CN114804070A - Preparation method of carbon nano hemispherical particles - Google Patents
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 51
- 239000002245 particle Substances 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 238000003756 stirring Methods 0.000 claims abstract description 44
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000013067 intermediate product Substances 0.000 claims abstract description 24
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000010438 heat treatment Methods 0.000 claims abstract description 23
- 238000005530 etching Methods 0.000 claims abstract description 22
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 20
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000005406 washing Methods 0.000 claims abstract description 18
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 15
- 239000010703 silicon Substances 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000007787 solid Substances 0.000 claims abstract description 14
- 238000006482 condensation reaction Methods 0.000 claims abstract description 9
- 238000001035 drying Methods 0.000 claims abstract description 9
- 238000000967 suction filtration Methods 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 7
- 239000000047 product Substances 0.000 claims abstract description 7
- 238000000227 grinding Methods 0.000 claims abstract description 5
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 5
- 239000000243 solution Substances 0.000 claims description 81
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 45
- 238000001291 vacuum drying Methods 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 14
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 13
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 239000008098 formaldehyde solution Substances 0.000 claims description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 9
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 9
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 claims description 8
- 239000008367 deionised water Substances 0.000 claims description 8
- 229910021641 deionized water Inorganic materials 0.000 claims description 8
- ZQZCOBSUOFHDEE-UHFFFAOYSA-N tetrapropyl silicate Chemical compound CCCO[Si](OCCC)(OCCC)OCCC ZQZCOBSUOFHDEE-UHFFFAOYSA-N 0.000 claims description 8
- 238000003837 high-temperature calcination Methods 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 6
- 238000005119 centrifugation Methods 0.000 claims description 6
- 239000011248 coating agent Substances 0.000 claims description 5
- 238000000576 coating method Methods 0.000 claims description 5
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 4
- 239000004472 Lysine Substances 0.000 claims description 4
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 claims description 4
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 4
- KDXKERNSBIXSRK-YFKPBYRVSA-N L-lysine Chemical compound NCCCC[C@H](N)C(O)=O KDXKERNSBIXSRK-YFKPBYRVSA-N 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 3
- 239000007859 condensation product Substances 0.000 claims description 3
- 239000001307 helium Substances 0.000 claims description 3
- 229910052734 helium Inorganic materials 0.000 claims description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 3
- 230000035484 reaction time Effects 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 239000003381 stabilizer Substances 0.000 claims description 3
- 229960000935 dehydrated alcohol Drugs 0.000 claims 1
- 229960004756 ethanol Drugs 0.000 claims 1
- 239000003054 catalyst Substances 0.000 abstract description 23
- 238000001354 calcination Methods 0.000 abstract description 3
- 239000012876 carrier material Substances 0.000 abstract description 2
- 230000007935 neutral effect Effects 0.000 abstract description 2
- 239000012295 chemical reaction liquid Substances 0.000 abstract 2
- 239000002345 surface coating layer Substances 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 17
- 230000000052 comparative effect Effects 0.000 description 13
- 230000006872 improvement Effects 0.000 description 11
- 239000000843 powder Substances 0.000 description 9
- 238000012546 transfer Methods 0.000 description 9
- 230000005540 biological transmission Effects 0.000 description 8
- 239000010411 electrocatalyst Substances 0.000 description 8
- 239000000377 silicon dioxide Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 238000012360 testing method Methods 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 6
- 239000010410 layer Substances 0.000 description 6
- 238000003786 synthesis reaction Methods 0.000 description 6
- 238000009826 distribution Methods 0.000 description 5
- 238000011068 loading method Methods 0.000 description 5
- 238000007789 sealing Methods 0.000 description 5
- 235000012239 silicon dioxide Nutrition 0.000 description 5
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 239000011259 mixed solution Substances 0.000 description 4
- 239000002077 nanosphere Substances 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012044 organic layer Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000004917 carbon fiber Substances 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000004570 mortar (masonry) Substances 0.000 description 2
- 239000002105 nanoparticle Substances 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000002525 ultrasonication Methods 0.000 description 2
- XKZQKPRCPNGNFR-UHFFFAOYSA-N 2-(3-hydroxyphenyl)phenol Chemical compound OC1=CC=CC(C=2C(=CC=CC=2)O)=C1 XKZQKPRCPNGNFR-UHFFFAOYSA-N 0.000 description 1
- 238000005904 alkaline hydrolysis reaction Methods 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000003760 magnetic stirring Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- -1 phenolic aldehyde Chemical class 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000004627 transmission electron microscopy Methods 0.000 description 1
- 238000001132 ultrasonic dispersion Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/15—Nano-sized carbon materials
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
- C25B11/055—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material
- C25B11/057—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material consisting of a single element or compound
- C25B11/065—Carbon
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- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
- C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
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- C01P2004/01—Particle morphology depicted by an image
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- C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
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Abstract
Description
技术领域technical field
本发明涉及催化剂制备领域,尤其是涉及一种碳纳米半球材料的颗粒方法。The invention relates to the field of catalyst preparation, in particular to a particle method of a carbon nano hemisphere material.
