CN106431491A - Preparation method of blocky mullite-silicon carbide composite aerogel material with high specific surface area - Google Patents
Preparation method of blocky mullite-silicon carbide composite aerogel material with high specific surface area Download PDFInfo
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- CN106431491A CN106431491A CN201610885971.8A CN201610885971A CN106431491A CN 106431491 A CN106431491 A CN 106431491A CN 201610885971 A CN201610885971 A CN 201610885971A CN 106431491 A CN106431491 A CN 106431491A
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- silicon carbide
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- aluminum
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- 229910010271 silicon carbide Inorganic materials 0.000 title claims abstract description 63
- 239000002131 composite material Substances 0.000 title claims abstract description 52
- 239000000463 material Substances 0.000 title claims abstract description 48
- 238000002360 preparation method Methods 0.000 title claims abstract description 16
- 239000004964 aerogel Substances 0.000 title abstract description 7
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims abstract description 57
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 claims abstract description 45
- 229910052863 mullite Inorganic materials 0.000 claims abstract description 45
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 23
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 23
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000010703 silicon Substances 0.000 claims abstract description 14
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 13
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 12
- 239000012298 atmosphere Substances 0.000 claims abstract description 12
- 238000001354 calcination Methods 0.000 claims abstract description 10
- 238000000352 supercritical drying Methods 0.000 claims abstract description 10
- 230000032683 aging Effects 0.000 claims abstract description 9
- 238000002156 mixing Methods 0.000 claims abstract description 7
- 229910052814 silicon oxide Inorganic materials 0.000 claims abstract description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 31
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 22
- 238000010438 heat treatment Methods 0.000 claims description 21
- 238000003756 stirring Methods 0.000 claims description 20
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 14
- 238000001035 drying Methods 0.000 claims description 10
- 239000007789 gas Substances 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 6
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 claims description 6
- 239000000499 gel Substances 0.000 claims description 6
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 claims description 6
- 239000011240 wet gel Substances 0.000 claims description 6
- ZFBOVYJITDWWBB-UHFFFAOYSA-N 3-triethoxysilylpropane-1,1,1-triamine Chemical compound CCO[Si](OCC)(OCC)CCC(N)(N)N ZFBOVYJITDWWBB-UHFFFAOYSA-N 0.000 claims description 4
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 4
- JGDITNMASUZKPW-UHFFFAOYSA-K aluminium trichloride hexahydrate Chemical compound O.O.O.O.O.O.Cl[Al](Cl)Cl JGDITNMASUZKPW-UHFFFAOYSA-K 0.000 claims description 4
- 229940009861 aluminum chloride hexahydrate Drugs 0.000 claims description 4
- XNDZQQSKSQTQQD-UHFFFAOYSA-N 3-methylcyclohex-2-en-1-ol Chemical compound CC1=CC(O)CCC1 XNDZQQSKSQTQQD-UHFFFAOYSA-N 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
- UNWUYTNKSRTDDC-UHFFFAOYSA-N tert-butylsilane Chemical compound CC(C)(C)[SiH3] UNWUYTNKSRTDDC-UHFFFAOYSA-N 0.000 claims description 3
- WOZZOSDBXABUFO-UHFFFAOYSA-N tri(butan-2-yloxy)alumane Chemical compound [Al+3].CCC(C)[O-].CCC(C)[O-].CCC(C)[O-] WOZZOSDBXABUFO-UHFFFAOYSA-N 0.000 claims description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims description 3
- 229920002554 vinyl polymer Polymers 0.000 claims description 3
- DGXAGETVRDOQFP-UHFFFAOYSA-N 2,6-dihydroxybenzaldehyde Chemical compound OC1=CC=CC(O)=C1C=O DGXAGETVRDOQFP-UHFFFAOYSA-N 0.000 claims description 2
- ZRYCRPNCXLQHPN-UHFFFAOYSA-N 3-hydroxy-2-methylbenzaldehyde Chemical compound CC1=C(O)C=CC=C1C=O ZRYCRPNCXLQHPN-UHFFFAOYSA-N 0.000 claims description 2
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 239000005011 phenolic resin Substances 0.000 claims description 2
- 229920001568 phenolic resin Polymers 0.000 claims description 2
- QQQSFSZALRVCSZ-UHFFFAOYSA-N triethoxysilane Chemical compound CCO[SiH](OCC)OCC QQQSFSZALRVCSZ-UHFFFAOYSA-N 0.000 claims description 2
- IXWOUPGDGMCKGT-UHFFFAOYSA-N 2,3-dihydroxybenzaldehyde Chemical compound OC1=CC=CC(C=O)=C1O IXWOUPGDGMCKGT-UHFFFAOYSA-N 0.000 claims 1
- BPSIOYPQMFLKFR-UHFFFAOYSA-N trimethoxy-[3-(oxiran-2-ylmethoxy)propyl]silane Chemical compound CO[Si](OC)(OC)CCCOCC1CO1 BPSIOYPQMFLKFR-UHFFFAOYSA-N 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 15
