CN112158822B - Preparation method of porous carbon microsphere - Google Patents
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 39
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 39
- 239000004005 microsphere Substances 0.000 title claims abstract description 39
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 229920005989 resin Polymers 0.000 claims abstract description 44
- 239000011347 resin Substances 0.000 claims abstract description 44
- 239000000839 emulsion Substances 0.000 claims abstract description 34
- 238000010438 heat treatment Methods 0.000 claims abstract description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 238000003756 stirring Methods 0.000 claims abstract description 27
- 239000003094 microcapsule Substances 0.000 claims abstract description 20
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 19
- 229920002545 silicone oil Polymers 0.000 claims abstract description 19
- 239000008367 deionised water Substances 0.000 claims abstract description 17
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 17
- 238000000197 pyrolysis Methods 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 10
- 239000011261 inert gas Substances 0.000 claims abstract description 5
- 238000002156 mixing Methods 0.000 claims abstract 3
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 claims description 23
- 229920001568 phenolic resin Polymers 0.000 claims description 23
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 14
- 239000003822 epoxy resin Substances 0.000 claims description 14
- 229920000647 polyepoxide Polymers 0.000 claims description 14
- 238000001035 drying Methods 0.000 claims description 13
- 238000003763 carbonization Methods 0.000 claims description 11
- 238000004321 preservation Methods 0.000 claims description 11
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 claims description 10
- 229910052786 argon Inorganic materials 0.000 claims description 7
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 claims description 3
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims description 3
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 claims description 3
- VILCJCGEZXAXTO-UHFFFAOYSA-N 2,2,2-tetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 claims description 2
- 239000005007 epoxy-phenolic resin Substances 0.000 claims description 2
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000011248 coating agent Substances 0.000 abstract 1
- 238000000576 coating method Methods 0.000 abstract 1
- 239000005011 phenolic resin Substances 0.000 description 21
- 239000011148 porous material Substances 0.000 description 18
- 238000010586 diagram Methods 0.000 description 10
- 239000000203 mixture Substances 0.000 description 6
- 238000001914 filtration Methods 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- 239000003575 carbonaceous material Substances 0.000 description 4
- 239000004593 Epoxy Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/05—Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
- Manufacturing Of Micro-Capsules (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
技术领域technical field
本发明属于多孔碳材料领域,具体涉及一种多孔碳微球的制备方法。The invention belongs to the field of porous carbon materials, and in particular relates to a preparation method of porous carbon microspheres.
背景技术Background technique
近年来多孔碳材料成为一种新型的快速发展起来的新型材料体系,在各个领域中的应用得到了广泛地关注,特别是在能源相关领域的应用。多孔材料因为结构上具有较高的孔隙率而具有一些相应的优异性能。众多的多孔材料中,多孔碳材料由于具有成本低、质量轻、无毒害、表面化学惰性、耐高温耐酸碱、高机械稳定性、良好的导电性、吸附性以及大的比表面积和孔体积等特点,在CO2吸附、储氢、催化以及燃料电池与电化学双电层电容器等领域显示出巨大的应用潜力而备受各界关注。In recent years, porous carbon materials have become a new type of rapidly developed new material system, and their applications in various fields have received extensive attention, especially in energy-related fields. Porous materials have some corresponding excellent properties due to their high porosity in structure. Among many porous materials, porous carbon materials are characterized by low cost, light weight, non-toxicity, surface chemical inertness, high temperature resistance, acid and alkali resistance, high mechanical stability, good electrical conductivity, adsorption, and large specific surface area and pore volume. And other characteristics, in the fields of CO2 adsorption, hydrogen storage, catalysis, and fuel cells and electrochemical double-layer capacitors, it has shown huge application potential and has attracted attention from all walks of life.
发明内容Contents of the invention
本发明旨在提供一种多孔碳微球的制备方法,该方法原料来源广,价格低廉,工艺简单,能耗低且环境友好,碳微球产率高,产业化前景好。The present invention aims to provide a method for preparing porous carbon microspheres, which has wide sources of raw materials, low price, simple process, low energy consumption, environmental friendliness, high yield of carbon microspheres, and good industrialization prospects.
