CN118516852B - Chemical activation process for carbon fiber battery felt catalyst - Google Patents
Chemical activation process for carbon fiber battery felt catalyst Download PDFInfo
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 74
- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 69
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 65
- 239000003054 catalyst Substances 0.000 title claims abstract description 39
- 238000001994 activation Methods 0.000 title claims abstract description 33
- 239000000126 substance Substances 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 238000006243 chemical reaction Methods 0.000 claims abstract description 27
- 238000002360 preparation method Methods 0.000 claims abstract description 22
- 238000001035 drying Methods 0.000 claims abstract description 21
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000000835 fiber Substances 0.000 claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims abstract description 14
- 230000003213 activating effect Effects 0.000 claims abstract description 10
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 8
- 230000008569 process Effects 0.000 claims abstract description 8
- 229920000742 Cotton Polymers 0.000 claims abstract description 4
- 229920006282 Phenolic fiber Polymers 0.000 claims abstract description 4
- 229920002239 polyacrylonitrile Polymers 0.000 claims abstract description 4
- 244000198134 Agave sisalana Species 0.000 claims abstract description 3
- 240000008564 Boehmeria nivea Species 0.000 claims abstract description 3
- 229920000297 Rayon Polymers 0.000 claims abstract description 3
- 229920002522 Wood fibre Polymers 0.000 claims abstract description 3
- 239000010426 asphalt Substances 0.000 claims abstract description 3
- 239000002025 wood fiber Substances 0.000 claims abstract description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 40
- DOGFGDKIOOAKNQ-UHFFFAOYSA-N 1-prop-2-enylpyrrolidin-1-ium-2-carboxylate Chemical compound OC(=O)C1CCCN1CC=C DOGFGDKIOOAKNQ-UHFFFAOYSA-N 0.000 claims description 25
- -1 12-mercaptododecyl cerium phosphate Chemical compound 0.000 claims description 20
- 229910052759 nickel Inorganic materials 0.000 claims description 20
- 230000004913 activation Effects 0.000 claims description 16
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 14
- HSJPMRKMPBAUAU-UHFFFAOYSA-N cerium(3+);trinitrate Chemical compound [Ce+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O HSJPMRKMPBAUAU-UHFFFAOYSA-N 0.000 claims description 12
- 238000004821 distillation Methods 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 9
- MUUOUUYKIVSIAR-LURJTMIESA-N (2s)-2-but-3-enyloxirane Chemical compound C=CCC[C@H]1CO1 MUUOUUYKIVSIAR-LURJTMIESA-N 0.000 claims description 8
- 239000004254 Ammonium phosphate Substances 0.000 claims description 7
- 229910000148 ammonium phosphate Inorganic materials 0.000 claims description 7
- 235000019289 ammonium phosphates Nutrition 0.000 claims description 7
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims description 7
- MVQUCQUAYDBXMV-UHFFFAOYSA-N 12-sulfanyldodecyl dihydrogen phosphate Chemical compound OP(O)(=O)OCCCCCCCCCCCCS MVQUCQUAYDBXMV-UHFFFAOYSA-N 0.000 claims description 6
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 claims description 6
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- QDRKDTQENPPHOJ-UHFFFAOYSA-N sodium ethoxide Chemical compound [Na+].CC[O-] QDRKDTQENPPHOJ-UHFFFAOYSA-N 0.000 claims description 6
- 238000005470 impregnation Methods 0.000 claims 1
- 238000004146 energy storage Methods 0.000 abstract description 4
- 238000001816 cooling Methods 0.000 abstract 1
- 230000001590 oxidative effect Effects 0.000 abstract 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 16
- 239000000243 solution Substances 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 6
- 238000007654 immersion Methods 0.000 description 5
- 229920002678 cellulose Polymers 0.000 description 4
- 239000001913 cellulose Substances 0.000 description 4
- 239000002243 precursor Substances 0.000 description 4
- 125000003396 thiol group Chemical group [H]S* 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- 238000007259 addition reaction Methods 0.000 description 3
- 238000003763 carbonization Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000009987 spinning Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 2
- 125000003342 alkenyl group Chemical group 0.000 description 2
- 229910052796 boron Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000002270 dispersing agent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 125000003700 epoxy group Chemical group 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- OXBLVCZKDOZZOJ-UHFFFAOYSA-N 2,3-Dihydrothiophene Chemical compound C1CC=CS1 OXBLVCZKDOZZOJ-UHFFFAOYSA-N 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 238000006845 Michael addition reaction Methods 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 238000007171 acid catalysis Methods 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000013475 authorization Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006664 bond formation reaction Methods 0.000 description 1