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 238000011065 in-situ storage Methods 0.000 abstract description 4
- 230000003064 anti-oxidating effect Effects 0.000 abstract description 3
- 238000003763 carbonization Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000006087 Silane Coupling Agent Substances 0.000 abstract 1
- 239000000701 coagulant Substances 0.000 abstract 1
- 238000006460 hydrolysis reaction Methods 0.000 abstract 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 abstract 1
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 description 12
- 230000003647 oxidation Effects 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 8
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 6
- 239000011148 porous material Substances 0.000 description 5
- 238000012512 characterization method Methods 0.000 description 4
- 238000007872 degassing Methods 0.000 description 4
- 239000003292 glue Substances 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- 239000012528 membrane Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000376 reactant Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000003980 solgel method Methods 0.000 description 3
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 239000012300 argon atmosphere Substances 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000011946 reduction process Methods 0.000 description 2
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- GGUPMVXPXHZNKF-UHFFFAOYSA-N benzene-1,2-diol;formaldehyde Chemical compound O=C.OC1=CC=CC=C1O GGUPMVXPXHZNKF-UHFFFAOYSA-N 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010301 surface-oxidation reaction Methods 0.000 description 1
- YUYCVXFAYWRXLS-UHFFFAOYSA-N trimethoxysilane Chemical class CO[SiH](OC)OC YUYCVXFAYWRXLS-UHFFFAOYSA-N 0.000 description 1
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- C04B38/063—Preparing or treating the raw materials individually or as batches
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
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- C04B35/16—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay
- C04B35/18—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay rich in aluminium oxide
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Abstract
Description
技术领域technical field
本发明属于气凝胶材料的制备工艺领域,涉及一种块状高比表莫来石-碳化硅复合气凝胶材料的制备方法;尤其设计一种采用一步溶胶-凝胶法结合超临界干燥工艺和热处理工艺条件制备块状高比表mullite/SiC抗氧化复合气凝胶的方法。The invention belongs to the field of preparation technology of airgel materials, and relates to a preparation method of blocky high-specification mullite-silicon carbide composite airgel materials; in particular, a one-step sol-gel method combined with supercritical drying is designed Process and heat treatment process conditions A method for preparing blocky high specific mullite/SiC anti-oxidation composite airgel.
背景技术Background technique
碳化硅多孔材料是一种新型功能材料,具备耐高温、耐磨损、热膨胀系数低、比表面积大和化学稳定性优异的优良特性,可以广泛应用于催化剂载体、高温气体过滤器、膜分离、传感器等领域。但是碳化硅材料在应用过程中,经常会遇到严重的氧化问题,在700℃左右便在表面形成氧化硅层,这在一定程度上降低了它的应用。莫来石材料是一系列由铝硅酸盐组成的矿物统称,莫来石是Al2O3-SiO2系中唯一稳定的二元化合物,具有耐高温、强度高、导热系数小,高的抗蠕变性能和热稳定性,同时与碳化硅材料具有相似的热膨胀系数。因此,莫来石复合碳化硅多孔材料的研究将具备广阔的前景。国内外众多科研工作者都对这种多孔材料开展了研究,但是当前的研究主要还是利用莫来石原位生成法,通过在原料中引入碳化硅材料,从而利用高温下碳化硅表面氧化形成的氧化硅层与原料中的铝源发生反应从而形成最终的碳化硅/莫来石复合多孔材料。Silicon carbide porous material is a new type of functional material with excellent characteristics of high temperature resistance, wear resistance, low thermal expansion coefficient, large specific surface area and excellent chemical stability. It can be widely used in catalyst carrier, high temperature gas filter, membrane separation, sensor and other fields. However, silicon carbide materials often encounter serious oxidation problems during the application process, and a silicon oxide layer is formed on the surface at around 700 ° C, which reduces its application to a certain extent. Mullite material is a general term for a series of minerals composed of aluminosilicates. Mullite is the only stable binary compound in the Al 2 O 3 -SiO 2 system. It has high temperature resistance, high strength, small thermal conductivity, and high Creep resistance and thermal stability, while having a similar coefficient of thermal expansion to SiC materials. Therefore, the research on mullite composite silicon carbide porous materials will have broad prospects. Many researchers at home and abroad have carried out research on this porous material, but the current research mainly uses the in-situ generation method of mullite, by introducing silicon carbide material into the raw material, so as to utilize the oxidation formed by the surface oxidation of silicon carbide at high temperature. The silicon layer reacts with the aluminum source in the raw material to form the final silicon carbide/mullite composite porous material.