背景技术Background technique
随着全球化石燃料的燃烧与能源需求的日益提高,环境危机与能源危机迫使我们寻找新型能源以替代传统不可再生能源。而解决这一问题的有效途径之一便是电催化。无论是新型电池的应用,还是开发新能源减少碳排放的电解水、CO2电还原等反应都依靠高效温度的电催化剂。催化剂载体是负载型催化剂的重要组成部分。良好的催化剂载体不仅对催化剂起到支撑作用,而且能极大地提高催化剂本身的性能。对于电催化而言,载体的优化能够极大提高催化剂的稳定性,同时也能通过改变结构形貌、提升传质效率、提高本征活性显著地提升催化剂的性能。因此,制备出合适的电催化载体至关重要。With the burning of fossil fuels and the increasing energy demand in the world, the environmental crisis and energy crisis force us to look for new energy sources to replace traditional non-renewable energy sources. One of the effective ways to solve this problem is electrocatalysis. Whether it is the application of new batteries, or the development of new energy sources to reduce carbon emissions, such as water electrolysis and CO 2 electroreduction, all rely on high-efficiency temperature electrocatalysts. The catalyst carrier is an important part of the supported catalyst. A good catalyst carrier not only supports the catalyst, but also greatly improves the performance of the catalyst itself. For electrocatalysis, the optimization of the support can greatly improve the stability of the catalyst, and can also significantly improve the performance of the catalyst by changing the structure and morphology, improving the mass transfer efficiency, and improving the intrinsic activity. Therefore, the preparation of suitable electrocatalytic supports is crucial.
目前常见的电催化碳载体包括碳纤维布、碳纤维纸等,结构简单,无法使催化剂暴露更多的活性位点。而泡沫镍、泡沫钴等催化剂载体在负载时难免会发生反应,为最终催化机理的研究带来困难。其他催化剂载体如硅基载体等也难以兼顾导电性与高负载量。因此提供一种既能保持良好的稳定性及导电性外,也能通过暴露更多活性位点、提升传质来提升催化剂性能的电催化剂载体具有十分重要的现实意义。At present, common electrocatalytic carbon supports include carbon fiber cloth, carbon fiber paper, etc., which have a simple structure and cannot expose more active sites to the catalyst. However, catalyst supports such as foamed nickel and foamed cobalt will inevitably react when loaded, which brings difficulties to the study of the final catalytic mechanism. It is also difficult for other catalyst supports, such as silicon-based supports, to achieve both electrical conductivity and high loading. Therefore, it is of great practical significance to provide an electrocatalyst support that can not only maintain good stability and conductivity, but also improve the catalyst performance by exposing more active sites and improving mass transfer.
发明内容SUMMARY OF THE INVENTION
本发明要解决的技术问题是提供一种碳纳米半球颗粒的制备方法;该制备方法合成的碳纳米半球粉末颗粒分布均匀、大小均一、形貌整齐且结构真空、粒径范围 300-350纳米;该碳纳米半球在保证良好的导电性的同时拥有更大的比表面积,使得负载上的催化剂暴露更多活性位点,同时存在介孔促进传质,是良好的催化剂载体材料。The technical problem to be solved by the present invention is to provide a preparation method of carbon nano hemispherical particles; the carbon nano hemispherical powder particles synthesized by the preparation method have uniform distribution, uniform size, neat appearance, vacuum structure, and a particle size range of 300-350 nanometers; The carbon nano-hemisphere has a larger specific surface area while ensuring good electrical conductivity, so that the supported catalyst exposes more active sites, and at the same time, the presence of mesopores promotes mass transfer, which is a good catalyst carrier material.
为解决上述第一个技术问题,本发明采用如下的技术方案:In order to solve the above-mentioned first technical problem, the present invention adopts the following technical scheme:
一种碳纳米半球颗粒的制备方法,包括如下步骤:A preparation method of carbon nano hemispherical particles, comprising the following steps:
1)将有机硅加入乙醇溶液中搅拌使其均匀分散,得溶液A;1) adding the organosilicon to the ethanol solution and stirring to make it evenly dispersed to obtain solution A;
2)配置碱水溶液,然后将其加入到溶液A中,得到溶液B;2) configure aqueous alkali solution, then add it to solution A to obtain solution B;
3)加热搅拌溶液B进行水解反应,待溶液转变至乳白色后,得到溶液C;加入间苯二酚和甲醛到溶液C中进行酚醛缩合反应,搅拌使酚醛缩合产物均匀包覆在溶液C中形成的硅球模板上,得到混合反应液;3) heating and stirring solution B to carry out hydrolysis reaction, after the solution is transformed into milky white, solution C is obtained; adding resorcinol and formaldehyde to solution C to carry out phenolic condensation reaction, stirring makes the phenolic condensation product evenly coated in solution C to form On the silicon sphere template, the mixed reaction solution was obtained;
4)将混合反应液离心洗涤,将离心洗涤后得到的固体在真空干燥箱内烘干,得到红棕色或浅棕色固体,然后将红棕色或浅棕色固体研磨得到中间产物D;4) the mixed reaction solution is centrifugally washed, and the solid obtained after the centrifugal washing is dried in a vacuum drying oven to obtain a reddish-brown or light-brown solid, and then the reddish-brown or light-brown solid is ground to obtain intermediate product D;
5)在惰性气氛条件下,在管式炉中采用高温煅烧使中间产物D表面包覆层完全碳化,得到碳化后的中间产物E;5) Under the condition of inert atmosphere, high temperature calcination is adopted in the tube furnace to completely carbonize the surface coating of the intermediate product D to obtain the carbonized intermediate product E;
6)将中间产物E取出,置于刻蚀液中搅拌刻蚀,刻蚀后进行抽滤并洗涤至中性,得到中间产物F;6) taking out the intermediate product E, placing it in the etching solution with stirring and etching, performing suction filtration and washing to neutrality after the etching to obtain the intermediate product F;
7)将中间产物F在真空干燥箱中干燥后,研磨得到本发明产物碳纳米半球颗粒。7) After drying the intermediate product F in a vacuum drying oven, grinding to obtain carbon nano hemispherical particles of the product of the present invention.
