CN100463851C - A kind of preparation method of superfine hydrophobic silicon dioxide - Google Patents
A kind of preparation method of superfine hydrophobic silicon dioxide Download PDFInfo
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- CN100463851C CN100463851C CNB2005100129475A CN200510012947A CN100463851C CN 100463851 C CN100463851 C CN 100463851C CN B2005100129475 A CNB2005100129475 A CN B2005100129475A CN 200510012947 A CN200510012947 A CN 200510012947A CN 100463851 C CN100463851 C CN 100463851C
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 122
- 239000000377 silicon dioxide Substances 0.000 title claims abstract description 56
- 230000002209 hydrophobic effect Effects 0.000 title claims abstract description 40
- 235000012239 silicon dioxide Nutrition 0.000 title claims abstract description 25
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract description 77
- 239000000843 powder Substances 0.000 claims abstract description 43
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000002245 particle Substances 0.000 claims abstract description 32
- 238000012986 modification Methods 0.000 claims abstract description 30
- 230000004048 modification Effects 0.000 claims abstract description 30
- 239000002904 solvent Substances 0.000 claims abstract description 26
- 239000000126 substance Substances 0.000 claims abstract description 26
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
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- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 22
- 238000001035 drying Methods 0.000 claims abstract description 21
- WYTZZXDRDKSJID-UHFFFAOYSA-N (3-aminopropyl)triethoxysilane Chemical compound CCO[Si](OCC)(OCC)CCCN WYTZZXDRDKSJID-UHFFFAOYSA-N 0.000 claims abstract description 20
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000001816 cooling Methods 0.000 claims abstract description 17
- 235000019270 ammonium chloride Nutrition 0.000 claims abstract description 16
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 14
- 238000000967 suction filtration Methods 0.000 claims abstract description 11
- 238000000227 grinding Methods 0.000 claims abstract description 9
- 239000000654 additive Substances 0.000 claims abstract description 8
- 230000000996 additive effect Effects 0.000 claims abstract description 7
- 238000004458 analytical method Methods 0.000 claims abstract description 4
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- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 7
- 238000010521 absorption reaction Methods 0.000 claims description 6
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- 229910004298 SiO 2 Inorganic materials 0.000 claims description 5
- 238000002441 X-ray diffraction Methods 0.000 claims description 5
- -1 aminopropyl Chemical group 0.000 claims description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 5
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- 230000008859 change Effects 0.000 claims description 4
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- 239000010431 corundum Substances 0.000 claims description 4
- 238000009826 distribution Methods 0.000 claims description 4
- 239000011521 glass Substances 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
- 229910052710 silicon Inorganic materials 0.000 claims description 4
- 239000010703 silicon Substances 0.000 claims description 4
- 238000004090 dissolution Methods 0.000 claims description 3
- 235000011167 hydrochloric acid Nutrition 0.000 claims description 3
- 239000004570 mortar (masonry) Substances 0.000 claims description 3
- 238000012360 testing method Methods 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 238000010835 comparative analysis Methods 0.000 claims description 2
- 238000006482 condensation reaction Methods 0.000 claims description 2
- 230000007062 hydrolysis Effects 0.000 claims description 2
- 238000006460 hydrolysis reaction Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 229960001866 silicon dioxide Drugs 0.000 claims 10
- 229960000935 dehydrated alcohol Drugs 0.000 claims 5
- 238000009835 boiling Methods 0.000 claims 2
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- 238000003828 vacuum filtration Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 36
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 abstract description 17
- 230000008569 process Effects 0.000 abstract description 15
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 abstract description 9
- 239000003054 catalyst Substances 0.000 abstract description 6
- 239000002994 raw material Substances 0.000 abstract description 6