气凝胶作为一种具备三维纳米多孔结构的轻质多孔材料,同样具有低密度、高比表面积、高孔隙率等特点,在吸附、催化、隔热和阻抗耦合等方面具备广阔的应用前景。如能将碳化硅材料和莫来石材料制备成多孔气凝胶结构,将具备更为优异的使用性能,当前国内外有关于碳化硅气凝胶的相关报道,(如专利号CN102910926A的中国专利),也有关于莫来石气凝胶材料的类似报道,(Cluzel F,Larnac G,Phalippou J.Structure and thermalevolution of mullite aerogels[J].Journal of materials science,1991,26(22):5979-5984),但是对于碳化硅/莫来石复合气凝胶材料并没有相关的文献报道。本专利中将莫来石与碳化硅气凝胶进行复合,通过一步溶胶-凝胶法结合超临界干燥工艺和热处理工艺条件制备块状耐高温高比表mullite/SiC抗氧化复合气凝胶,这样一来可以提高碳化硅材料的成块性能(碳化硅气凝胶成块性能极差),二来也可以更好的提高碳化硅材料的抗氧化性能。As a lightweight porous material with a three-dimensional nanoporous structure, airgel also has the characteristics of low density, high specific surface area, and high porosity. It has broad application prospects in adsorption, catalysis, heat insulation, and impedance coupling. If silicon carbide material and mullite material can be prepared into a porous airgel structure, it will have more excellent performance. At present, there are relevant reports about silicon carbide airgel at home and abroad, (such as the Chinese patent of patent No. CN102910926A ), there are also similar reports about mullite airgel materials, (Cluzel F, Larnac G, Phalippou J.Structure and thermalevolution of mullite aerogels[J].Journal of materials science, 1991,26(22):5979-5984 ), but there is no relevant literature report on silicon carbide/mullite composite airgel materials. In this patent, mullite and silicon carbide airgel are combined, and a block-shaped high-temperature-resistant high-specification mullite/SiC anti-oxidation composite airgel is prepared by a one-step sol-gel method combined with supercritical drying process and heat treatment process conditions. In this way, the agglomeration performance of the silicon carbide material can be improved (the agglomeration performance of the silicon carbide aerogel is extremely poor), and secondly, the oxidation resistance of the silicon carbide material can be better improved.
发明内容Contents of the invention
本发明的目的是为了改进现有技术存在的不足而提供一种块状高比表莫来石-碳化硅复合气凝胶材料的制备方法,该方法用料和工艺简单,微观结构可控性好,制备出的气凝胶材料具备低密度、高比表、抗氧化、耐高温等特性,同时与纤维复合之后可以制备成各种形状的样品,对实现气凝胶材料在催化剂载体、高温气体过滤器、膜分离、传感器等领域的应用具备积极的生产意义。The purpose of the present invention is to provide a method for preparing a blocky high-specification mullite-silicon carbide composite airgel material in order to improve the deficiencies in the prior art. The method uses simple materials and processes, and the microstructure is controllable Well, the prepared airgel material has the characteristics of low density, high specific surface area, oxidation resistance, and high temperature resistance. At the same time, it can be prepared into samples of various shapes after being combined with fibers. Applications in fields such as gas filters, membrane separation, and sensors have positive production significance.