作为技术方案的进一步改进,步骤1)中,所述有机硅选自正硅酸丙酯、四丙氧基硅烷、正硅酸四乙酯中的一种或多种。As a further improvement of the technical solution, in step 1), the organosilicon is selected from one or more of propyl orthosilicate, tetrapropoxysilane, and tetraethyl orthosilicate.
优选地,步骤1)中,所述有机硅用量为3-12mL;无水乙醇用量为70-150mL。Preferably, in step 1), the amount of the organosilicon is 3-12mL; the amount of anhydrous ethanol is 70-150mL.
作为技术方案的进一步改进,步骤2)中,所述碱选自浓氨水、氢氧化钠或赖氨酸。As a further improvement of the technical solution, in step 2), the alkali is selected from concentrated ammonia, sodium hydroxide or lysine.
优选地,步骤2)中,所述碱水溶液的浓度为25-30wt%,用量为2-10mL。Preferably, in step 2), the concentration of the alkaline aqueous solution is 25-30 wt %, and the dosage is 2-10 mL.
作为技术方案的进一步改进,步骤3)中,所述加热搅拌的温度为25-40℃;且反应过程中密封。As a further improvement of the technical solution, in step 3), the temperature of the heating and stirring is 25-40° C.; and it is sealed during the reaction.
优选地,步骤3)中,所述加热搅拌使用水浴锅进行;加热搅拌的时间为10-40 分钟。Preferably, in step 3), the heating and stirring are performed using a water bath; the heating and stirring time is 10-40 minutes.
优选地,步骤3)中,所述甲醛来自18wt%的甲醛水溶液,其中含有5-8wt%的甲醇稳定剂,且甲醛水溶液的用量为0.56-1.4mL;所述间苯二酚的用量为0.4-1g。Preferably, in step 3), the formaldehyde comes from 18wt% formaldehyde solution, which contains 5-8wt% methanol stabilizer, and the amount of the formaldehyde solution is 0.56-1.4mL; the amount of the resorcinol is 0.4 mL -1g.
优选地,步骤3)中,所述酚醛缩合反应的反应时间为3-24h。Preferably, in step 3), the reaction time of the phenolic condensation reaction is 3-24h.
作为技术方案的进一步改进,步骤4)中,所述离心洗涤是指先后用去离子水和无水乙醇超声洗涤并离心分离,至离心后上次液体无水澄清透明为止。所述离心的转速为1000-6000rpm。As a further improvement of the technical solution, in step 4), the centrifugal washing refers to ultrasonic washing and centrifugal separation with deionized water and absolute ethanol successively, until the last time the liquid is anhydrous and clear after centrifugation. The rotation speed of the centrifugation is 1000-6000 rpm.
优选地,步骤4)中,所述真空干燥箱内的真空度为0.08-0.12MPa。Preferably, in step 4), the vacuum degree in the vacuum drying box is 0.08-0.12MPa.
作为技术方案的进一步改进,步骤5)中,所述惰性气氛为氮气或氦气。As a further improvement of the technical solution, in step 5), the inert atmosphere is nitrogen or helium.
优选地,步骤5)中,所述高温煅烧的温度为700-900℃,升温梯度为1-10K/min,时间为1-2h。Preferably, in step 5), the temperature of the high-temperature calcination is 700-900° C., the heating gradient is 1-10K/min, and the time is 1-2h.
作为技术方案的进一步改进,步骤6)中,所述刻蚀液选自氢氧化钠溶液或氢氟酸溶液。As a further improvement of the technical solution, in step 6), the etching solution is selected from sodium hydroxide solution or hydrofluoric acid solution.
优选地,步骤6)中,所述刻蚀液采用氢氧化钠溶液时,其浓度为3-5M。Preferably, in step 6), when the etching solution is a sodium hydroxide solution, its concentration is 3-5M.
优选地,步骤6)中,所述搅拌刻蚀的温度为78-82℃,时间为8-24h。Preferably, in step 6), the temperature of the stirring etching is 78-82° C. and the time is 8-24 h.
作为技术方案的进一步改进,步骤7)中,所述真空干燥箱内的真空度为0.08-0.12MPa。As a further improvement of the technical solution, in step 7), the vacuum degree in the vacuum drying box is 0.08-0.12MPa.
优选地,步骤7)中,所述真空干燥箱内的温度为40-70℃,烘干时间为12-24h。Preferably, in step 7), the temperature in the vacuum drying box is 40-70°C, and the drying time is 12-24h.
本发明所记载的任何范围包括端值以及端值之间的任何数值以及端值或者端值之间的任意数值所构成的任意子范围。Any range recited herein includes the endpoints and any number between the endpoints and any sub-ranges formed by the endpoints or any number between the endpoints.
如无特殊说明,本发明中的各原料均可通过市售购买获得,本发明中所用的设备可采用所属领域中的常规设备或参照所属领域的现有技术进行。Unless otherwise specified, each raw material in the present invention can be obtained through commercial purchase, and the equipment used in the present invention can be performed with conventional equipment in the field or with reference to the prior art in the field.