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
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- 150000002484 inorganic compounds Chemical class 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
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- 238000004062 sedimentation Methods 0.000 description 2
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- VXEGSRKPIUDPQT-UHFFFAOYSA-N 4-[4-(4-methoxyphenyl)piperazin-1-yl]aniline Chemical compound C1=CC(OC)=CC=C1N1CCN(C=2C=CC(N)=CC=2)CC1 VXEGSRKPIUDPQT-UHFFFAOYSA-N 0.000 description 1
- 239000006087 Silane Coupling Agent Substances 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000002535 acidifier Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
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- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910052910 alkali metal silicate Inorganic materials 0.000 description 1
- 230000001458 anti-acid effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
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- 229910052681 coesite Inorganic materials 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
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- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- BVKYCEVCMKTQBN-UHFFFAOYSA-N methoxy(propyl)silicon Chemical compound CCC[Si]OC BVKYCEVCMKTQBN-UHFFFAOYSA-N 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
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- 238000000926 separation method Methods 0.000 description 1
- 239000005049 silicon tetrachloride Substances 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 239000008279 sol Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
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- 125000003396 thiol group Chemical class [H]S* 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
- QQQSFSZALRVCSZ-UHFFFAOYSA-N triethoxysilane Chemical compound CCO[SiH](OCC)OCC QQQSFSZALRVCSZ-UHFFFAOYSA-N 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
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Abstract
本发明为一种超细疏水性二氧化硅的制取方法,它是以化学物质正硅酸乙酯为原料,以氯化氨为催化剂,以去离子水为反应剂,以无水乙醇为溶剂,以盐酸,氨水为pH值控制剂,以γ-氨丙基三乙氧基硅烷为改性添加剂,以乙二醇为改性溶剂,经过合理的化学物质配比、精选、纯度控制、催化剂、溶剂、改性添加剂、改性溶剂的优化使用,溶胶、凝胶、酸碱度pH值控制调节,经烘干、研磨、过筛,在250℃焙烧、冷却、疏水改性处理、化合反应、抽滤、二次烘干、检测分析对比,最终得到高纯度的超细疏水性二氧化硅白色粉末,产物粉末颗粒分布均匀,形貌接近球形,粒径为60-70nm,产物疏水性能好,可与多种同类材料及高分子材料匹配,该制取方法使用设备少,工艺流程短,环境污染小,产收率高,可达97%,纯度好,纯度可达98%,是十分理想的制取超细疏水性二氧化硅白色粉末的方法。
The invention relates to a preparation method of superfine hydrophobic silicon dioxide, which uses the chemical substance ethyl orthosilicate as the raw material, uses ammonium chloride as the catalyst, deionized water as the reactant, and absolute ethanol as the Solvent, with hydrochloric acid and ammonia water as the pH controller, γ-aminopropyltriethoxysilane as the modification additive, and ethylene glycol as the modification solvent, after reasonable chemical substance ratio, selection, and purity control , Catalysts, solvents, modified additives, optimized use of modified solvents, sol, gel, pH value control and adjustment, after drying, grinding, sieving, roasting at 250 ° C, cooling, hydrophobic modification treatment, compound reaction , suction filtration, secondary drying, detection analysis and comparison, and finally obtain high-purity ultrafine hydrophobic silica white powder, the product powder particles are evenly distributed, the shape is close to spherical, the particle size is 60-70nm, and the product has good hydrophobicity , can be matched with a variety of similar materials and polymer materials. This preparation method uses less equipment, short process flow, less environmental pollution, high yield, up to 97%, and good purity, up to 98%, which is very The ideal method for preparing ultra-fine hydrophobic silica white powder.
Description
技术领域: Technical field:
本发明涉及一种超细疏水性二氧化硅的制取方法,属非金属复合材料无机化合物制取方法的技术领域。The invention relates to a method for preparing ultrafine hydrophobic silicon dioxide, which belongs to the technical field of methods for preparing inorganic compounds of non-metallic composite materials.
背景技术: Background technique:
无机化合物二氧化硅是一种性能优良、用途广泛的无机添加剂,俗称白碳黑,是一种轻质非晶固体材料,具有比表面积大、密度小、分散性好等特点,有优异的耐热性、耐磨性和焊接性能,被广泛用于橡胶、塑料、涂料、粘合剂、密封胶、光纤材料、高分子材料、现代医学、生物工程、光学等领域。Inorganic compound silica is an inorganic additive with excellent performance and wide application. It is commonly known as white carbon black. Thermal, wear-resistant and welding properties, are widely used in rubber, plastics, coatings, adhesives, sealants, optical fiber materials, polymer materials, modern medicine, bioengineering, optics and other fields.