本发明中,树脂与水不相溶,在树脂体积大于水的体积时,通过高速搅拌下可形成树脂包水乳液,整个乳液与连续相硅油不相溶,且硅油粘度较大,具有自乳化作用,因此当乳液加入连续相,搅拌可形成许多乳液微滴,待乳液微滴中的树脂固化将水包覆其中,即可形成树脂包水微胶囊。In the present invention, the resin is immiscible with water, and when the volume of the resin is greater than that of water, a water-in-resin emulsion can be formed under high-speed stirring. Therefore, when the emulsion is added to the continuous phase, many emulsion droplets can be formed by stirring. After the resin in the emulsion droplets solidifies and covers them with water, the water-in-resin microcapsules can be formed.
本发明提供了一种新型多孔碳微球的制备方法,该方法是将树脂与固化剂混合成一体,然后加入去离子水,高速搅拌形成乳液,再将乳液滴加入到到硅油中,高速搅拌形成树脂包水的微滴,加热使树脂固化从而形成树脂包水微胶囊,再对其进行高温热解炭化,最终制得多孔碳微球。The invention provides a preparation method of novel porous carbon microspheres. The method is to mix resin and curing agent into one, then add deionized water, stir at high speed to form an emulsion, then add the emulsion dropwise into silicone oil, and stir at high speed Water-in-resin droplets are formed, and the resin is cured by heating to form water-in-resin microcapsules, which are then subjected to high-temperature pyrolysis and carbonization to finally produce porous carbon microspheres.
上述的多孔碳微球的制备方法,具体包括以下步骤:The preparation method of the above-mentioned porous carbon microspheres specifically comprises the following steps:
(1)将树脂与固化剂混合组成均一相;(1) Mix the resin and curing agent to form a homogeneous phase;
(2)将去离子水加入到树脂均一相中,高速搅拌成乳液;(2) Add deionized water into the resin homogeneous phase and stir at high speed to form an emulsion;
(3)将乳液滴加到与硅油中,高速搅拌形成复相乳液;(3) Add the emulsion dropwise to the silicone oil, and stir at high speed to form a complex emulsion;
(4)加热复相乳液使树脂固化,制备树脂包水微胶囊;(4) Heating the multiphase emulsion to solidify the resin to prepare water-in-resin microcapsules;
(5)将过滤、洗涤、干燥后的树脂包水微胶囊置于惰性气体保护下,进行高温热解炭化,最终得到多孔碳微球。(5) Put the filtered, washed and dried water-in-resin microcapsules under the protection of an inert gas, and perform high-temperature pyrolysis and carbonization to finally obtain porous carbon microspheres.
进一步地,所述树脂为环氧树脂,酚醛树脂中的一种。Further, the resin is one of epoxy resin and phenolic resin.
进一步地,所述固化剂为乙二胺、二乙烯三胺、三乙烯四胺、对甲苯磺酸中的一种。Further, the curing agent is one of ethylenediamine, diethylenetriamine, triethylenetetramine, and p-toluenesulfonic acid.
进一步地,所述步骤(1)中,树脂与固化剂的质量比为100:7-100:13。Further, in the step (1), the mass ratio of the resin to the curing agent is 100:7-100:13.
进一步地,所述步骤(2)中,树脂与去离子水的质量比为100:50-100:70。Further, in the step (2), the mass ratio of resin to deionized water is 100:50-100:70.
进一步地,所述硅油为甲基硅油,粘度为100ps-2000ps,树脂与硅油的质量比为1:3-1:6。Further, the silicone oil is methyl silicone oil, the viscosity is 100ps-2000ps, and the mass ratio of resin to silicone oil is 1:3-1:6.
进一步地,所述搅拌速度为10000-30000r/min。Further, the stirring speed is 10000-30000r/min.
进一步地,所述步骤(4)中,加热温度为60-150℃,升温速率为1-5℃/min,保温时间为1-24h。Further, in the step (4), the heating temperature is 60-150°C, the heating rate is 1-5°C/min, and the holding time is 1-24h.