- 150000001721 carbon Chemical group 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010668 complexation reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000007405 data analysis Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 150000002815 nickel Chemical class 0.000 description 1
- 239000012038 nucleophile Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920005903 polyol mixture Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000007142 ring opening reaction Methods 0.000 description 1
- 230000001235 sensitizing effect Effects 0.000 description 1
- 229910000033 sodium borohydride Inorganic materials 0.000 description 1
- 239000012279 sodium borohydride Substances 0.000 description 1
- 239000001509 sodium citrate Substances 0.000 description 1
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012651 thiol-epoxy addition reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- D06M13/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
- D06M13/50—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with organometallic compounds; with organic compounds containing boron, silicon, selenium or tellurium atoms
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- D06M11/01—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with hydrogen, water or heavy water; with hydrides of metals or complexes thereof; with boranes, diboranes, silanes, disilanes, phosphines, diphosphines, stibines, distibines, arsines, or diarsines or complexes thereof
- D06M11/05—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with hydrogen, water or heavy water; with hydrides of metals or complexes thereof; with boranes, diboranes, silanes, disilanes, phosphines, diphosphines, stibines, distibines, arsines, or diarsines or complexes thereof with water, e.g. steam; with heavy water
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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Abstract
本发明提供碳纤维电池毡催化剂化学活化工艺,涉及活性碳纤维制备技术领域。包括以下步骤:将选自聚丙烯腈、沥青纤维、酚醛纤维、粘胶纤维、木纤维、剑麻纤维、苎麻纤维、棉纤维中一种的碳纤维浸渍在催化剂中,并进行烘干;烘干后,将碳纤维缓慢升温,在空气中充分氧化后冷却至室温;将氧化后的碳纤维置于管式高温炉中,在氮气的保护下升温,用水蒸汽进行活化处理,然后烘干。本发明制备的碳纤维电池毡的高比表面积和得率的结合,使得活性碳纤维在能量存储和转换领域具有优异的性能表现。The present invention provides a carbon fiber battery felt catalyst chemical activation process, which relates to the technical field of activated carbon fiber preparation. The process comprises the following steps: impregnating a carbon fiber selected from polyacrylonitrile, asphalt fiber, phenolic fiber, viscose fiber, wood fiber, sisal fiber, ramie fiber, and cotton fiber in a catalyst, and drying the carbon fiber; after drying, slowly heating the carbon fiber, fully oxidizing it in the air, and then cooling it to room temperature; placing the oxidized carbon fiber in a tubular high-temperature furnace, heating it under the protection of nitrogen, activating it with water vapor, and then drying it. The combination of high specific surface area and yield of the carbon fiber battery felt prepared by the present invention enables the activated carbon fiber to have excellent performance in the field of energy storage and conversion.
Description
技术领域Technical Field
本发明涉及活性碳纤维制备技术领域,尤其是碳纤维电池毡催化剂化学活化工艺。The invention relates to the technical field of active carbon fiber preparation, in particular to a process for chemical activation of carbon fiber battery felt catalyst.
背景技术Background Art
活性碳纤维是一种理想、高效的吸附材料,是在碳纤维技术和活性炭技术相结合的基础上发展起来的。活性碳纤维是继粒状活性炭和粉状活性炭之后的第3代活性炭产品,因具备特殊的表面化学结构和物理吸附特性,被广泛应用于环保、医用卫生、化工等领域。Activated carbon fiber is an ideal and efficient adsorption material, which is developed on the basis of the combination of carbon fiber technology and activated carbon technology. Activated carbon fiber is the third generation of activated carbon products after granular activated carbon and powdered activated carbon. Due to its special surface chemical structure and physical adsorption characteristics, it is widely used in environmental protection, medical hygiene, chemical industry and other fields.
授权公告号为CN103290526B的专利,公开了一种利用木质生物质为原料通过物理活化制备木质活性碳纤维的方法,该方法是将木粉置于液化装置中,加入多元醇混合物为液化剂,在酸催化条件下制备液化物;加入合成剂合成纺丝液后、熔融纺丝,制得纤维原丝;最后将原丝置于碳化、活化装置中,以水蒸气作为活化剂制备获得木质活性碳纤维。The patent with authorization announcement number CN103290526B discloses a method for preparing wood activated carbon fibers by physical activation using wood biomass as raw materials. The method comprises placing wood powder in a liquefaction device, adding a polyol mixture as a liquefier, and preparing a liquefied product under acid catalysis conditions; adding a synthetic agent to synthesize a spinning solution, and then melt spinning to obtain fiber precursors; finally, placing the precursors in a carbonization and activation device, and using water vapor as an activator to prepare wood activated carbon fibers.