目前,制取改性二氧化硅的方法有多种形式,例如气相法、沉淀法、重力沉降法等,改性的形式有添加硫醇基硅烷偶联剂改性,例如3—硫醇基甲氧基丙基硅烷法、添加钛酸酯法、干法,湿法、热处理法,化学处理法等,进行表面覆盖改性,机械化学改性、外膜改性、局部活性改性,这些方法各有长处,但也存在很多不足。At present, there are many methods for preparing modified silica, such as gas phase method, precipitation method, gravity sedimentation method, etc., and the modified form is modified by adding thiol silane coupling agent, such as 3-thiol group Methoxypropyl silane method, adding titanate method, dry method, wet method, heat treatment method, chemical treatment method, etc., for surface coverage modification, mechanochemical modification, outer film modification, local active modification, these Each method has its advantages, but there are also many shortcomings.
例如:气相法,是以卤化硅为原料,采用四氯化硅在氢氧焰中水解制取,是在1200℃高温下水解制取二氧化硅气体,然后冷凝,气相法物质浓度小,生成的粒子凝聚少,制取焙烧温度高,生产过程中消耗能源多,成本高,污染大。For example: the gas phase method uses silicon halide as the raw material to produce silicon tetrachloride by hydrolysis in an oxyhydrogen flame. It hydrolyzes silicon dioxide gas at a high temperature of 1200°C and then condenses it. The gas phase method has a small concentration of substances and produces The particle aggregation is less, the preparation and roasting temperature is high, the production process consumes a lot of energy, the cost is high, and the pollution is large.
例如:沉淀法,是以碱式硅酸盐为原料,以水或有机溶剂为反应介质,沉淀法也有多种形式:在有机溶剂中制备高分散性能的二氧化硅,酸化剂与硅酸盐反应、沉淀、分离、干燥制备二氧化硅,碱金属硅酸盐与无机酸混合制备,水玻璃的碳酸化制备,喷雾造粒制备,由于反应介质、反应配比、工艺条件不同,所得产物性能迥异,不易控制。For example: the precipitation method uses basic silicate as the raw material and uses water or organic solvent as the reaction medium. The precipitation method also has various forms: preparing silica with high dispersion performance in organic solvent, acidifying agent and silicate Reaction, precipitation, separation, drying to prepare silica, alkali metal silicate and inorganic acid mixed preparation, water glass carbonation preparation, spray granulation preparation, due to the difference in reaction medium, reaction ratio and process conditions, the properties of the obtained product Very different, not easy to control.
例如:重力沉降法,是在重力场下使悬浮液中的颗粒沉降、扩散、晶化、获取二氧化硅颗粒,但很难控制二氧化硅的结晶颗粒进行有序的排列,制取时间长。For example: the gravity sedimentation method is to make the particles in the suspension settle, diffuse, crystallize and obtain silica particles under the gravitational field, but it is difficult to control the orderly arrangement of the crystal particles of silica, and the preparation time is long .
二氧化硅的改性处理也有多种形式,但在改性过程中,也有诸多不足之处,有的不符合产物需要,有的改性周期长,有的改性后的化学性能不稳定。There are also many forms of silica modification, but in the modification process, there are also many shortcomings, some do not meet the product requirements, some have a long modification period, and some have unstable chemical properties after modification.