进一步地,所述步骤(5)中,干燥温度为40-80℃,时间为1-8h。Further, in the step (5), the drying temperature is 40-80° C., and the drying time is 1-8 hours.
进一步地,所述步骤(5)中,惰性气体为氩气。Further, in the step (5), the inert gas is argon.
进一步地,所述步骤(5)中,高温热解炭化的工艺条件为:在80-90℃,保温20-40min,然后升温到350-450℃,保温50-90min,再升温到600-1000℃,保温60-180min,升温速率为1-5℃/min。Further, in the step (5), the process conditions of high-temperature pyrolysis and carbonization are: at 80-90°C, keep warm for 20-40min, then raise the temperature to 350-450°C, keep warm for 50-90min, and then raise the temperature to 600-1000°C ℃, keep warm for 60-180min, and the heating rate is 1-5℃/min.
本发明的有益效果:Beneficial effects of the present invention:
本发明提供的新型多孔碳微球的制备方法,其工艺步骤简单,原料成本低,无污染,碳微球收率高,能耗低,对制备的环境条件和所用设备要求低,可简单快速高效的实现多孔碳微球的制备,为多孔碳材料的制备提供了一种新途径。The preparation method of the novel porous carbon microspheres provided by the present invention has simple process steps, low cost of raw materials, no pollution, high yield of carbon microspheres, low energy consumption, low requirements on the environmental conditions for preparation and equipment used, and can be simple and fast The efficient preparation of porous carbon microspheres provides a new way for the preparation of porous carbon materials.
附图说明Description of drawings
图1为本发明实施例1制备的碳微球的SEM图。FIG. 1 is an SEM image of carbon microspheres prepared in Example 1 of the present invention.
图2为本发明实施例1制备的碳微球的孔径分布图。Fig. 2 is a pore size distribution diagram of carbon microspheres prepared in Example 1 of the present invention.
图3为本发明实施例2制备的碳微球的孔径分布图。Fig. 3 is a pore size distribution diagram of carbon microspheres prepared in Example 2 of the present invention.
图4为本发明实施例3制备的碳微球的孔径分布图。Fig. 4 is a pore size distribution diagram of carbon microspheres prepared in Example 3 of the present invention.
图5为本发明实施例4制备的碳微球的孔径分布图。Fig. 5 is a pore size distribution diagram of carbon microspheres prepared in Example 4 of the present invention.
图6为本发明实施例5制备的碳微球的孔径分布图。Fig. 6 is a pore size distribution diagram of carbon microspheres prepared in Example 5 of the present invention.
具体实施方式Detailed ways
下面通过实施例来进一步说明本发明,但不局限于以下实施例。The present invention is further illustrated by the following examples, but not limited to the following examples.
实施例1Example 1
一种新型多孔碳微球的制备方法,其主要包括以下步骤:A preparation method of novel porous carbon microspheres, which mainly comprises the following steps:
(1)将环氧树脂与固化剂乙二胺混合组成均一相;所述环氧树脂与固化剂的质量比为100:7。(1) Mix the epoxy resin and the curing agent ethylenediamine to form a homogeneous phase; the mass ratio of the epoxy resin to the curing agent is 100:7.
(2)将去离子水加入到环氧树脂均一相中,高速搅拌成乳液;所述环氧树脂与去离子水的质量比为100:50。(2) Add deionized water into the homogeneous phase of epoxy resin, and stir at high speed to form an emulsion; the mass ratio of the epoxy resin to deionized water is 100:50.
(3)将乳液滴加到与硅油中,高速搅拌形成复相乳液;所述环氧树脂与硅油的质量比为1:3;所述搅拌速度为10000r/min。(3) Add the emulsion dropwise to the silicone oil, and stir at high speed to form a multi-phase emulsion; the mass ratio of the epoxy resin to the silicone oil is 1:3; the stirring speed is 10000r/min.