本发明的技术方案为:块状高比表莫来石-碳化硅复合气凝胶材料的制备方法,其具体步骤如下:The technical scheme of the present invention is: the preparation method of massive high specific surface mullite-silicon carbide composite airgel material, and its specific steps are as follows:
(1)将碳源、甲醛、乙醇、水、铝源均匀混合后,在20~50℃的温度下均匀搅拌,得到水解的有机/氧化铝二元溶胶体系;(1) After uniformly mixing carbon source, formaldehyde, ethanol, water and aluminum source, uniformly stirring at a temperature of 20-50°C to obtain a hydrolyzed organic/alumina binary sol system;
(2)将硅源加入到步骤(1)中得到的二元溶胶体系中,继续在20~50℃的温度下均匀搅拌,得到交联的三元溶胶体系;(2) adding the silicon source to the binary sol system obtained in step (1), and continuing to stir evenly at a temperature of 20-50° C. to obtain a cross-linked ternary sol system;
(3)将步骤(2)中得到的三元溶胶体系倒入模具中反应至凝胶,放置10~30h;(3) Pour the ternary sol system obtained in step (2) into a mold to react to gel, and place it for 10 to 30 hours;
(4)将步骤(3)中加入老化液,在25~75℃的烘箱内进行置换;(4) Add the aging solution in step (3), and replace it in an oven at 25-75°C;
(5)将步骤(4)中得到的湿凝胶进行CO2超临界干燥处理,得到有机/甲醛/氧化硅/氧化铝复合气凝胶;(5) the wet gel obtained in the step (4) is carried out with CO supercritical drying treatment to obtain organic/formaldehyde/silicon oxide/alumina composite airgel;
(6)将步骤(5)中得到的复合气凝胶在惰性氛围气体保护下进行热处理,从而得到C/莫来石/SiC复合气凝胶;(6) heat-treating the composite airgel obtained in step (5) under the protection of an inert atmosphere gas, thereby obtaining C/mullite/SiC composite airgel;
(7)将步骤(6)中得到的C/莫来石/SiC复合气凝胶置于空气氛围中进行煅烧除碳,从而得到最终的块状多孔莫来石/SiC复合气凝胶材料;(7) placing the C/mullite/SiC composite airgel obtained in step (6) in an air atmosphere for calcination to remove carbon, thereby obtaining the final massive porous mullite/SiC composite airgel material;
其中:步骤(1)中的碳源、乙醇、水、铝源按照1:(1~4):(10~30):(1~5):(0.1~0.5)的摩尔比均匀混合;步骤(2)中的硅源与碳源按照摩尔比(0.5~5):1进行混合。Wherein: the carbon source, ethanol, water, aluminum source in the step (1) are uniformly mixed according to the molar ratio of 1: (1~4): (10~30): (1~5): (0.1~0.5); The silicon source and the carbon source in (2) are mixed according to the molar ratio (0.5-5):1.
优选步骤(1)中所述的碳源为邻苯二酚-甲醛、间苯二酚-甲醛、混甲酚-甲醛、均苯三酚-甲醛或酚醛树脂中的一种或其混合物。优选步骤(1)中所述的铝源为六水合氯化铝、九水合硝酸铝、仲丁醇铝或异丙醇铝中的一种或其混合物。Preferably, the carbon source described in step (1) is one of catechol-formaldehyde, resorcinol-formaldehyde, cresol-formaldehyde, pyroglucinol-formaldehyde or phenolic resin or a mixture thereof. Preferably, the aluminum source described in step (1) is one of aluminum chloride hexahydrate, aluminum nitrate nonahydrate, aluminum sec-butoxide or aluminum isopropoxide or a mixture thereof.
优选步骤(2)中所述的硅源为三氨丙基三乙氧基硅烷、乙烯基三过氧化叔丁基硅烷、丁二烯基三乙氧基硅烷或γ-缩水甘油醚氧丙基三甲氧基硅烷中的一种或其混合物。Preferably, the silicon source described in step (2) is triaminopropyl triethoxysilane, vinyl triperoxy tert-butyl silane, butadienyl triethoxy silane or γ-glycidyl ether oxypropyl One or a mixture of trimethoxysilanes.
优选步骤(1)中搅拌转速为400~600rpm,搅拌时间为0.5~4h;步骤(2)中搅拌转速为400~600rpm,搅拌时间为0.1~2h。Preferably, the stirring speed in step (1) is 400-600 rpm, and the stirring time is 0.5-4 h; the stirring speed in step (2) is 400-600 rpm, and the stirring time is 0.1-2 h.
优选步骤(4)中所述的老化液为乙醇、甲醇、丙酮、乙醚、正戊醇或异丙醇中的一种或其混合物。Preferably, the aging solution described in step (4) is one of ethanol, methanol, acetone, ether, n-pentanol or isopropanol or a mixture thereof.
优选步骤(5)中所述的干燥方法为干燥温度为50~70℃,高压反应釜内压强为8~12MPa,放气速率为5~20L/min,干燥时间为8~20h。Preferably, the drying method described in step (5) is as follows: the drying temperature is 50-70° C., the pressure in the autoclave is 8-12 MPa, the gas release rate is 5-20 L/min, and the drying time is 8-20 hours.