公开号为CN105220275A的专利申请,公开了利用纤维素制备活性碳纤维的方法。具体是将乙酸纤维素放入液化反应釜中,加入苯酚与酸性催化剂,得到纤维素苯酚树脂;在树脂中添加一定比例丙酮作为溶剂合成纺丝液,纺丝液经熔融纺丝后,在一定条件下热固化,制备获得纤维素原丝;将原丝置于碳化以及活化装置中,通过碳化及活化过程制备获得纤维素基础活性碳纤维。The patent application with publication number CN105220275A discloses a method for preparing activated carbon fibers using cellulose. Specifically, cellulose acetate is placed in a liquefaction reactor, phenol and an acid catalyst are added to obtain a cellulose phenol resin; a certain proportion of acetone is added to the resin as a solvent to synthesize a spinning solution, and the spinning solution is melt-spun and thermally cured under certain conditions to prepare cellulose precursors; the precursors are placed in a carbonization and activation device, and cellulose-based activated carbon fibers are prepared through a carbonization and activation process.
公开号为CN109735830A的专利申请,公开了一种活化液以及制备方法和碳纤维复合材料的制备方法。一种活化液,由以下组分制成:分散剂、柠檬酸钠、镍盐和含硼化合物;含硼化合物为硼氢化钾或硼氢化钠;所述活化液的pH值为9~11。该活化液中分散剂可以避免碳纤维在水溶液中的团聚且可以防止碳纤维活化水洗后再次团聚,且该活化液集一体化,碳纤维只需置于活化液中,即可完成碳纤维分散、敏化和活化的步骤。The patent application with publication number CN109735830A discloses an activation solution and a preparation method and a preparation method of a carbon fiber composite material. An activation solution is made of the following components: a dispersant, sodium citrate, a nickel salt and a boron-containing compound; the boron-containing compound is potassium borohydride or sodium borohydride; the pH value of the activation solution is 9 to 11. The dispersant in the activation solution can prevent the carbon fiber from agglomerating in an aqueous solution and can prevent the carbon fiber from agglomerating again after activation and washing. The activation solution is integrated, and the carbon fiber only needs to be placed in the activation solution to complete the steps of dispersing, sensitizing and activating the carbon fiber.
然而现有技术生产工艺得率低、成本高;化学活化法虽然可以大幅度提高产品得率,但需要多次水洗,产品较脆而难以在生产中得到推广。However, the existing production process has low yield and high cost; although the chemical activation method can greatly improve the product yield, it requires multiple water washings, and the product is brittle and difficult to be promoted in production.
发明内容Summary of the invention
本发明的目的在于提供碳纤维电池毡催化剂化学活化工艺,本方法制备的碳纤维电池毡的高比表面积和得率的结合,使得活性碳纤维在能量存储和转换领域具有优异的性能表现。The purpose of the present invention is to provide a process for chemical activation of carbon fiber battery felt catalyst. The combination of high specific surface area and yield of the carbon fiber battery felt prepared by this method makes the activated carbon fiber have excellent performance in the field of energy storage and conversion.
本发明所采用的技术方案是:The technical solution adopted by the present invention is:
碳纤维电池毡催化剂化学活化工艺,包括以下步骤:The carbon fiber battery felt catalyst chemical activation process includes the following steps:
S1:将选自聚丙烯腈、沥青纤维、酚醛纤维、粘胶纤维、木纤维、剑麻纤维、苎麻纤维、棉纤维中一种的碳纤维浸渍在催化剂中,并进行烘干;S1: impregnating a carbon fiber selected from the group consisting of polyacrylonitrile, asphalt fiber, phenolic fiber, viscose fiber, wood fiber, sisal fiber, ramie fiber, and cotton fiber in a catalyst and drying the carbon fiber;
S2:烘干后,将碳纤维缓慢升温至240-250℃,在空气中充分氧化后冷却至室温;S2: After drying, the carbon fiber is slowly heated to 240-250°C, fully oxidized in the air, and then cooled to room temperature;
S3:将氧化后的碳纤维置于管式高温炉中,在氮气的保护下升温,用水蒸汽进行活化处理,然后烘干;S3: placing the oxidized carbon fiber in a tubular high-temperature furnace, heating it under the protection of nitrogen, activating it with water vapor, and then drying it;
所述的催化剂的制备方法包括以下步骤:The preparation method of the catalyst comprises the following steps:
在反应釜中加入0.03-0.6份的12-巯基十二烷基磷酸铈配合物和0.05-0.5份的1-烯丙基吡咯烷-2-羧酸镍配合物,再加入2-6份的乙醇钠和200-300份的丙酮,搅拌均匀后升温至45-55℃反应100-150分钟;随后加入10-20份的磷酸铵和1-6份的(S)-1,2-环氧基-5-己烯,保温混合100-150分钟,得到所需的催化剂。0.03-0.6 parts of 12-mercaptododecyl cerium phosphate complex and 0.05-0.5 parts of 1-allylpyrrolidine-2-carboxylic acid nickel complex are added into a reaction kettle, and then 2-6 parts of sodium ethoxide and 200-300 parts of acetone are added, and the mixture is stirred evenly and heated to 45-55° C. and reacted for 100-150 minutes; then 10-20 parts of ammonium phosphate and 1-6 parts of (S)-1,2-epoxy-5-hexene are added, and the mixture is kept warm and mixed for 100-150 minutes to obtain the desired catalyst.
