mm~20mm,与浓度为5wt%的NH4OH溶液按照固液比1Kg:10L加入到反应釜中,密封加热至120℃,加压浸渍1h,降至室温后抽滤,滤液调整浓度后循环利用,滤饼在100℃下烘干,得到催化剂处理稻壳,备用;(1) Sieve the raw rice husk to remove impurities, crush it to a particle size of 10 mm to 20 mm, and add NH 4 OH solution with a concentration of 5wt% into the reaction kettle according to the solid-to-liquid ratio of 1Kg:10L, seal and heat to 120°C, Pressure impregnation for 1 hour, suction filtration after cooling down to room temperature, the filtrate is recycled after adjusting the concentration, and the filter cake is dried at 100°C to obtain catalyst-treated rice husks for later use;
(2)将步骤(1)得到的催化剂处理稻壳置于管式炉中,在氮气保护下,先以5℃/min的升温速率升温至200℃,热解0.5h,再以升温速率升温至500℃,热解1h,得到催化热解炭;(2) Place the catalyst-treated rice husk obtained in step (1) in a tube furnace, and under the protection of nitrogen, first raise the temperature to 200°C at a heating rate of 5°C/min, pyrolyze for 0.5h, and then raise the temperature at a heating rate To 500 ° C, pyrolysis for 1 hour, to obtain catalytic pyrolysis carbon;
(3)将步骤(2)得到的催化热解炭按照固液比1Kg:10L与浓度为5wt%的NaOH溶液混合,加热回流2h,降至室温后抽滤,将滤饼水洗至中性,烘干,得到脱硅热解炭;(3) The catalytic pyrolytic carbon obtained in step (2) is mixed with a NaOH solution having a concentration of 5wt% according to a solid-to-liquid ratio of 1Kg:10L, heated to reflux for 2h, suction filtered after being down to room temperature, and the filter cake is washed to neutrality, drying to obtain desiliconized pyrolytic carbon;
(4)按照质量比为4:1,将步骤(3)得到的脱硅热解炭与浸渍沥青混合均匀,置于反应釜中,升温至200℃,在压力为0.5MPa条件下浸渍2h,冷却后,得到沥青浸渍热解炭;(4) According to the mass ratio of 4:1, mix the desiliconized pyrolytic carbon obtained in step (3) with the impregnated pitch evenly, place it in a reaction kettle, raise the temperature to 200°C, and impregnate it for 2 hours under the condition of a pressure of 0.5MPa, After cooling, the pitch-impregnated pyrolytic carbon is obtained;
(5)按照炭碱质量比1:2.5,将步骤(4)得到的沥青浸渍热解炭与氢氧化钠加入置于氮气保护的管式炉中,先以5℃/min的升温速率升温至450℃保持0.5h,再以5℃/min的升温速率升温至700℃,保持1h,降至室温后洗至中性,于120℃下烘干,得到催化稻壳/沥青基电容炭AC3。(5) According to the carbon-alkali mass ratio of 1:2.5, add the asphalt-impregnated pyrolytic carbon and sodium hydroxide obtained in step (4) into a tube furnace protected by nitrogen, and first heat up to Keep at 450°C for 0.5h, then raise the temperature to 700°C at a rate of 5°C/min, hold for 1h, wash to neutral after cooling down to room temperature, and dry at 120°C to obtain catalytic rice husk/pitch-based capacitor carbon AC3.
实施例4Example 4
按照质量比为6:1,将步骤(3)得到的脱硅热解炭与浸渍沥青混合均匀,置于反应釜中,其他条件同实施例3一致,得到催化稻壳/沥青基电容炭AC4。According to the mass ratio of 6:1, the desiliconized pyrolytic carbon obtained in step (3) is mixed with the impregnated pitch evenly, and placed in the reaction kettle. The other conditions are the same as in Example 3, and the catalytic rice husk/pitch-based capacitor carbon AC4 is obtained. .
实施例5Example 5
按照质量比为8:1,将步骤(3)得到的脱硅热解炭与浸渍沥青混合均匀,置于反应釜中,其他条件同实施例3一致,得到催化稻壳/沥青基电容炭AC5。According to the mass ratio of 8:1, the desiliconized pyrolytic carbon obtained in step (3) is mixed evenly with the impregnated pitch, and placed in the reaction kettle. The other conditions are the same as in Example 3, and the catalytic rice husk/pitch-based capacitor carbon AC5 is obtained. .