(4)加热使树脂固化,加热温度为60℃,升温速率为5℃/min,保温时间为24h;制备环氧树脂包水微胶囊;(4) Heating to solidify the resin, the heating temperature is 60°C, the heating rate is 5°C/min, and the holding time is 24h; prepare water-coated epoxy resin microcapsules;
(5)将过滤,洗涤,干燥(干燥温度为40℃,时间为8h)后的环氧树脂包水微胶囊置于氩气保护下,进行高温热解炭化,80℃保温30min,400℃保温60min,800℃保温120min,升温速率5℃/min。(5) Put the water-in-epoxy microcapsules after filtration, washing and drying (drying temperature at 40°C for 8 hours) under the protection of argon for high-temperature pyrolysis and carbonization, heat preservation at 80°C for 30 minutes, and heat preservation at 400°C 60min, 800°C for 120min,
图1为本实施例中制备的碳微球的SEM图。Figure 1 is a SEM image of the carbon microspheres prepared in this example.
从图1a中可以看出碳微球呈球形,其粒径分布在1-100μm之间,其表面分布着许多大小不一的孔洞,其中许多粒径较小的碳微球吸附在较大粒径碳微球的大孔洞中;图1b中可以看出碳微球在自然条件下容易团聚,说明其具有较高的表面能,容易吸附在一起;图1c为图1b的局部放大图,可以看出存在大量的微孔。It can be seen from Figure 1a that the carbon microspheres are spherical, and their particle size distribution is between 1-100 μm. In Fig. 1b, it can be seen that carbon microspheres are easy to agglomerate under natural conditions, indicating that they have high surface energy and are easy to adsorb together; Fig. 1c is a partial enlarged view of Fig. 1b, which can be It is seen that a large number of microvoids are present.
图2为本实施例中制备的碳微球的孔径分布图。从图2中可以看出其孔分布为2nm的微孔,10-50nm的介孔和50-100nm的大孔,其比表面积为80.83m2/g。Figure 2 is a pore size distribution diagram of the carbon microspheres prepared in this example. It can be seen from Figure 2 that the pore distribution is micropores of 2nm, mesopores of 10-50nm and macropores of 50-100nm, and its specific surface area is 80.83m 2 /g.
实施例2Example 2
一种新型多孔碳微球的制备方法,其主要包括以下步骤:A preparation method of novel porous carbon microspheres, which mainly comprises the following steps:
(1)将酚醛树脂与固化剂对甲苯磺酸混合组成均一相;所述酚醛树脂与固化剂的质量比为100:10。(1) Mix the phenolic resin and the curing agent p-toluenesulfonic acid to form a homogeneous phase; the mass ratio of the phenolic resin to the curing agent is 100:10.
(2)将去离子水加入到酚醛树脂均一相中,高速搅拌成乳液;所述酚醛树脂与去离子水的质量比为100:60。(2) Add deionized water into the homogeneous phase of phenolic resin, and stir at high speed to form an emulsion; the mass ratio of the phenolic resin to deionized water is 100:60.
(3)将乳液滴加到与硅油中,高速搅拌形成复相乳液;所述酚醛树脂与硅油的质量比为1:4;所述搅拌速度为10000r/min。(3) Add the emulsion dropwise to the silicone oil, and stir at high speed to form a multi-phase emulsion; the mass ratio of the phenolic resin to the silicone oil is 1:4; the stirring speed is 10000r/min.
(4)加热使树脂固化,加热温度为120℃,升温速率为3℃/min,保温时间为1h,制备酚醛树脂包水微胶囊;(4) Heating to solidify the resin, the heating temperature is 120°C, the heating rate is 3°C/min, and the holding time is 1h, to prepare water-coated phenolic resin microcapsules;
(5)将过滤,洗涤,干燥(干燥温度为50℃,时间为6h)后的酚醛树脂包水微胶囊置于氩气保护下,进行高温热解炭化,90℃保温40min,450℃保温50min,900℃保温90min,升温速率5℃/min。(5) Put the water-coated phenolic resin microcapsules after filtration, washing, and drying (drying temperature at 50°C for 6 hours) under the protection of argon for high-temperature pyrolysis and carbonization, heat preservation at 90°C for 40 minutes, and heat preservation at 450°C for 50 minutes , keep at 900°C for 90min, and the heating rate is 5°C/min.