与现有技术相比较,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
本发明通过使用去模板法合成了一种新型的碳纳米半球颗粒,用做电催化剂载体。总体合成思路为碱性水解有机硅合成二氧化硅模板,利用酚醛反应在上面包覆有机层。再利用高温煅烧将有机层碳化后将二氧化硅模板刻蚀掉,最终形成规整均一的碳纳米半球。合成过程中通过改变条件能够很好地调控合成效果。精确调控条件使得碳纳米球从中间破裂塌陷,反而能够进一步增大催化剂的负载面积。合成的碳纳米半球粉末颗粒分布均匀、大小均一、形貌整齐且结构真空、粒径范围300-350纳米,同时球体表面布有介孔,既能为催化剂提供较高的比表面积,也具备良好的传质能力。该种方法便捷简单,为电催化剂的研究提供了一种良好的载体选择。In the present invention, a new type of carbon nano hemispherical particle is synthesized by using a template removal method, which is used as an electrocatalyst carrier. The general synthesis idea is to synthesize silica template by alkaline hydrolysis of organosilicon, and use phenolic reaction to coat the organic layer on it. Then, the organic layer is carbonized by high temperature calcination, and then the silicon dioxide template is etched away, and finally a regular and uniform carbon nano hemisphere is formed. The synthesis effect can be well controlled by changing the conditions during the synthesis. Precisely adjusting the conditions makes the carbon nanospheres collapse and collapse from the middle, which can further increase the loading area of the catalyst. The synthesized carbon nano-hemispherical powder has uniform particle distribution, uniform size, neat morphology and vacuum structure, and the particle size range is 300-350 nanometers. At the same time, the surface of the sphere is covered with mesopores, which can not only provide a high specific surface area for the catalyst, but also have good mass transfer capacity. This method is convenient and simple, and provides a good carrier choice for the study of electrocatalysts.
附图说明Description of drawings
下面结合附图对本发明的具体实施方式作进一步详细的说明The specific embodiments of the present invention will be described in further detail below in conjunction with the accompanying drawings.
图1为实施例1制得样品的BJH孔径分布曲线;Fig. 1 is the BJH pore size distribution curve of the sample obtained in Example 1;
图2为实施例1制得样品的透射电子显微镜图;Fig. 2 is the transmission electron microscope picture of the sample obtained in Example 1;
图3为实施例1制得样品的XRD谱图;Fig. 3 is the XRD spectrum of the sample obtained in Example 1;
图4为对比例1所制得样品的透射电子显微镜图;Fig. 4 is the transmission electron microscope picture of the prepared sample of Comparative Example 1;
图5为对比例2所制得样品的扫描电子显微镜图;Fig. 5 is the scanning electron microscope picture of the prepared sample of Comparative Example 2;
图6为对比例2所制得样品的透射电子显微镜谱图;Fig. 6 is the transmission electron microscope spectrogram of the prepared sample of Comparative Example 2;
图7为对比例3所制得样品的扫描电子显微镜谱图;Fig. 7 is the scanning electron microscope spectrogram of the prepared sample of Comparative Example 3;
图8为对比例5所制得样品的透射电子显微镜谱图。FIG. 8 is a transmission electron microscope spectrum of the sample prepared in Comparative Example 5. FIG.
具体实施方式Detailed ways
为了更清楚地说明本发明,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。In order to illustrate the present invention more clearly, the present invention will be further described below with reference to the 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.
作为本发明的一个方面,本发明一种碳纳米半球颗粒的制备方法,包括如下步骤:As an aspect of the present invention, a preparation method of carbon nano hemispherical particles of the present invention comprises the following steps:
1)将有机硅加入乙醇溶液中搅拌使其均匀分散,得溶液A;1) adding the organosilicon to the ethanol solution and stirring to make it evenly dispersed to obtain solution A;
2)配置碱水溶液,然后将其加入到溶液A中,得到溶液B;2) configure aqueous alkali solution, then add it to solution A to obtain solution B;
3)加热搅拌溶液B进行水解反应,待溶液转变至乳白色后,得到溶液C;加入间苯二酚和甲醛到溶液C中进行酚醛缩合反应,搅拌使酚醛缩合产物均匀包覆在溶液C中形成的硅球模板上,得到混合反应液;3) heating and stirring solution B to carry out hydrolysis reaction, after the solution is transformed into milky white, solution C is obtained; adding resorcinol and formaldehyde to solution C to carry out phenolic condensation reaction, stirring makes the phenolic condensation product evenly coated in solution C to form On the silicon sphere template, the mixed reaction solution was obtained;
4)将混合反应液离心洗涤,将离心洗涤后得到的固体在真空干燥箱内烘干,得到红棕色或浅棕色固体,然后将红棕色或浅棕色固体研磨得到中间产物D;4) the mixed reaction solution is centrifugally washed, and the solid obtained after the centrifugal washing is dried in a vacuum drying oven to obtain a reddish-brown or light-brown solid, and then the reddish-brown or light-brown solid is ground to obtain intermediate product D;
5)在惰性气氛条件下,在管式炉中采用高温煅烧使中间产物D表面包覆层完全碳化,得到碳化后的中间产物E;5) Under the condition of inert atmosphere, high temperature calcination is adopted in the tube furnace to completely carbonize the surface coating of the intermediate product D to obtain the carbonized intermediate product E;
6)将中间产物E取出,置于刻蚀液中搅拌刻蚀,刻蚀后进行抽滤并洗涤至中性,得到中间产物F;6) taking out the intermediate product E, placing it in the etching solution with stirring and etching, performing suction filtration and washing to neutrality after the etching to obtain the intermediate product F;
7)将中间产物F在真空干燥箱中干燥后,研磨得到本发明产物碳纳米半球颗粒。7) After drying the intermediate product F in a vacuum drying oven, grinding to obtain carbon nano hemispherical particles of the product of the present invention.