实施例6Example 6
按照质量比为10:1,将步骤(3)得到的脱硅热解炭与浸渍沥青混合均匀,置于反应釜中,其他条件同实施例3一致,得到催化稻壳/沥青基电容炭AC6。According to the mass ratio of 10:1, the desiliconized pyrolytic carbon obtained in step (3) was mixed with the impregnated pitch evenly, and placed in the reaction kettle. The other conditions were the same as in Example 3, and the catalytic rice husk/pitch-based capacitor carbon AC6 was obtained. .
实施例7Example 7
将原料稻壳筛分除杂,粉碎至粒径为10mm~20mm,与质量浓度为2%的HCl溶液按照固液比1Kg:10L混合,其他条件同实施例3一致,得到催化稻壳/沥青基电容炭AC7。The raw rice husk is screened to remove impurities, crushed to a particle size of 10 mm to 20 mm, mixed with HCl solution having a mass concentration of 2% according to a solid-to-liquid ratio of 1Kg:10L, and other conditions are the same as in Example 3 to obtain catalytic rice husk/asphalt Base Capacitor Carbon AC7.
实施例8Example 8
(1)按照干基质量比4:1,将实施例3制备的催化稻壳/沥青基电容炭加入到电极沥青乙醇悬浊液中,搅拌分散1h,加热回收溶剂,固体置于干燥箱中,85℃干燥5h~12h,制备出沥青/电容炭混合粉末;(1) According to the dry mass ratio of 4:1, the catalytic rice husk/pitch-based capacitor carbon prepared in Example 3 was added to the electrode pitch ethanol suspension, stirred and dispersed for 1 hour, the solvent was recovered by heating, and the solid was placed in a drying box , dried at 85°C for 5h to 12h to prepare pitch/capacitor carbon mixed powder;
(2)将沥青/电容炭混合粉末转移至管式炉中,在氮气保护下,升温至200℃恒温热处理1h,再升温至800℃恒温热处理1h,降温,打散,制备出沥青改性电容炭AC8。(2) Transfer the asphalt/capacitor carbon mixed powder to a tube furnace, and under the protection of nitrogen, heat up to 200°C for 1 hour, then heat up to 800°C for 1 hour, cool down, break up, and prepare a pitch-modified capacitor Charcoal AC8.
表1实施例样品的循环稳定性与比电容Cyclic stability and specific capacitance of table 1 embodiment sample
注:体积比电容与循环稳定性均在6moL/L的KOH电解液中测试。Note: The volume specific capacitance and cycle stability are tested in 6moL/L KOH electrolyte.
从表1可以看出,催化稻壳/沥青基电容炭的体积比电容与稻壳基电容炭相比有了较大的提升,电化学循环稳定性也更优异。It can be seen from Table 1 that the volume specific capacitance of the catalytic rice husk/pitch-based capacitor carbon has been greatly improved compared with the rice husk-based capacitor carbon, and the electrochemical cycle stability is also better.
显然,以上实施例的说明只是用于帮助理解本发明的方法及其核心思想,但是对于本领域的普通技术人员而言,可以在不脱离权利要求所述的本发明的精神和原理的情况下对这些实施例进行多种变化、修改和替换,这些改进和修饰也落入本发明权利要求的保护范围之内。Obviously, the descriptions of the above embodiments are only used to help understand the method of the present invention and its core idea, but for those of ordinary skill in the art, they can Various changes, modifications and substitutions are made to these embodiments, and these improvements and modifications also fall within the protection scope of the claims of the present invention.
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OKHOVAT, A.: ""Pore Size Distribution Analysis of Coal-Based Activated Carbons: Investigating the Effects of Activating Agent and Chemical Ratio"", 《ISRN CHEMICAL ENGINEERING》 * |
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CN112142051A (en) * | 2020-08-24 | 2020-12-29 | 吉林大学 | A method for removing active functional groups on the surface of capacitive carbon by chemical coating |
CN116588932A (en) * | 2023-05-19 | 2023-08-15 | 中国神华煤制油化工有限公司 | Method for manufacturing coconut shell capacitor carbon for super capacitor, coconut shell capacitor carbon and application |
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