优选步骤(5)中置换次数为3~6次,每次置换时间为12~24h。Preferably, the number of replacements in step (5) is 3 to 6 times, and the time for each replacement is 12 to 24 hours.
优选步骤(6)中所述的热处理温度在1000~1500℃之间;升温速度为2~10℃/min,热处理时间为3~10h;惰性氛围保护气体为氩气、氮气或氦气。Preferably, the heat treatment temperature in step (6) is between 1000-1500° C.; the heating rate is 2-10° C./min, and the heat treatment time is 3-10 hours; the inert atmosphere protection gas is argon, nitrogen or helium.
优选步骤(7)中所述的空气热煅烧温度在400~800℃之间;升温速度为3~5℃/min,热处理时间为2~5h。Preferably, the air heat calcination temperature in step (7) is between 400-800°C; the heating rate is 3-5°C/min, and the heat treatment time is 2-5h.
有益效果:Beneficial effect:
(1)工艺简单。采用一步溶胶-凝胶法,同时引入碳源、铝源和硅源,并通过后续的超临界干燥、碳化和碳热还原过程,使硅源和铝源在高温下生成莫来石相,硅源和碳源生成碳化硅相,最后再通过空气热煅烧去处碳模板,从而最终制得块状高比表莫来石/碳化硅复合气凝胶。(1) The process is simple. Using a one-step sol-gel method, introducing carbon source, aluminum source and silicon source at the same time, and through the subsequent supercritical drying, carbonization and carbothermal reduction process, the silicon source and aluminum source can generate mullite phase at high temperature, silicon source and carbon source to form a silicon carbide phase, and finally the carbon template is removed by air heat calcination, so as to finally obtain a blocky high specific surface mullite/silicon carbide composite aerogel.
(2)原位生成碳化硅相。当前制备碳化硅/莫来石复合材料时,均是以碳化硅微粉、氧化铝微粉为反应原料,通过碳化硅相在高温下形成的氧化硅层与氧化铝反应形成莫来石相。而本方案中,碳化硅也是与原位生成的,是通过硅源和碳源在高温下的碳热还原过程得到的,因此结构更加精细,同时由于碳模板的存在,制备的材料孔隙率更高,比表面积更大。(2) In situ generation of silicon carbide phase. At present, when preparing silicon carbide/mullite composite materials, silicon carbide micropowder and alumina micropowder are used as reaction raw materials, and the silicon oxide layer formed by the silicon carbide phase at high temperature reacts with alumina to form a mullite phase. In this solution, silicon carbide is also generated in situ, which is obtained through the carbothermal reduction process of silicon source and carbon source at high temperature, so the structure is finer. At the same time, due to the existence of carbon template, the porosity of the prepared material is higher. Higher, larger specific surface area.
(3)本方法中制备的碳化硅/莫来石气凝胶材料为完整块状,同时由于莫来石相的引入进一步提高了碳化硅材料的抗氧化性能,这对于实现气凝胶材料在催化剂载体、高温气体过滤器、膜分离、传感器等领域的应用具备积极的意义。(3) The silicon carbide/mullite airgel material prepared in this method is a complete block, and the oxidation resistance of the silicon carbide material is further improved due to the introduction of the mullite phase, which is helpful for realizing the airgel material in The application in the fields of catalyst carrier, high temperature gas filter, membrane separation and sensor has positive significance.
附图说明Description of drawings
图1是实例1制得的块状高比表莫来石/碳化硅复合气凝胶材料的实物照片;Fig. 1 is the physical photo of the massive high specific surface mullite/silicon carbide composite airgel material that example 1 makes;
图2是实例2中,调节乙醇含量后得到的不同反应物浓度(铝源、硅源和碳源总和)下经过1400℃碳热还原后三元气凝胶体系的XRD衍射图。Fig. 2 is the XRD diffraction pattern of the ternary airgel system after carbothermal reduction at 1400°C under different reactant concentrations (the sum of aluminum source, silicon source and carbon source) obtained after adjusting the ethanol content in Example 2.