作为技术方案的进一步改进,步骤1)中,所述有机硅选自正硅酸丙酯、四丙氧基硅烷、正硅酸四乙酯中的一种或多种。优选地,所述有机硅是正硅酸丙酯,使用正硅酸四乙酯作为硅源更有利于调控,提高正硅酸四乙酯的用量会加速二氧化硅结晶,最终形成的碳纳米半球内径增加。As a further improvement of the technical solution, in step 1), the organosilicon is selected from one or more of propyl orthosilicate, tetrapropoxysilane, and tetraethyl orthosilicate. Preferably, the organosilicon is propyl orthosilicate, and using tetraethyl orthosilicate as the silicon source is more conducive to regulation, and increasing the amount of tetraethyl orthosilicate will accelerate the crystallization of silicon dioxide, and the carbon nano hemispheres formed finally The inner diameter is increased.
优选地,步骤1)中,所述有机硅用量为3-12mL;无水乙醇用量为70-150mL。Preferably, in step 1), the amount of the organosilicon is 3-12mL; the amount of anhydrous ethanol is 70-150mL.
作为技术方案的进一步改进,步骤2)中,所述碱选自浓氨水、氢氧化钠或赖氨酸。As a further improvement of the technical solution, in step 2), the alkali is selected from concentrated ammonia, sodium hydroxide or lysine.
优选地,步骤2)中,所述碱水溶液的浓度为25-30wt%,用量为2-10mL。Preferably, in step 2), the concentration of the alkaline aqueous solution is 25-30 wt %, and the dosage is 2-10 mL.
作为技术方案的进一步改进,步骤3)中,所述加热搅拌的温度为25-40℃;且反应过程中密封;进行密封有助于防止有机硅挥发。As a further improvement of the technical solution, in step 3), the temperature of the heating and stirring is 25-40° C.; and sealing is performed during the reaction; sealing is helpful to prevent organic silicon from volatilizing.
优选地,步骤3)中,所述加热搅拌使用水浴锅进行,使合成过程更可控;加热搅拌的时间为10-40分钟。所述加热搅拌时长会影响硅酸水解和结晶程度,进而影响硅球模板及后续碳球的粒径。Preferably, in step 3), the heating and stirring are performed in a water bath, so that the synthesis process is more controllable; the heating and stirring time is 10-40 minutes. The heating and stirring time will affect the degree of hydrolysis and crystallization of silicic acid, thereby affecting the particle size of the silicon sphere template and subsequent carbon spheres.
优选地,步骤3)中,所述甲醛来自18wt%的甲醛水溶液,其中含有5-8wt%的甲醇稳定剂,且甲醛水溶液的用量为0.56-1.4mL;所述间苯二酚的用量为0.4-1g。先后加入间苯二酚和甲醛后溶液颜色由起初的澄清透明迅速变为乳白色再缓慢转变为红棕色最终变为深棕色,使缩合反应进行完全实现良好的调控,通过改变不同比例下甲醛和间苯二酚的用量可调节最终形成碳层的厚度。Preferably, in step 3), the formaldehyde comes from 18wt% formaldehyde solution, which contains 5-8wt% methanol stabilizer, and the amount of the formaldehyde solution is 0.56-1.4mL; the amount of the resorcinol is 0.4 mL -1g. After adding resorcinol and formaldehyde successively, the color of the solution changed from clear and transparent at first to milky white and then slowly changed to reddish brown and finally to dark brown, so that the condensation reaction was completely and well regulated. The amount of diphenol used can adjust the thickness of the finally formed carbon layer.
优选地,步骤3)中,所述酚醛缩合反应的反应时间为3-24h。Preferably, in step 3), the reaction time of the phenolic condensation reaction is 3-24h.
作为技术方案的进一步改进,步骤4)中,所述离心洗涤是指先后用去离子水和无水乙醇超声洗涤并离心分离,至离心后上次液体无水澄清透明为止。As a further improvement of the technical solution, in step 4), the centrifugal washing refers to ultrasonic washing and centrifugal separation with deionized water and absolute ethanol successively, until the last time the liquid is anhydrous and clear after centrifugation.
优选地,步骤4)中,所述真空干燥箱内的真空度为0.08-0.12MPa。Preferably, in step 4), the vacuum degree in the vacuum drying box is 0.08-0.12MPa.
在某些实施例中,步骤5)中,所述惰性气氛为氮气或氦气。In some embodiments, in step 5), the inert atmosphere is nitrogen or helium.
在某些实施例中,步骤5)中,所述高温煅烧的温度为700-900℃,升温梯度为 1-10K/min,时间为1-2h。In certain embodiments, in step 5), the temperature of the high-temperature calcination is 700-900° C., the heating gradient is 1-10K/min, and the time is 1-2h.
在某些实施例中,步骤6)中,所述刻蚀液选自氢氧化钠溶液或氢氟酸溶液。In some embodiments, in step 6), the etching solution is selected from sodium hydroxide solution or hydrofluoric acid solution.
在某些实施例中,步骤6)中,所述刻蚀液采用氢氧化钠溶液时,其浓度为3-5M。In some embodiments, in step 6), when the etching solution is a sodium hydroxide solution, its concentration is 3-5M.
在某些实施例中,步骤6)中,所述搅拌刻蚀的温度为78-82℃,时间为8-24h。In some embodiments, in step 6), the temperature of the stirring etching is 78-82° C., and the time is 8-24 h.
在某些实施例中,步骤7)中,所述真空干燥箱内的真空度为0.08-0.12MPa。In certain embodiments, in step 7), the vacuum degree in the vacuum drying box is 0.08-0.12 MPa.
在某些实施例中,步骤7)中,所述真空干燥箱内的温度为40-70℃,烘干时间为12-24h。In some embodiments, in step 7), the temperature in the vacuum drying box is 40-70° C., and the drying time is 12-24 h.