发明内容: Invention content:
发明目的:Purpose of the invention:
本发明的目的就是针对背景技术的不足,采用一种全新的溶胶、凝胶技术,采用新的制取工艺流程,用正硅酸乙酯做原料,用氯化氨做催化剂,用去离子水做反应剂,用无水乙醇做溶剂,用盐酸和氨水做酸碱度pH值调节剂,用γ—氨丙基三乙氧基硅烷做改性添加剂,用乙二醇做改性溶剂,采用溶胶、凝胶、烘干、过筛、焙烧、改性反应、抽滤、二次烘干,最终得到高纯度的、高分散性的超细疏水性二氧化硅白色粉末。The purpose of the present invention is exactly for the deficiency of background technology, adopts a kind of brand-new sol, gel technology, adopts new production technological process, makes raw material with orthosilicate ethyl ester, makes catalyst with ammonium chloride, uses deionized water As a reaction agent, use absolute ethanol as a solvent, use hydrochloric acid and ammonia water as a pH regulator, use γ-aminopropyltriethoxysilane as a modification additive, and use ethylene glycol as a modification solvent. Gel, drying, sieving, roasting, modification reaction, suction filtration, and secondary drying to finally obtain high-purity, high-dispersion ultrafine hydrophobic silica white powder.
技术方案:Technical solutions:
本发明使用的化学物质为:正硅酸乙酯、无水乙醇、去离子水、氯化氨、氨水、盐酸、γ—氨丙基三乙氧基硅烷、乙二醇,其组合配比是:以克、毫升为计量单位The chemical substance used in the present invention is: tetraethyl orthosilicate, absolute ethanol, deionized water, ammonium chloride, ammoniacal liquor, hydrochloric acid, γ-aminopropyltriethoxysilane, ethylene glycol, and its combination ratio is : Units of measurement are grams and milliliters
正硅酸乙酯:C8H20O4Si 5毫升±0.2毫升Tetraethyl silicate: C 8 H 20 O 4 Si 5ml ± 0.2ml
无水乙醇: C2H5OH 50毫升±1毫升Absolute ethanol: C 2 H 5 OH 50ml±1ml
去离子水: H2O 50毫升±0.2毫升Deionized water: H 2 O 50ml±0.2ml
氯化氨: NH4Cl 0.5毫升±0.02毫升Ammonium chloride: NH 4 Cl 0.5ml±0.02ml
氨水: NH3·H2O 0.20毫升±0.02毫升Ammonia water: NH 3 ·H 2 O 0.20ml±0.02ml
盐酸: HCl 0.30毫升±0.02毫升Hydrochloric acid: HCl 0.30ml±0.02ml
γ—氨丙基三乙氧基硅烷 NH2C3H6Si(OC2H5)3 γ—Aminopropyltriethoxysilane NH 2 C 3 H 6 Si(OC 2 H 5 ) 3
0.5毫升±0.02毫升0.5ml±0.02ml
乙二醇 C4H6O2 50毫升±1毫升Ethylene glycol C4H6O2 50ml ± 1ml
本发明的制取方法如下:The preparation method of the present invention is as follows:
(1)精选化学物质(1) Selected chemical substances
对配比所需化学物质要进行精选,并进行纯度控制:The chemical substances required for the ratio should be selected and controlled for purity:
正硅酸乙酯: 99.9%Tetraethyl silicate: 99.9%
无水乙醇: 99.7%Absolute ethanol: 99.7%
去离子水: 99.9%Deionized water: 99.9%
氯化氨(浓度): 28.0%Ammonium chloride (concentration): 28.0%
氨水(浓度): 40.0%Ammonia (concentration): 40.0%
盐酸(浓度): 38.0%Hydrochloric acid (concentration): 38.0%
γ—氨丙基三乙氧基硅烷: 99.8%γ-Aminopropyltriethoxysilane: 99.8%
乙二醇: 99.9%Ethylene glycol: 99.9%
(2)配置溶液并混合(2) Configure the solution and mix
选取配比所需的化学物质,进行溶液配制:Select the chemical substances required for the ratio and prepare the solution:
正硅酸乙酯:5毫升±0.2毫升Tetraethyl silicate: 5ml ± 0.2ml
无水乙醇: 50毫升±1毫升Absolute ethanol: 50ml ± 1ml
去离子水: 50毫升±0.2毫升Deionized water: 50ml±0.2ml