具体实施方式detailed description
实例1Example 1
将邻苯二酚、甲醛、乙醇、水、六水合氯化铝按摩尔比1:2:17.4:2:0.18均匀混合后,在20℃的温度、转速600rpm下均匀搅拌0.5h,得到部分水解的有机/氧化铝二元溶胶体系。然后将三氨丙基三乙氧基硅烷以与邻苯二酚摩尔比为0.77:1加入到上述二元溶胶体系中,继续在20℃的温度、转速600rpm下均匀搅拌0.1h,然后倒入模具中反应至凝胶,放置10h后加入乙醇老化液,在25℃的烘箱内进行置换3次,每次12h。然后对该湿凝胶进行CO2超临界干燥处理,超临界反应温度为50℃。反应釜压强为10MPa,放气速率为5L/min,干燥时间为20h后得到邻苯二酚/甲醛/氧化硅/氧化铝复合气凝胶。将该复合气凝胶在氩气氛围气体保护下进行1000℃热处理,升温速度为3℃/min,保温时间为3h,从而得到C/mullite/SiC复合气凝胶。最后将得到的C/mullite/SiC复合气凝胶置于空气氛围中500℃下进行煅烧除碳,升温速率3℃/min,保温时间3h,从而得到最终的块状多孔mullite/SiC复合气凝胶材料。经过表征发现,该块状高比表莫来石/碳化硅复合气凝胶材料的密度为0.25g/cm3,比表面积为134m2/g,比纯碳化硅材料的抗氧化温度提高98℃。所制得的块状高比表莫来石/碳化硅复合气凝胶材料的实物照片如图1所示,从图1可以看出,制得的莫来石/碳化硅复合气凝胶材料为块状材料,表面呈现碳化硅材料的浅绿色,虽然强度较差,但是孔隙率高,比表面积大。After uniformly mixing catechol, formaldehyde, ethanol, water, and aluminum chloride hexahydrate in a molar ratio of 1:2:17.4:2:0.18, stir evenly at a temperature of 20°C and a speed of 600rpm for 0.5h to obtain partially hydrolyzed organic/alumina binary sol system. Then add triaminopropyltriethoxysilane to the above-mentioned binary sol system at a molar ratio of 0.77:1 to catechol, continue to stir evenly at a temperature of 20°C at a speed of 600rpm for 0.1h, and then pour React to gel in the mold, add ethanol aging solution after standing for 10 hours, and replace in an oven at 25°C for 3 times, each time for 12 hours. Then the wet gel was subjected to CO2 supercritical drying treatment, and the supercritical reaction temperature was 50 °C. The pressure of the reactor was 10 MPa, the degassing rate was 5 L/min, and the drying time was 20 hours to obtain catechol/formaldehyde/silica/alumina composite airgel. The composite airgel was heat-treated at 1000°C under the protection of argon atmosphere, the heating rate was 3°C/min, and the holding time was 3h, so as to obtain the C/mullite/SiC composite airgel. Finally, the obtained C/mullite/SiC composite airgel is placed in the air atmosphere at 500°C for calcination to remove carbon, the heating rate is 3°C/min, and the holding time is 3h, so as to obtain the final blocky porous mullite/SiC composite airgel glue material. After characterization, it was found that the bulk high specific surface mullite/silicon carbide composite airgel material has a density of 0.25g/cm 3 and a specific surface area of 134m 2 /g, which is 98°C higher than that of pure silicon carbide materials. . The physical photo of the obtained massive high specific surface mullite/silicon carbide composite airgel material is shown in Figure 1, as can be seen from Figure 1, the prepared mullite/silicon carbide composite airgel material It is a block material with the light green color of silicon carbide on the surface. Although the strength is poor, it has high porosity and large specific surface area.
实例2Example 2
将邻苯二酚、甲醛、乙醇、水、六水合氯化铝按摩尔比1:3:25.3:3:0.32均匀混合后,在30℃的温度、转速500rpm下均匀搅拌1h,得到部分水解的有机/氧化铝二元溶胶体系。然后将丁二烯基三乙氧基硅烷以与邻苯二酚摩尔比为2:1加入到上述二元溶胶体系中,继续在30℃的温度、转速500rpm下均匀搅拌0.5h,然后倒入模具中反应至凝胶,放置20h后加入丙酮老化液,在60℃的烘箱内进行置换4次,每次18h。然后对该湿凝胶进行CO2超临界干燥处理,超临界反应温度为60℃。反应釜压强为12MPa,放气速率为10L/min,干燥时间为10h后得到邻苯二酚/甲醛/氧化硅/氧化铝复合气凝胶。将该复合气凝胶在氩气氛围气体保护下进行1400℃热处理,升温速度为5℃/min,保温时间为5h,从而得到C/mullite/SiC复合气凝胶。最后将得到的C/mullite/SiC复合气凝胶置于空气氛围中700℃下进行煅烧除碳,升温速率5℃/min,保温时间4h,从而得到最终的块状多孔mullite/SiC复合气凝胶材料。经过表征发现,该块状高比表莫来石/碳化硅复合气凝胶材料的密度为0.32g/cm3,比表面积为156m2/g,比纯碳化硅材料的抗氧化温度提高94℃。调节乙醇含量后得到的不同反应物浓度(铝源、硅源和碳源总和)下经过1400℃碳热还原后三元气凝胶体系的XRD衍射图如图2所示,从图中可以看出,经过1400℃碳热还原后,当反应物浓度位于20%~45%时,材料中均出现了较为明显的碳化硅和莫来石相,同时材料中还含有大量的碳模板,但是经过后续的空气煅烧热处理后,结构并未坍塌,材料仍然呈现出图1的完整块状。