进一步的,所述的12-巯基十二烷基磷酸铈配合物的制备方法为:Furthermore, the preparation method of the 12-mercaptododecyl cerium phosphate complex is:
在反应釜中称取10-17份的12-巯基十二烷基磷酸和3-6份的硝酸铈,加入100-200份的水中,在30-40℃下反应30-90分钟,然后通过蒸馏除去水分,得到12-巯基十二烷基磷酸铈配合物。10-17 parts of 12-mercaptododecyl phosphoric acid and 3-6 parts of cerium nitrate are weighed into a reaction kettle, added into 100-200 parts of water, reacted at 30-40° C. for 30-90 minutes, and then the water is removed by distillation to obtain a cerium 12-mercaptododecyl phosphoric acid complex.
进一步的,所述的1-烯丙基吡咯烷-2-羧酸镍配合物的制备方法为:Furthermore, the preparation method of the 1-allylpyrrolidine-2-carboxylic acid nickel complex is:
在反应釜中称取12-20份的1-烯丙基吡咯烷-2-羧酸和2-5份的硝酸镍,加入200-300份的水中,在40-60℃下反应20-40分钟,然后通过蒸馏除去水分,得到1-烯丙基吡咯烷-2-羧酸镍配合物。12-20 parts of 1-allylpyrrolidine-2-carboxylic acid and 2-5 parts of nickel nitrate are weighed into a reaction kettle, added into 200-300 parts of water, reacted at 40-60° C. for 20-40 minutes, and then the water is removed by distillation to obtain 1-allylpyrrolidine-2-carboxylic acid nickel complex.
进一步的,所述的S1的浸渍时间为30-60min。Furthermore, the immersion time of S1 is 30-60 minutes.
进一步的,所述的S2的氧化时间为60-90min。Furthermore, the oxidation time of S2 is 60-90 min.
进一步的,所述的S2的升温速率为3-5℃/min。Furthermore, the heating rate of S2 is 3-5°C/min.
进一步的,所述的S3的水蒸汽活化过程中,碳纤维在800-900℃的温度下保持1-3h,以确保碳纤维的表面充分活化,从而提高其在电池中的电化学性能。Furthermore, during the water vapor activation process of S3, the carbon fiber is maintained at a temperature of 800-900° C. for 1-3 hours to ensure that the surface of the carbon fiber is fully activated, thereby improving its electrochemical performance in the battery.
反应机理:巯基-烯基加成反应:Reaction mechanism: thiol-ene addition reaction:
12-巯基十二烷基磷酸铈配合物中的巯基(-SH)与1-烯丙基吡咯烷-2-羧酸镍配合物中的烯基(C=C)发生加成反应;该反应可能通过迈克尔加成机理进行,其中巯基作为亲核试剂攻击烯基的β碳原子,形成碳-硫键。The thiol group (-SH) in the cerium 12-mercaptododecylphosphate complex undergoes an addition reaction with the alkenyl group (C=C) in the nickel 1-allylpyrrolidine-2-carboxylate complex; the reaction may proceed via a Michael addition mechanism, in which the thiol group acts as a nucleophile to attack the β-carbon atom of the alkenyl group to form a carbon-sulfur bond.
巯基-环氧基加成反应:Thiol-epoxy addition reaction:
加成产物中的剩余巯基与(S)-1,2-环氧基-5-己烯中的环氧基进行开环加成反应,巯基攻击环氧基中较少取代的碳原子,导致环氧环开环并形成新的碳-硫键。The remaining thiol group in the addition product undergoes a ring-opening addition reaction with the epoxy group in (S)-1,2-epoxy-5-hexene, and the thiol group attacks the less substituted carbon atom in the epoxy group, resulting in the opening of the epoxy ring and the formation of a new carbon-sulfur bond.
复配:Compounding:
加成产物与磷酸铵进行复配,涉及氢键形成或其他非共价相互作用,从而产生最终的催化剂结构;这种复配可以改善催化剂的热稳定性、机械强度或催化活性。The addition product is complexed with ammonium phosphate, involving hydrogen bond formation or other non-covalent interactions, to produce the final catalyst structure; this complexation can improve the thermal stability, mechanical strength or catalytic activity of the catalyst.
有益效果:1、碳纤维毡改性:使用本发明的催化剂对碳纤维毡进行改性,可以显著提高其孔隙率和平均孔径;这种改性使得碳纤维毡在电池应用中具有更好的电解质渗透性和离子传输效率。Beneficial effects: 1. Modification of carbon fiber felt: Using the catalyst of the present invention to modify the carbon fiber felt can significantly improve its porosity and average pore size; this modification enables the carbon fiber felt to have better electrolyte permeability and ion transfer efficiency in battery applications.