将正硅酸乙酯5毫升±0.2毫升置于三口烧瓶中,然后加入无水乙醇50毫升±1毫升,插入搅拌器搅拌5分钟,然后插入滴液漏斗,将去离子水50毫升±0.2毫升缓慢滴入三口烧瓶中,边滴入、边搅拌10分钟,使其澄清,成澄清混合溶液;Put 5 ml ± 0.2 ml of tetraethyl orthosilicate in a three-necked flask, then add 50 ml ± 1 ml of absolute ethanol, insert a stirrer and stir for 5 minutes, then insert a dropping funnel, add 50 ml ± 0.2 ml of deionized water Slowly drop it into a three-necked flask, and stir it for 10 minutes while adding it, to make it clear and form a clear mixed solution;
(3)调节酸碱度pH值(3) Adjust pH value
偏酸性调节:将三口烧瓶置于电加热套上,加热温度为60℃±1℃,在滴液漏斗中依次滴入氯化氨0.5毫升±0.02毫升、盐酸0.3毫升±0.02毫升,并用搅拌器剧烈搅拌,搅拌时间为3分钟±0.3分钟,恒温保温12分钟±1分钟,正硅酸乙酯水解,酸碱度pH值=3—4,偏酸性;Slightly acidic adjustment: place the three-neck flask on an electric heating mantle at a heating temperature of 60°C±1°C, drop in successively 0.5ml±0.02ml of ammonium chloride and 0.3ml±0.02ml of hydrochloric acid into the dropping funnel, and use a stirrer to Stir vigorously, the stirring time is 3 minutes ± 0.3 minutes, keep warm at constant temperature for 12 minutes ± 1 minute, hydrolyze ethyl orthosilicate, pH value = 3-4, slightly acidic;
偏碱性调节:三口瓶中的混合溶液温度为60℃±1℃,在滴液漏斗中滴入氨水0.20毫升±0.02毫升,边滴入、边加热、边剧烈搅拌,恒温保温、剧烈搅拌15分钟±1分钟,混合溶液的酸碱度pH值=8—9,偏碱性;Alkaline adjustment: the temperature of the mixed solution in the three-necked bottle is 60°C ± 1°C, drop 0.20ml ± 0.02ml of ammonia water into the dropping funnel, add it, heat it, stir vigorously, keep warm at constant temperature, and stir vigorously for 15 Minute ± 1 minute, the pH value of the mixed solution is 8-9, slightly alkaline;
混合溶液缩聚,混合溶液成湿凝胶状态,然后关闭电加热套,停止加热、搅拌,生成湿性凝胶产物;The mixed solution is polycondensed, and the mixed solution becomes a wet gel state, then the electric heating mantle is turned off, heating and stirring are stopped, and a wet gel product is generated;
溶胶、凝胶时将发生化合反应,反应式如下:A compound reaction will occur during sol and gel, and the reaction formula is as follows:
式中:SiO2·2H2O—水合二氧化硅In the formula: SiO 2 ·2H 2 O—hydrated silicon dioxide
(4)烘干(4) drying
将湿性凝胶产物取出置于刚玉产物舟中,将湿性凝胶产物连同产物舟一起置于烘箱中烘干,烘干温度为60℃±1℃,时间为90分钟±1分钟,湿性凝胶产物烘干后成干性凝胶产物;Take out the wet gel product and place it in a corundum product boat, and dry the wet gel product together with the product boat in an oven at a temperature of 60°C±1°C for 90 minutes±1 minute. The product becomes a dry gel product after drying;
(5)研磨、过筛(5) Grinding and sieving
将干性凝胶产物置于玛瑙研钵中,用研磨棒进行研磨,研磨后用180目筛网过筛,研磨、过筛反复进行,留下细粉,为二氧化硅产物细粉;Place the dry gel product in an agate mortar, grind it with a grinding rod, sieve it through a 180-mesh sieve after grinding, grind and sieve it repeatedly, and leave a fine powder, which is a fine powder of the silica product;
(6)焙烧(6) Roasting
将产物二氧化硅白色细粉置于刚玉产物舟中,将产物及产物舟置于高温炉中焙烧,焙烧温度为250℃±3℃,焙烧恒温保温时间为30分钟±1分钟,焙烧后的粉末即为超细二氧化硅白色粉末;Put the product white fine powder of silica in a corundum product boat, put the product and the product boat in a high-temperature furnace for roasting, the roasting temperature is 250 ° C ± 3 ° C, the roasting constant temperature holding time is 30 minutes ± 1 minute, the roasted The powder is superfine silicon dioxide white powder;
(7)冷却(7) cooling