After uniformly mixing catechol, formaldehyde, ethanol, water, and aluminum chloride hexahydrate in a molar ratio of 1:3:25.3:3:0.32, stir evenly at a temperature of 30°C and a speed of 500 rpm for 1 hour to obtain partially hydrolyzed Organic/alumina binary sol system. Then add butadienyltriethoxysilane to the above-mentioned binary sol system at a molar ratio of 2:1 to catechol, continue to stir evenly at 30°C and 500rpm for 0.5h, and then pour React to gel in the mold, add acetone aging solution after standing for 20 hours, and replace it in an oven at 60°C for 4 times, each time for 18 hours. Then the wet gel was subjected to CO2 supercritical drying treatment, and the supercritical reaction temperature was 60 °C. The pressure of the reactor was 12MPa, the degassing rate was 10L/min, and the drying time was 10h to obtain the catechol/formaldehyde/silica/alumina composite airgel. The composite airgel was heat-treated at 1400°C under the protection of argon atmosphere, the heating rate was 5°C/min, and the holding time was 5h, so as to obtain the C/mullite/SiC composite airgel. Finally, the obtained C/mullite/SiC composite airgel is placed in the air atmosphere at 700°C for calcination to remove carbon, the heating rate is 5°C/min, and the holding time is 4h, so as to obtain the final blocky porous mullite/SiC composite airgel glue material. After characterization, it is found that the density of the blocky high specific surface mullite/silicon carbide composite airgel material is 0.32g/cm 3 , the specific surface area is 156m 2 /g, and the oxidation resistance temperature of the pure silicon carbide material is 94°C higher. . The XRD diffraction pattern of the ternary airgel system after carbothermal reduction at 1400 °C under different reactant concentrations (the sum of aluminum source, silicon source and carbon source) obtained after adjusting the ethanol content is shown in Figure 2. It can be seen from the figure that , after carbothermal reduction at 1400°C, when the concentration of the reactants was between 20% and 45%, relatively obvious silicon carbide and mullite phases appeared in the material, and the material also contained a large amount of carbon templates, but after subsequent After the air calcination heat treatment, the structure did not collapse, and the material still showed a complete block in Figure 1.
实例3Example 3
将间苯二酚、甲醛、乙醇、水、九水合硝酸铝按摩尔比1:4:30:5:0.46均匀混合后,在35℃的温度、转速500rpm下均匀搅拌2h,得到部分水解的有机/氧化铝二元溶胶体系。然后将三氨丙基三乙氧基硅烷以与间苯二酚摩尔比为5:1加入到上述二元溶胶体系中,继续在35℃的温度、转速400rpm下均匀搅拌1.5h,然后倒入模具中反应至凝胶,放置25h后加入乙醇老化液,在70℃的烘箱内进行置换5次,每次24h。然后对该湿凝胶进行CO2超临界干燥处理,超临界反应温度为55℃。反应釜压强为9MPa,放气速率为20L/min,干燥时间为13h后得到间苯二酚/甲醛/氧化硅/氧化铝复合气凝胶。将该复合气凝胶在氮气氛围气体保护下进行1350℃热处理,升温速度为8℃/min,保温时间为6h,从而得到C/mullite/SiC复合气凝胶。最后将得到的C/mullite/SiC复合气凝胶置于空气氛围中800℃下进行煅烧除碳,升温速率5℃/min,保温时间2h,从而得到最终的块状多孔mullite/SiC复合气凝胶材料。经过表征发现,该块状高比表莫来石/碳化硅复合气凝胶材料的密度为0.22g/cm3,比表面积为156m2/g,比纯碳化硅材料的抗氧化温度提高125℃。After uniformly mixing resorcinol, formaldehyde, ethanol, water, and aluminum nitrate nonahydrate in a molar ratio of 1:4:30:5:0.46, stir evenly at a temperature of 35°C and a speed of 500rpm for 2 hours to obtain partially hydrolyzed organic /alumina binary sol system. Then add triaminopropyltriethoxysilane to the above-mentioned binary sol system at a molar ratio of 5:1 to resorcinol, continue to stir evenly at a temperature of 35°C and a speed of 400rpm for 1.5h, and then pour React to gel in the mold, place it for 25 