图3为本实施例中制备的碳微球的孔径分布图。从图3中可以看出其孔分布主要为1nm的微孔,另外存在少量的20-50nm的介孔和50-100nm的大孔,其比表面积为277.3m2/g。Figure 3 is a pore size distribution diagram of the carbon microspheres prepared in this example. It can be seen from Figure 3 that the pore distribution is mainly micropores of 1 nm, and there are a small amount of mesopores of 20-50 nm and macropores of 50-100 nm, and its specific surface area is 277.3 m 2 /g.
实施例3Example 3
一种新型多孔碳微球的制备方法,其主要包括以下步骤:A preparation method of novel porous carbon microspheres, which mainly comprises the following steps:
(1)将酚醛树脂与固化剂对甲苯磺酸混合组成均一相;所述酚醛树脂与固化剂的质量比为100:11。(1) Mix the phenolic resin and the curing agent p-toluenesulfonic acid to form a homogeneous phase; the mass ratio of the phenolic resin to the curing agent is 100:11.
(2)将去离子水加入到酚醛树脂均一相中,高速搅拌成乳液;所述酚醛树脂与去离子水的质量比为100:55。(2) Add deionized water into the homogeneous phase of phenolic resin, and stir at high speed to form an emulsion; the mass ratio of the phenolic resin to deionized water is 100:55.
(3)将乳液滴加到与硅油中,高速搅拌形成复相乳液;所述酚醛树脂与硅油的质量比为1:5;所述搅拌速度为15000r/min。(3) Add the emulsion dropwise to the silicone oil, and stir at high speed to form a multi-phase emulsion; the mass ratio of the phenolic resin to the silicone oil is 1:5; the stirring speed is 15000r/min.
(4)加热使树脂固化,加热温度为150℃,升温速率为4℃/min,保温时间为1h;制备酚醛树脂包水微胶囊;(4) Heating to solidify the resin, the heating temperature is 150°C, the heating rate is 4°C/min, and the holding time is 1h; prepare water-coated phenolic resin microcapsules;
(5)将过滤,洗涤,干燥(干燥温度为70℃,时间为4h)后的酚醛树脂包水微胶囊置于氩气保护下,进行高温热解炭化,85℃保温30min,300℃保温80min,750℃保温120min,升温速率5℃/min。(5) Put the water-coated phenolic resin microcapsules after filtration, washing and drying (drying temperature at 70°C for 4 hours) under the protection of argon for high-temperature pyrolysis and carbonization, heat preservation at 85°C for 30 minutes, and heat preservation at 300°C for 80 minutes , 750°C for 120min,
图4为本实施例中制备的碳微球的孔径分布图。从图4中可以看出其孔分布为1-2nm的微孔,且主要为1nm的微孔,5-50nm的介孔和50-100nm的大孔,其比表面积为124.97m2/g。Figure 4 is a pore size distribution diagram of the carbon microspheres prepared in this example. It can be seen from Figure 4 that the pore distribution is micropores of 1-2nm, mainly micropores of 1nm, mesopores of 5-50nm and macropores of 50-100nm, and the specific surface area is 124.97m 2 /g.
实施例4Example 4
一种新型多孔碳微球的制备方法,其主要包括以下步骤:A preparation method of novel porous carbon microspheres, which mainly comprises the following steps:
(1)将酚醛树脂与固化剂对甲苯磺酸混合组成均一相;所述酚醛树脂与固化剂的质量比为100:9。(1) Mix the phenolic resin and the curing agent p-toluenesulfonic acid to form a homogeneous phase; the mass ratio of the phenolic resin to the curing agent is 100:9.
(2)将去离子水加入到酚醛树脂均一相中,高速搅拌成乳液;所述酚醛树脂与去离子水的质量比为100:65。(2) Add deionized water into the homogeneous phase of phenolic resin, and stir at high speed to form an emulsion; the mass ratio of the phenolic resin to deionized water is 100:65.
(3)将乳液滴加到与硅油中,高速搅拌形成复相乳液;所述酚醛树脂与硅油的质量比为1:4.5;所述搅拌速度为20000r/min。(3) Add the emulsion dropwise to the silicone oil, and stir at a high speed to form a multi-phase emulsion; the mass ratio of the phenolic resin to the silicone oil is 1:4.5; the stirring speed is 20000r/min.