本发明通过使用去模板法合成了一种新型的碳纳米半球用以电催化剂载体。合成过程中通过改变条件能够很好地调控合成效果。精确调控条件使得碳纳米球从中间破裂塌陷,反而能够进一步增大催化剂的负载面积。合成的碳纳米半球粉末颗粒分布均匀、大小均一、形貌整齐且结构真空、粒径范围300-350纳米,同时球体表面布有介孔,既能为催化剂提供较高的比表面积,也具备良好的传质能力。该种方法便捷可行,为电催化剂的研究提供了一种良好的载体选择。In the present invention, a new type of carbon nano hemisphere is synthesized by using the template removal method for electrocatalyst carrier. The synthesis effect can be well controlled by changing the conditions during the synthesis. Precisely adjusting the conditions makes the carbon nanospheres collapse and collapse from the middle, which can further increase the loading area of the catalyst. The synthesized carbon nano-hemispherical powder has uniform particle distribution, uniform size, neat morphology and vacuum structure, and the particle size range is 300-350 nanometers. At the same time, the surface of the sphere is covered with mesopores, which can not only provide a high specific surface area for the catalyst, but also have good mass transfer capacity. This method is convenient and feasible, and provides a good carrier choice for the study of electrocatalysts.
实施例1Example 1
一种碳纳米半球材料的制备方法,包括如下步骤:A preparation method of carbon nano-hemisphere material, comprising the following steps:
1)量筒称取70mL无水乙醇加入烧杯中,使用移液枪移取3.5mL正硅酸四乙酯加入乙醇溶液中并放入磁子进行搅拌至完全分散并保持搅拌待用;1) Weigh 70mL of absolute ethanol into the beaker with a measuring cylinder, use a pipette to pipette 3.5mL of tetraethyl orthosilicate into the ethanol solution and put it into the magnetic element to stir until it is completely dispersed and keep stirring for later use;
2)称取3mL的28wt%浓氨水溶液加入到10mL去离子水中进行超声至均匀分散;2) Weigh 3mL of 28wt% concentrated ammonia solution and add it to 10mL of deionized water for ultrasonication until uniform dispersion;
3)将氨水溶液加入到正硅酸四乙酯的乙醇溶液中将混合溶液在水浴锅中加热维持在40℃并进行磁力搅拌,搅拌20分钟至溶液即将转变为乳白色。搅拌时注意用封口膜封装烧杯进行密封,防止有毒的正硅酸四乙酯挥发。氨水加入及加热搅拌使得正硅酸四乙酯进行水解,加热搅拌的时间会影响最终形成的二氧化硅模板的粒径,根据 pH值与硅源含量进行调整;3) The ammonia solution was added to the ethanol solution of tetraethyl orthosilicate, the mixed solution was heated in a water bath and maintained at 40°C and magnetically stirred, and stirred for 20 minutes until the solution was about to turn milky white. When stirring, pay attention to sealing the beaker with parafilm to prevent the volatilization of toxic tetraethyl orthosilicate. The addition of ammonia water and heating and stirring make tetraethyl orthosilicate hydrolyze, and the time of heating and stirring will affect the particle size of the finally formed silica template, which is adjusted according to pH value and silicon source content;
4)使用电子天平称取0.8g间苯二酚、使用移液枪量取1.2mL甲醛溶液加入到混合溶液中进行酚醛缩合反应并搅拌24h使其均匀包覆在硅球模板上;先后加入间苯二酚和甲醛后溶液颜色由起初的澄清透明迅速变为乳白色再缓慢转变为红棕色最终变为深棕色,表示二氧化硅成核结晶后酚醛缩合包覆在二氧化硅;4) Use an electronic balance to weigh 0.8g of resorcinol, use a pipette to measure 1.2mL of formaldehyde solution, add it to the mixed solution for phenolic condensation reaction, and stir for 24h to make it evenly coated on the silicon sphere template; After quinone and formaldehyde, the color of the solution changed from clear and transparent at first to milky white and then slowly to reddish brown and finally to dark brown, indicating that the phenolic condensation of silica was coated on silica after nucleation and crystallization of silica;
5)将混合溶液转移至离心管中8000rpm离心,离心分层后倒去上层红色透明液体,加入去离子水进行超声至分散,再次离心洗去残留的氨等;继续倒去上层液体并加入无水乙醇,超声分散后离心洗去残留的酚、醛等,重复进行无水乙醇离心洗涤至上层液体透明无色;5) Transfer the mixed solution to a centrifuge tube and centrifuge at 8000 rpm. After centrifugation and stratification, pour off the upper layer of red transparent liquid, add deionized water for ultrasonication to disperse, and centrifuge again to wash off residual ammonia, etc.; continue to pour out the upper layer liquid and add no Water ethanol, after ultrasonic dispersion, centrifugal washing to remove residual phenol, aldehyde, etc., repeat centrifugal washing with absolute ethanol until the upper liquid is transparent and colorless;
6)将最好离心后的下层固体在真空干燥箱中70℃真空干燥12h,烘箱内的真空度需保持在0.08-0.12MPa以下,干燥后呈现红棕色或浅棕色固体。使用研钵将其研磨成均匀棕色粉末,以便碳化均匀;6) Dry the bottom solid after centrifugation in a vacuum drying oven at 70℃ for 12h. The vacuum degree in the oven should be kept below 0.08-0.12MPa, and it will appear reddish-brown or light-brown solid after drying. Use a mortar and pestle to grind it into a uniform brown powder for uniform carbonization;