2、活性碳纤维性能:本发明制备的活性碳纤维具有以下特点:2. Activated carbon fiber performance: The activated carbon fiber prepared by the present invention has the following characteristics:
比表面积高达2155m2/g,这为电化学反应提供了极大的表面活性区域,增强了电荷存储和传递能力;The specific surface area is as high as 2155m2 /g, which provides a large surface active area for electrochemical reactions and enhances the charge storage and transfer capabilities;
得率达到59.37%,这表明在活化过程中原材料的有效利用率较高,减少了材料浪费;The yield reached 59.37%, which indicates that the effective utilization rate of raw materials was high during the activation process, reducing material waste;
综合性能:高比表面积和得率的结合,使得活性碳纤维在能量存储和转换领域具有优异的性能表现。Comprehensive performance: The combination of high specific surface area and yield makes activated carbon fiber have excellent performance in the field of energy storage and conversion.
具体实施方式DETAILED DESCRIPTION
为更进一步阐述本发明为实现预定发明目的所采取的技术手段及功效,以下结合实施例与对比例,进行详细说明:In order to further explain the technical means and effects adopted by the present invention to achieve the predetermined invention purpose, the following is a detailed description in combination with embodiments and comparative examples:
比表面积测定:参照GB2596-81氮气吸附法,采用JB-1型比表面测定仪测定。Specific surface area determination: refer to GB2596-81 nitrogen adsorption method and use JB-1 specific surface area measuring instrument for determination.
实施例1:碳纤维电池毡催化剂化学活化工艺,包括以下步骤:Example 1: A process for chemical activation of a carbon fiber battery felt catalyst, comprising the following steps:
S1:将选自聚丙烯腈的碳纤维浸渍在催化剂中,并进行烘干;S1: impregnating carbon fiber selected from polyacrylonitrile in a catalyst and drying the carbon fiber;
S2:烘干后,将碳纤维缓慢升温至240℃,在空气中充分氧化后冷却至室温;S2: After drying, the carbon fiber is slowly heated to 240°C, fully oxidized in air, and then cooled to room temperature;
S3:将氧化后的碳纤维置于管式高温炉中,在氮气的保护下升温,用水蒸汽进行活化处理,然后烘干。S3: placing the oxidized carbon fiber in a tubular high-temperature furnace, heating it under the protection of nitrogen, activating it with water vapor, and then drying it.
所述的催化剂的制备方法包括以下步骤:The preparation method of the catalyst comprises the following steps:
在反应釜中加入0.03g的12-巯基十二烷基磷酸铈配合物和0.05g的1-烯丙基吡咯烷-2-羧酸镍配合物,再加入2g的乙醇钠和200g的丙酮,搅拌均匀后升温至45℃反应100分钟;随后加入10g的磷酸铵和1g的(S)-1,2-环氧基-5-己烯,保温混合100分钟,得到所需的催化剂。0.03 g of 12-mercaptododecyl cerium phosphate complex and 0.05 g of 1-allylpyrrolidine-2-carboxylic acid nickel complex were added to a reaction kettle, and then 2 g of sodium ethoxide and 200 g of acetone were added, and the mixture was stirred evenly and heated to 45° C. to react for 100 minutes; then 10 g of ammonium phosphate and 1 g of (S)-1,2-epoxy-5-hexene were added, and the mixture was kept warm and mixed for 100 minutes to obtain the desired catalyst.
所述的12-巯基十二烷基磷酸铈配合物的制备方法为:The preparation method of the 12-mercaptododecyl cerium phosphate complex is as follows:
在反应釜中称取10g的12-巯基十二烷基磷酸和3g的硝酸铈,加入100g的水中,在30℃下反应30分钟,然后通过蒸馏除去水分,得到12-巯基十二烷基磷酸铈配合物。10 g of 12-mercaptododecyl phosphoric acid and 3 g of cerium nitrate were weighed into a reaction kettle, added into 100 g of water, reacted at 30° C. for 30 minutes, and then the water was removed by distillation to obtain a cerium 12-mercaptododecyl phosphoric acid complex.
所述的1-烯丙基吡咯烷-2-羧酸镍配合物的制备方法为:The preparation method of the 1-allylpyrrolidine-2-carboxylic acid nickel complex is as follows:
在反应釜中称取12g的1-烯丙基吡咯烷-2-羧酸和2g的硝酸镍,加入200g的水中,在40℃下反应20分钟,然后通过蒸馏除去水分,得到1-烯丙基吡咯烷-2-羧酸镍配合物。12 g of 1-allylpyrrolidine-2-carboxylic acid and 2 g of nickel nitrate were weighed into a reaction kettle, added into 200 g of water, reacted at 40° C. for 20 minutes, and then the water was removed by distillation to obtain 1-allylpyrrolidine-2-carboxylic acid nickel complex.