(4)加热使树脂固化,加热温度为140℃,升温速率为3℃/min,保温时间为2.5h;制备酚醛树脂包水微胶囊;(4) Heating to solidify the resin, the heating temperature is 140°C, the heating rate is 3°C/min, and the holding time is 2.5h; prepare water-coated phenolic resin microcapsules;
(5)将过滤,洗涤,干燥(干燥温度为60℃,时间为8h)后的酚醛树脂包水微胶囊置于氩气保护下,进行高温热解炭化,80℃保温20min,450℃保温70min,800℃保温100min,升温速率3℃/min。(5) Put the water-coated phenolic resin microcapsules after filtration, washing, and drying (drying temperature at 60°C for 8 hours) under the protection of argon for high-temperature pyrolysis and carbonization, heat preservation at 80°C for 20 minutes, and heat preservation at 450°C for 70 minutes , keep at 800°C for 100min, and the heating rate is 3°C/min.
图5为本实施例中制备的碳微球的孔径分布图。从图5中可以看出其孔分布为1-2nm的微孔,且主要为1.5nm的微孔,少量15-50nm的介孔和50-100nm的大孔,其比表面积为244.08m2/g。Fig. 5 is a diagram of the pore size distribution of the carbon microspheres prepared in this example. It can be seen from Figure 5 that the pore distribution is micropores of 1-2nm, mainly micropores of 1.5nm, a small amount of mesopores of 15-50nm and macropores of 50-100nm, and its specific surface area is 244.08m 2 / g.
实施例5Example 5
一种新型多孔碳微球的制备方法,其主要包括以下步骤:A preparation method of novel porous carbon microspheres, which mainly comprises the following steps:
(1)将环氧树脂与固化剂二乙烯三胺混合组成均一相;所述环氧树脂与固化剂的质量比为100:8。(1) Mix the epoxy resin and the curing agent diethylenetriamine to form a homogeneous phase; the mass ratio of the epoxy resin to the curing agent is 100:8.
(2)将去离子水加入到环氧树脂均一相中,高速搅拌成乳液;所述环氧树脂与去离子水的质量比为100:55。(2) Add deionized water into the homogeneous phase of epoxy resin, and stir at high speed to form an emulsion; the mass ratio of the epoxy resin to deionized water is 100:55.
(3)将乳液滴加到与硅油中,高速搅拌形成复相乳液;所述环氧树脂与硅油的质量比为1:5;所述搅拌速度为30000r/min。(3) Add the emulsion dropwise to the silicone oil, and stir at high speed to form a multi-phase emulsion; the mass ratio of the epoxy resin to the silicone oil is 1:5; the stirring speed is 30000r/min.
(4)加热使树脂固化,加热温度为60℃,升温速率为3℃/min,保温时间为18h;制备环氧树脂包水微胶囊;(4) Heating to solidify the resin, the heating temperature is 60°C, the heating rate is 3°C/min, and the holding time is 18h; prepare water-coated epoxy resin microcapsules;
(5)将过滤,洗涤,干燥(干燥温度为50℃,时间为6h)后的环氧树脂包水微胶囊置于氩气保护下,进行高温热解炭化,80℃保温30min,350℃保温80min,800℃保温120min,升温速率1℃/min。(5) Put the water-in-epoxy microcapsules after filtration, washing, and drying (drying temperature at 50°C for 6 hours) under the protection of argon for high-temperature pyrolysis and carbonization, heat preservation at 80°C for 30 minutes, and heat preservation at 350°C 80min, 800°C for 120min,
图6为本实施例中制备的碳微球的孔径分布图。从图6中可以看出其孔分布为1-2nm的微孔,且主要为2nm的微孔,且存在大量的5-50nm的介孔和50-100nm的大孔,其比表面积为69.97m2/g。Fig. 6 is a pore size distribution diagram of the carbon microspheres prepared in this example. It can be seen from Figure 6 that the pore distribution is 1-2nm micropores, mainly 2nm micropores, and there are a large number of 5-50nm mesopores and 50-100nm macropores, and its specific surface area is 69.97m 2 /g.
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