hours, add ethanol aging solution, and replace it in an oven at 70°C for 5 times, 24 hours each time. Then the wet gel was subjected to CO2 supercritical drying treatment, and the supercritical reaction temperature was 55 °C. The pressure of the reactor was 9 MPa, the degassing rate was 20 L/min, and the drying time was 13 hours to obtain resorcinol/formaldehyde/silica/alumina composite airgel. The composite airgel was heat-treated at 1350°C under the protection of nitrogen atmosphere, the heating rate was 8°C/min, and the holding time was 6h, so as to obtain the C/mullite/SiC composite airgel. Finally, the obtained C/mullite/SiC composite airgel is placed in the air atmosphere at 800°C for calcination to remove carbon, the heating rate is 5°C/min, and the holding time is 2h, so as to obtain the final blocky porous mullite/SiC composite airgel glue material. After characterization, it is found that the density of the blocky high specific surface mullite/silicon carbide composite airgel material is 0.22g/cm 3 , the specific surface area is 156m 2 /g, and the oxidation resistance temperature of the pure silicon carbide material is 125°C higher. .
实例4Example 4
将均苯三酚、甲醛、乙醇、水、仲丁醇铝按摩尔比1:1.4:12:1.6:0.25均匀混合后,在40℃的温度、转速400rpm下均匀搅拌3h,得到部分水解的有机/氧化铝二元溶胶体系。然后将乙烯基三过氧化叔丁基硅烷以与均苯三酚摩尔比为3:1加入到上述二元溶胶体系中,继续在40℃的温度、转速400rpm下均匀搅拌1.3h,然后倒入模具中反应至凝胶,放置15h后加入正戊醇老化液,在50℃的烘箱内进行置换3次,每次18h。然后对该湿凝胶进行CO2超临界干燥处理,超临界反应温度为70℃。反应釜压强为9.5MPa,放气速率为15L/min,干燥时间为8h后得到均苯三酚/甲醛/氧化硅/氧化铝复合气凝胶。将该复合气凝胶在氦气氛围气体保护下进行1500℃热处理,升温速度为5℃/min,保温时间为10h,从而得到C/mullite/SiC复合气凝胶。最后将得到的C/mullite/SiC复合气凝胶置于空气氛围中600℃下进行煅烧除碳,升温速率3℃/min,保温时间5h,从而得到最终的块状多孔mullite/SiC复合气凝胶材料。经过表征发现,该块状高比表莫来石/碳化硅复合气凝胶材料的密度为0.26g/cm3,比表面积为186m2/g,比纯碳化硅材料的抗氧化温度提高156℃。After uniformly mixing pyroglucinol, formaldehyde, ethanol, water, and aluminum sec-butoxide in a molar ratio of 1:1.4:12:1.6:0.25, uniformly stirring at a temperature of 40°C and a speed of 400 rpm for 3 hours, the partially hydrolyzed organic /alumina binary sol system. Then add vinyl triperoxy tert-butylsilane to the above-mentioned binary sol system at a molar ratio of 3:1 to pyroglucinol, continue to stir evenly at 40°C and 400rpm for 1.3h, and then pour React to gel in the mold, place it for 15 hours, add n-amyl alcohol aging solution, and replace it in an oven at 50°C for 3 times, each time for 18 hours. Then the wet gel was subjected to CO2 supercritical drying treatment, and the supercritical reaction temperature was 70 °C. The pressure of the reactor was 9.5 MPa, the degassing rate was 15 L/min, and the drying time was 8 hours to obtain the composite airgel of pyroglucinol/formaldehyde/silica/alumina. The composite airgel was heat-treated at 1500°C under the protection of helium atmosphere, the heating rate was 5°C/min, and the holding time was 10h, so as to obtain the C/mullite/SiC composite airgel. Finally, the obtained C/mullite/SiC composite airgel was calcined to remove carbon at 600°C in the air atmosphere, the heating rate was 3°C/min, and the holding time was 5h, so as to obtain the final blocky porous mullite/SiC composite airgel glue material. After characterization, it is found that the density of the blocky high specific surface mullite/silicon carbide composite airgel material is 0.26g/cm 3 , the specific surface area is 186m 2 /g, and the oxidation resistance temperature of the pure silicon carbide material is 156°C higher. .
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