所述的S1的浸渍时间为30min。The immersion time of S1 is 30 minutes.
所述的S2的氧化时间为60min。The oxidation time of S2 is 60 min.
所述的S2的升温速率为3℃/min。The heating rate of S2 is 3°C/min.
所述的S3的水蒸汽活化过程中,碳纤维在800℃的温度下保持1h,以确保碳纤维的表面充分活化,从而提高其在电池中的电化学性能。During the water vapor activation process of S3, the carbon fiber is kept at a temperature of 800° C. for 1 hour to ensure that the surface of the carbon fiber is fully activated, thereby improving its electrochemical performance in the battery.
实施例2:碳纤维电池毡催化剂化学活化工艺,包括以下步骤:Example 2: A process for chemically activating a carbon fiber battery felt catalyst, comprising the following steps:
S1:将选自沥青纤维的碳纤维浸渍在催化剂中,并进行烘干;S1: impregnating carbon fiber selected from pitch fiber in a catalyst and drying the catalyst;
S2:烘干后,将碳纤维缓慢升温至245℃,在空气中充分氧化后冷却至室温;S2: After drying, the carbon fiber is slowly heated to 245°C, fully oxidized in air, and then cooled to room temperature;
S3:将氧化后的碳纤维置于管式高温炉中,在氮气的保护下升温,用水蒸汽进行活化处理,然后烘干。S3: placing the oxidized carbon fiber in a tubular high-temperature furnace, heating it under the protection of nitrogen, activating it with water vapor, and then drying it.
所述的催化剂的制备方法包括以下步骤:The preparation method of the catalyst comprises the following steps:
在反应釜中加入0.2g的12-巯基十二烷基磷酸铈配合物和0.2g的1-烯丙基吡咯烷-2-羧酸镍配合物,再加入3g的乙醇钠和240g的丙酮,搅拌均匀后升温至48℃反应110分钟;随后加入13g的磷酸铵和2g的(S)-1,2-环氧基-5-己烯,保温混合110分钟,得到所需的催化剂。0.2 g of 12-mercaptododecyl cerium phosphate complex and 0.2 g of 1-allylpyrrolidine-2-carboxylic acid nickel complex were added to a reaction kettle, and then 3 g of sodium ethoxide and 240 g of acetone were added. After stirring evenly, the temperature was raised to 48° C. and the reaction was carried out for 110 minutes. Subsequently, 13 g of ammonium phosphate and 2 g of (S)-1,2-epoxy-5-hexene were added, and the mixture was kept warm and mixed for 110 minutes to obtain the desired catalyst.
所述的12-巯基十二烷基磷酸铈配合物的制备方法为:The preparation method of the 12-mercaptododecyl cerium phosphate complex is as follows:
在反应釜中称取12g的12-巯基十二烷基磷酸和4g的硝酸铈,加入140g的水中,在35℃下反应50分钟,然后通过蒸馏除去水分,得到12-巯基十二烷基磷酸铈配合物。12 g of 12-mercaptododecyl phosphoric acid and 4 g of cerium nitrate were weighed into a reaction kettle, added into 140 g of water, reacted at 35° C. for 50 minutes, and then the water was removed by distillation to obtain a cerium 12-mercaptododecyl phosphoric acid complex.
所述的1-烯丙基吡咯烷-2-羧酸镍配合物的制备方法为:The preparation method of the 1-allylpyrrolidine-2-carboxylic acid nickel complex is as follows:
在反应釜中称取14g的1-烯丙基吡咯烷-2-羧酸和3g的硝酸镍,加入240g的水中,在45℃下反应25分钟,然后通过蒸馏除去水分,得到1-烯丙基吡咯烷-2-羧酸镍配合物。14 g of 1-allylpyrrolidine-2-carboxylic acid and 3 g of nickel nitrate were weighed into a reaction kettle, added to 240 g of water, reacted at 45° C. for 25 minutes, and then the water was removed by distillation to obtain 1-allylpyrrolidine-2-carboxylic acid nickel complex.
所述的S1的浸渍时间为40min。The immersion time of S1 is 40 minutes.
所述的S2的氧化时间为70min。The oxidation time of S2 is 70 min.
所述的S2的升温速率为4℃/min。The heating rate of S2 is 4°C/min.
所述的S3的水蒸汽活化过程中,碳纤维在840℃的温度下保持2h,以确保碳纤维的表面充分活化,从而提高其在电池中的电化学性能。During the water vapor activation process of S3, the carbon fiber is kept at a temperature of 840° C. for 2 hours to ensure that the surface of the carbon fiber is fully activated, thereby improving its electrochemical performance in the battery.