7)将粉末转移至瓷舟中放进管式炉,管式炉先通入惰性气体1-2h,未排出内部氧气可能会导致碳氧化挥发。然后以5K/min升温至900摄氏度,保持2h进行高温煅烧,使材料表面包覆层完全碳化,再冷却至室温取出待用;7) Transfer the powder to the porcelain boat and put it into the tube furnace. The tube furnace is first filled with inert gas for 1-2 hours. If the internal oxygen is not discharged, it may cause carbon oxidation and volatilization. Then, the temperature was raised to 900 degrees Celsius at 5K/min, and calcined at high temperature for 2 hours to completely carbonize the coating layer on the surface of the material, and then cooled to room temperature and taken out for use;
8)取30.93g氢氧化钠置于烧杯,加入250mL去离子水,并放入磁子,磁力搅拌直至完全溶解,配制成3mol/L的NaOH溶液;8) Take 30.93g of sodium hydroxide and place it in a beaker, add 250mL of deionized water, and put in a magnet, stir magnetically until it is completely dissolved, and prepare a 3mol/L NaOH solution;
9)将碳化后的粉末取出置于NaOH溶液中在80℃下进行加热搅拌,加热搅拌时注意用封口膜对烧杯进行密封,搅拌24h至完全刻蚀;9) Take out the carbonized powder and place it in a NaOH solution for heating and stirring at 80°C. When heating and stirring, pay attention to sealing the beaker with a sealing film, and stir for 24 hours until it is completely etched;
10)将刻蚀后的混合溶液进行抽滤。抽滤完成时继续加入去离子水进行多次抽滤洗涤,直至呈现中性,洗去残留氢氧化钠;10) Suction filtration of the etched mixed solution. When the suction filtration is completed, continue to add deionized water to carry out suction filtration and washing for several times until it is neutral, and the residual sodium hydroxide is washed away;
11)将抽滤后的样品在真空干燥箱干燥中40℃干燥24h,干燥完全后使用研钵进行研磨得到碳纳米半球颗粒。11) Dry the sample after suction filtration at 40° C. for 24 hours in a vacuum drying oven, and grind it with a mortar to obtain carbon nano-hemispherical particles.
图1所示为本实施例1制得产品的BJH孔径分布曲线,可以看出,该碳半球颗粒表面分布有微孔、介孔,具有良好的传质能力,BET测试也表明其具有较大的比表面积(550-700m2/g)。Figure 1 shows the BJH pore size distribution curve of the product prepared in Example 1. It can be seen that the surface of the carbon hemispherical particles is distributed with micropores and mesopores, and has good mass transfer ability. BET test also shows that it has a large The specific surface area (550-700m 2 /g).
图2所示为本实施例1制得产品的透射电子显微镜图,经低倍透射显微镜检测,本实施例获得的碳纳米半球材料尺寸均一,300-350纳米左右,结构规整且稳定。Figure 2 shows the transmission electron microscope image of the product obtained in Example 1. After low-power transmission microscope detection, the carbon nano-hemisphere material obtained in this example has a uniform size, about 300-350 nanometers, and has a regular and stable structure.
图3所示为实施例1制得样品的XRD谱图,据图可知,该材料为无定形碳,说明硅模板已经被基本去除;说明该载体既不会因为硅等影响性能,又能提供大量的表面积及优秀的传质能力,是电催化剂优异载体;由此,说明此方法的适用性。Figure 3 shows the XRD spectrum of the sample prepared in Example 1. According to the figure, the material is amorphous carbon, indicating that the silicon template has been basically removed; it indicates that the carrier will not affect the performance due to silicon, etc., and can provide The large surface area and excellent mass transfer capacity make it an excellent carrier for electrocatalysts; thus, the applicability of this method is demonstrated.
实施例2Example 2
重复实施例1,其不用之处仅在于,步骤1)中使用正硅酸丙酯(TPOS)。Example 1 was repeated except that propyl orthosilicate (TPOS) was used in step 1).
实施例3Example 3
重复实施例1,其不同之处仅在于,步骤2)中使用氢氧化钠或赖氨酸调节pH。Example 1 was repeated, except that in step 2) sodium hydroxide or lysine was used to adjust the pH.
实施例4Example 4
重复实施例1,其不同之处仅在于,步骤8)中使用HF进行刻蚀。取5mL氢氟酸溶于25mL去离子水在塑料离心管中配置溶液。取0.5g碳化后粉末加入配置的溶液并加入磁子进行磁力搅拌。需要注意的是,搅拌时离心管密封并置于通风厨,无需进行加热。Example 1 was repeated, except that HF was used for etching in step 8). Dissolve 5 mL of hydrofluoric acid in 25 mL of deionized water and prepare the solution in a plastic centrifuge tube. Add 0.5 g of carbonized powder to the prepared solution and add a magnet for magnetic stirring. It should be noted that the centrifuge tube is sealed and placed in the fume hood during stirring, and no heating is required.
对比例1Comparative Example 1
重复实施例1,其不同之处仅在于,将步骤4)中的间苯二酚改为0.4g,甲醛溶液改为0.56mL。Example 1 was repeated, except that the resorcinol in step 4) was changed to 0.4 g, and the formaldehyde solution was changed to 0.56 mL.
如图4所示,经低倍透射显微镜检测,此种方法获得的碳球催化剂载体由于外层碳层过薄,进行了不规则的塌陷,最终难以支撑半球的形貌结构。As shown in Figure 4, the low-power transmission microscope test shows that the carbon spherical catalyst support obtained by this method undergoes irregular collapse because the outer carbon layer is too thin, and finally it is difficult to support the hemispherical morphology structure.
对比例2Comparative Example 2
重复实施例1,其不同之处仅在于,提高步骤4)中间苯二酚的用量至1.6g、甲醛溶液的用量为2.4mL。Example 1 was repeated, and the difference was only in that step 4) the consumption of resorcinol was increased to 1.6 g, and the consumption of formaldehyde solution was 2.4 mL.