焙烧后的超细二氧化硅粉末置于冷却容器中,在自然空气中冷却,冷却速度为2.5℃/分钟,冷却时间为90分钟,至常温20℃±3℃,然后取出置于专用容器中保存;The calcined ultrafine silicon dioxide powder is placed in a cooling container and cooled in natural air at a cooling rate of 2.5°C/min for 90 minutes until it reaches a normal temperature of 20°C±3°C, then taken out and placed in a special container save;
(8)超细二氧化硅粉体的疏水改性处理(8) Hydrophobic modification treatment of ultrafine silica powder
疏水改性剂:γ—氨丙基三乙氧基硅烷 0.5毫升±0.02毫升Hydrophobic modifier: γ-aminopropyltriethoxysilane 0.5ml±0.02ml
疏水改性溶剂:乙二醇 50毫升±1毫升Hydrophobic modification solvent: ethylene glycol 50ml ± 1ml
第一步:溶剂溶解,将冷却后的二氧化硅白色粉末置于四口烧瓶中,插入搅拌器、滴液漏斗、温度计、冷凝回流管,将四口烧瓶置于电加热套上,当加热温度为198℃±0.5℃时,按配比量加入改性溶剂乙二醇50毫升±1毫升,同时进行搅拌,使二氧化硅粉体溶解,时间为1分钟±0.2分钟;Step 1: Dissolve the solvent, put the cooled white silicon dioxide powder in a four-necked flask, insert a stirrer, dropping funnel, thermometer, and condensing reflux tube, and place the four-necked flask on an electric heating mantle, when heated When the temperature is 198°C±0.5°C, add 50ml±1ml of modified solvent ethylene glycol according to the ratio, and stir at the same time to dissolve the silica powder, and the time is 1 minute±0.2 minutes;
第二步:添加改性剂,改性反应,改性溶剂乙二醇加完后,滴入改性添加剂γ—氨丙基三乙氧基硅烷0.5毫升±0.02毫升,边滴入、边用搅拌器搅拌,在加热198℃±0.5℃状态下,使溶液混合并反应,时间为120分钟±1分钟,成混合溶液,反应式如下:The second step: add modifier, modifying reaction, after the modified solvent ethylene glycol is added, drop in the modified additive γ-aminopropyltriethoxysilane 0.5 ml ± 0.02 ml, drop and use Stir with a stirrer, and heat the solution at 198°C ± 0.5°C to mix and react the solution for 120 minutes ± 1 minute to form a mixed solution. The reaction formula is as follows:
乙二醇为溶剂,将改变二氧化硅表面特性,产生羟基中心堆积,在SiO2表面的羟基可与乙二醇的羟基基团由氢键联结,进行缩合反应,反应如下:Ethylene glycol is used as a solvent, which will change the surface characteristics of silica and produce hydroxyl center accumulation. The hydroxyl groups on the surface of SiO2 can be hydrogen bonded with the hydroxyl groups of ethylene glycol to undergo condensation reaction. The reaction is as follows:
式中:Si——硅 H——氢 C——碳Where: Si——silicon H——hydrogen C——carbon
O——氧 OH——氢氧根 HO——氢氧根O——oxygen OH——hydroxide HO——hydroxide
改性剂γ-氨丙基三乙氧基硅烷添加后将进行改性反应,反应式如下:After the modifier γ-aminopropyltriethoxysilane is added, the modification reaction will be carried out, and the reaction formula is as follows:
式中:NH2C3H6Si2·H2O——水合氨丙基In the formula: NH 2 C 3 H 6 Si 2 ·H 2 O——Aminopropyl hydrate
第三步:抽滤,将改性反应后的混合溶液置于循环水式真空泵中进行抽滤,将液体抽出,成粘稠状白色产物;The third step: suction filtration, place the mixed solution after the modification reaction in a circulating water vacuum pump for suction filtration, and extract the liquid to form a viscous white product;
第四步:烘干,将粘稠状白色产物置于烘箱中烘干,烘箱温度为200℃±1℃,烘干时间为60分钟±1分钟,即得到超细疏水性二氧化硅白色粉末。The fourth step: drying, put the viscous white product in an oven for drying, the oven temperature is 200°C ± 1°C, and the drying time is 60 minutes ± 1 minute to obtain superfine hydrophobic silicon dioxide white powder .