实施例3:碳纤维电池毡催化剂化学活化工艺,包括以下步骤:Example 3: A process for chemical activation of a carbon fiber battery felt catalyst, comprising the following steps:
S1:将选自酚醛纤维的碳纤维浸渍在催化剂中,并进行烘干;S1: impregnating carbon fiber selected from phenolic fiber in a catalyst and drying it;
S2:烘干后,将碳纤维缓慢升温至245℃,在空气中充分氧化后冷却至室温;S2: After drying, the carbon fiber is slowly heated to 245°C, fully oxidized in air, and then cooled to room temperature;
S3:将氧化后的碳纤维置于管式高温炉中,在氮气的保护下升温,用水蒸汽进行活化处理,然后烘干。S3: placing the oxidized carbon fiber in a tubular high-temperature furnace, heating it under the protection of nitrogen, activating it with water vapor, and then drying it.
所述的催化剂的制备方法包括以下步骤:The preparation method of the catalyst comprises the following steps:
在反应釜中加入0.5g的12-巯基十二烷基磷酸铈配合物和0.4g的1-烯丙基吡咯烷-2-羧酸镍配合物,再加入5g的乙醇钠和280g的丙酮,搅拌均匀后升温至53℃反应140分钟;随后加入18g的磷酸铵和5g的(S)-1,2-环氧基-5-己烯,保温混合40分钟,得到所需的催化剂。0.5 g of 12-mercaptododecyl cerium phosphate complex and 0.4 g of 1-allylpyrrolidine-2-carboxylic acid nickel complex were added to a reaction kettle, and then 5 g of sodium ethoxide and 280 g of acetone were added. After stirring evenly, the temperature was raised to 53° C. and the reaction lasted for 140 minutes. Subsequently, 18 g of ammonium phosphate and 5 g of (S)-1,2-epoxy-5-hexene were added, and the mixture was kept warm and mixed for 40 minutes to obtain the desired catalyst.
所述的12-巯基十二烷基磷酸铈配合物的制备方法为:The preparation method of the 12-mercaptododecyl cerium phosphate complex is as follows:
在反应釜中称取16g的12-巯基十二烷基磷酸和5g的硝酸铈,加入180g的水中,在35℃下反应70分钟,然后通过蒸馏除去水分,得到12-巯基十二烷基磷酸铈配合物。16 g of 12-mercaptododecyl phosphoric acid and 5 g of cerium nitrate were weighed into a reaction kettle, added into 180 g of water, reacted at 35° C. for 70 minutes, and then the water was removed by distillation to obtain a 12-mercaptododecyl phosphoric acid cerium complex.
所述的1-烯丙基吡咯烷-2-羧酸镍配合物的制备方法为:The preparation method of the 1-allylpyrrolidine-2-carboxylic acid nickel complex is as follows:
在反应釜中称取18g的1-烯丙基吡咯烷-2-羧酸和4g的硝酸镍,加入280g的水中,在55℃下反应35分钟,然后通过蒸馏除去水分,得到1-烯丙基吡咯烷-2-羧酸镍配合物。18 g of 1-allylpyrrolidine-2-carboxylic acid and 4 g of nickel nitrate were weighed into a reaction kettle, added into 280 g of water, reacted at 55° C. for 35 minutes, and then the water was removed by distillation to obtain 1-allylpyrrolidine-2-carboxylic acid nickel complex.
所述的S1的浸渍时间为50min。The immersion time of S1 is 50 minutes.
所述的S2的氧化时间为80min。The oxidation time of S2 is 80 min.
所述的S2的升温速率为4℃/min。The heating rate of S2 is 4°C/min.
所述的S3的水蒸汽活化过程中,碳纤维在880℃的温度下保持2h,以确保碳纤维的表面充分活化,从而提高其在电池中的电化学性能。During the water vapor activation process of S3, the carbon fiber is kept at a temperature of 880° C. for 2 hours to ensure that the surface of the carbon fiber is fully activated, thereby improving its electrochemical performance in the battery.
实施例4:碳纤维电池毡催化剂化学活化工艺,包括以下步骤:Example 4: A process for chemically activating a carbon fiber battery felt catalyst, comprising the following steps:
S1:将选自棉纤维的碳纤维浸渍在催化剂中,并进行烘干;S1: impregnating carbon fiber selected from cotton fiber in a catalyst and drying it;
S2:烘干后,将碳纤维缓慢升温至250℃,在空气中充分氧化后冷却至室温;S2: After drying, the carbon fiber is slowly heated to 250°C, fully oxidized in air, and then cooled to room temperature;
S3:将氧化后的碳纤维置于管式高温炉中,在氮气的保护下升温,用水蒸汽进行活化处理,然后烘干。S3: placing the oxidized carbon fiber in a tubular high-temperature furnace, heating it under the protection of nitrogen, activating it with water vapor, and then drying it.