由图5的SEM测试可以看出,此时呈现良好的球形。经透射电子显微镜检测,如图6所示,形成了规整均匀的碳纳米球,也可考虑作为形貌结构优异的中空碳纳米球电催化剂载体。但此时碳层厚度较厚,约为50nm,一定程度上约束了催化剂的负载量。It can be seen from the SEM test in Fig. 5 that a good spherical shape is present at this time. Through transmission electron microscopy, as shown in Figure 6, regular and uniform carbon nanospheres were formed, which can also be considered as hollow carbon nanospheres electrocatalyst carriers with excellent morphology and structure. However, at this time, the thickness of the carbon layer is relatively thick, about 50 nm, which limits the catalyst loading to a certain extent.
对比例3Comparative Example 3
重复对比例1,其不同之处仅在于,步骤4)中,在搅拌3h过后就将其静置待离心洗涤。The comparative example 1 was repeated, except that in step 4), after stirring for 3 h, it was left to stand for centrifugal washing.
由图7的SEM测试可以看出,由于搅拌时间过短,酚醛形成的有机层难以进行均匀的包覆。说明无法通过减少搅拌时间对对比例2进行优化,优选的方法是减少酚和醛的用量。It can be seen from the SEM test in Fig. 7 that due to the short stirring time, it is difficult for the organic layer formed by phenolic aldehyde to be uniformly coated. It shows that the optimization of Comparative Example 2 cannot be achieved by reducing the stirring time, and the preferred method is to reduce the amount of phenol and aldehyde.
经检测,得到的Ag纳米颗粒在取不同样品进行检测时,呈现出差异性的Ag分布情况和含量。After testing, the obtained Ag nanoparticles showed different Ag distribution and content when different samples were taken for testing.
对比例4Comparative Example 4
重复实施例1,不同之处仅在于,步骤6)中,煅烧的温度改为70℃,保持1h 后等待自然降温。Example 1 was repeated, the only difference was that in step 6), the calcination temperature was changed to 70° C., kept for 1 h, and then waited for natural cooling.
此条件煅烧后的粉末时常呈现墨绿色。可以推断,该条件下的碳球尚未完全碳化,对后期催化剂的负载带来不可控的变量。The powder calcined under this condition often appears dark green. It can be inferred that the carbon spheres under this condition have not been fully carbonized, which brings uncontrollable variables to the catalyst loading in the later stage.
对比例5Comparative Example 5
重复实施例1,其不同之处仅在于,步骤10)中,降低NaOH溶液的浓度或停止加热搅拌。Example 1 was repeated, except that, in step 10), the concentration of the NaOH solution was reduced or the heating and stirring were stopped.
经图8的低倍透射显微镜检测,得到的纳米颗粒为实心球形。可以推断,该条件下的碳球内部二氧化硅模板并未刻蚀完全,碳球无法破裂形成半球型,硅的存在也极大影响了碳球的性能。Detected by the low-power transmission microscope in FIG. 8 , the obtained nanoparticles are solid spherical. It can be inferred that the silicon dioxide template inside the carbon spheres under these conditions is not completely etched, the carbon spheres cannot be broken to form a hemispherical shape, and the presence of silicon also greatly affects the performance of the carbon spheres.
对比例6Comparative Example 6
重复实施例1中步骤1-5,其不同之处仅在于,步骤4)中,不加入间苯二酚与甲醛溶液而直接搅拌24h后进行离心洗涤。Steps 1-5 in Example 1 were repeated, except that, in step 4), without adding resorcinol and formaldehyde solution, the solution was directly stirred for 24h and then centrifuged and washed.
搅拌24h过程中溶液转变为乳白色后并未发生变色,表明溶液由乳白色缓慢转变为红棕色最终变为深棕色的过程确实为酚醛缩合包覆的过程。将溶液进行离心洗涤干燥后得到白色粉末产品。经检测,最终产品为纯二氧化硅颗粒,表明如果不进行酚醛缩合包覆则无法形成碳层。During stirring for 24h, the solution turned milky white and did not change color, indicating that the process of the solution slowly changing from milky white to reddish brown and finally to dark brown was indeed a process of phenolic condensation coating. The solution was centrifuged, washed and dried to obtain a white powder product. After testing, the final product was pure silica particles, indicating that the carbon layer could not be formed without phenolic condensation coating.
综上所述,本发明的一种碳纳米半球材料的制备方法,模板硅源的选择、酚醛缩合的用量、真空条件、刻蚀的条件、煅烧碳化时的温度与时间等,相互协调、相互配合形成一个完整的技术方案,才可以制得本发明要求的一种碳纳米半球材料催化剂。To sum up, the preparation method of a carbon nano hemisphere material of the present invention, the selection of template silicon source, the amount of phenolic condensation, the vacuum conditions, the etching conditions, the temperature and time during calcination and carbonization, etc., are coordinated and mutually compatible. Only when a complete technical solution is formed, the carbon nano-hemisphere material catalyst required by the present invention can be prepared.
显然,本发明的上述实施例仅仅是为清楚地说明本发明所作的举例,而并非是对本发明的实施方式的限定。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无法对所有的实施方式予以穷举。凡是属于本发明的技术方案所引伸出的显而易见的变化或变动仍处于本发明的保护范围之列。Obviously, the above-mentioned embodiments of the present invention are only examples for clearly illustrating the present invention, and are not intended to limit the embodiments of the present invention. For those of ordinary skill in the art, changes or modifications in other different forms can also be made on the basis of the above description. Not all implementations can be exhaustive here. Any obvious changes or changes derived from the technical solutions of the present invention are still within the protection scope of the present invention.
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