所述的催化剂的制备方法包括以下步骤:The preparation method of the catalyst comprises the following steps:
在反应釜中加入0.6g的12-巯基十二烷基磷酸铈配合物和0.5g的1-烯丙基吡咯烷-2-羧酸镍配合物,再加入6g的乙醇钠和300g的丙酮,搅拌均匀后升温至55℃反应150分钟;随后加入20g的磷酸铵和6g的(S)-1,2-环氧基-5-己烯,保温混合150分钟,得到所需的催化剂。0.6 g of 12-mercaptododecyl cerium phosphate complex and 0.5 g of 1-allylpyrrolidine-2-carboxylic acid nickel complex were added to a reaction kettle, and then 6 g of sodium ethoxide and 300 g of acetone were added. After stirring evenly, the temperature was raised to 55° C. and the reaction was carried out for 150 minutes. Subsequently, 20 g of ammonium phosphate and 6 g of (S)-1,2-epoxy-5-hexene were added, and the mixture was mixed for 150 minutes under heat preservation to obtain the desired catalyst.
所述的12-巯基十二烷基磷酸铈配合物的制备方法为:The preparation method of the 12-mercaptododecyl cerium phosphate complex is as follows:
在反应釜中称取17g的12-巯基十二烷基磷酸和6g的硝酸铈,加入200g的水中,在40℃下反应90分钟,然后通过蒸馏除去水分,得到12-巯基十二烷基磷酸铈配合物。17 g of 12-mercaptododecyl phosphoric acid and 6 g of cerium nitrate were weighed into a reaction kettle, added into 200 g of water, reacted at 40° C. for 90 minutes, and then the water was removed by distillation to obtain a 12-mercaptododecyl phosphoric acid cerium complex.
所述的1-烯丙基吡咯烷-2-羧酸镍配合物的制备方法为:The preparation method of the 1-allylpyrrolidine-2-carboxylic acid nickel complex is as follows:
在反应釜中称取20g的1-烯丙基吡咯烷-2-羧酸和5g的硝酸镍,加入300g的水中,在60℃下反应40分钟,然后通过蒸馏除去水分,得到1-烯丙基吡咯烷-2-羧酸镍配合物。20 g of 1-allylpyrrolidine-2-carboxylic acid and 5 g of nickel nitrate were weighed into a reaction kettle, added into 300 g of water, reacted at 60° C. for 40 minutes, and then the water was removed by distillation to obtain 1-allylpyrrolidine-2-carboxylic acid nickel complex.
所述的S1的浸渍时间为60min。The immersion time of S1 is 60 minutes.
所述的S2的氧化时间为90min。The oxidation time of S2 is 90 min.
所述的S2的升温速率为5℃/min。The heating rate of S2 is 5°C/min.
所述的S3的水蒸汽活化过程中,碳纤维在900℃的温度下保持3h,以确保碳纤维的表面充分活化,从而提高其在电池中的电化学性能。During the water vapor activation process of S3, the carbon fiber is kept at a temperature of 900° C. for 3 hours to ensure that the surface of the carbon fiber is fully activated, thereby improving its electrochemical performance in the battery.
对比例1:不加入12-巯基十二烷基磷酸铈配合物,其他同实施例1。Comparative Example 1: No 12-mercaptododecyl cerium phosphate complex was added, and the other steps were the same as in Example 1.
对比例2:不加入1-烯丙基吡咯烷-2-羧酸镍配合物,其他同实施例1。Comparative Example 2: No 1-allylpyrrolidine-2-carboxylic acid nickel complex was added, and the other steps were the same as in Example 1.
对比例3:不加入(S)-1,2-环氧基-5-己烯,其他同实施例1。Comparative Example 3: (S)-1,2-epoxy-5-hexene was not added, and the other steps were the same as those in Example 1.
表1:各实施例与对比例的测试结果Table 1: Test results of various embodiments and comparative examples
通过以上实施例与对比例的数据分析,本发明制备的碳纤维电池毡,具有高比表面积和得率,使得活性碳纤维在能量存储和转换领域具有优异的性能表现。Through the data analysis of the above embodiments and comparative examples, the carbon fiber battery felt prepared by the present invention has a high specific surface area and yield, so that the activated carbon fiber has excellent performance in the field of energy storage and conversion.
以上实施例只对本发明具有示例性的作用,而不具有任何限制性的作用,本领域的技术人员在本发明的基础上做出的任何非实质性的修改,都应属于本发明的保护范围。The above embodiments are only illustrative of the present invention and do not have any limiting effect. Any non-substantial modifications made by those skilled in the art on the basis of the present invention should fall within the protection scope of the present invention.
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CN116770581A (en) * | 2023-08-28 | 2023-09-19 | 烟台奥森制动材料有限公司 | Method for preparing antioxidant carbon fiber solid felt by adopting metal ion purifying agent |
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