(9)收集产物(9) Collecting products
将改性后的产物——超细疏水性二氧化硅白色粉末,置于棕色透明的玻璃容器中,密闭避光保存;Put the modified product—white superfine hydrophobic silicon dioxide powder—in a brown transparent glass container, and store it in airtight and dark place;
(10)检测分析对比(10) Detection analysis comparison
对超细疏水性二氧化硅白色粉末进行纯度、色泽、形态、形貌、物相结构、颗粒尺寸、疏水性能、羟基紫外线吸收程度、物理化学性能进行检测、分析、对比、用粒径分析仪进行粒度及粒径分布测试,用透射电镜、X—射线衍射分析仪进行颗粒形貌、尺寸对比分析;The purity, color, shape, shape, phase structure, particle size, hydrophobicity, hydroxyl ultraviolet absorption degree, physical and chemical properties of ultrafine hydrophobic silica white powder are detected, analyzed, compared, and particle size analyzers are used Carry out particle size and particle size distribution test, and use transmission electron microscope and X-ray diffraction analyzer to conduct comparative analysis of particle shape and size;
(11)储存(11) storage
对制取的超细疏水性二氧化硅白色粉末,置于棕色透明的玻璃容器中,避光密闭储存于干燥、阴凉、洁净的环境中,储存温度为20℃±3℃,要严格防水、防潮、防火、防晒、防酸碱侵蚀。The prepared superfine hydrophobic silicon dioxide white powder is placed in a brown transparent glass container and stored in a dry, cool and clean environment away from light. The storage temperature is 20°C ± 3°C. It must be strictly waterproof, Moisture-proof, fire-proof, sun-proof, anti-acid and alkali erosion.
所述的超细疏水性二氧化硅的制取以正硅酸乙酯为原料,以氯化氨为催化剂,以去离子水为反应剂,以无水乙醇为溶剂,以盐酸、氨水为酸碱度pH值的调节剂,以γ-氨丙基三乙氧基硅烷为改性剂,以乙二醇为改性溶剂。The preparation of the ultra-fine hydrophobic silicon dioxide uses ethyl orthosilicate as a raw material, ammonium chloride as a catalyst, deionized water as a reactant, absolute ethanol as a solvent, and hydrochloric acid and ammonia as a pH The regulator of the pH value uses γ-aminopropyltriethoxysilane as the modifying agent and ethylene glycol as the modifying solvent.
所述的溶胶、凝胶过程中,在60℃±1℃的加热状态下,正硅酸乙酯、去离子水、无水乙醇的混合溶液滴入氯化氨0.5毫升±0.02毫升、盐酸0.3毫升±0.02毫升,并用搅拌器剧烈搅拌,搅拌时间为3分钟±0.3分钟,恒温保温12分钟±1分钟,正硅酸乙酯水解,酸碱度pH值=3—4,偏酸性;在60℃±1℃加热状态下,滴入氨水0.2毫升±0.02毫升,剧烈搅拌15分钟±1分钟,混合溶液的酸碱度pH值=8—9,偏碱性。In the process of sol and gel, under the heating state of 60°C±1°C, the mixed solution of ethyl orthosilicate, deionized water and absolute ethanol was dripped into 0.5ml±0.02ml of ammonium chloride, 0.3ml of hydrochloric acid mL ± 0.02 mL, and vigorously stirred with a stirrer, the stirring time is 3 minutes ± 0.3 minutes, kept at a constant temperature for 12 minutes ± 1 minute, hydrolyzed tetraethyl orthosilicate, pH value = 3-4, slightly acidic; at 60 ° C ± Under heating at 1°C, add 0.2ml ± 0.02ml of ammonia water dropwise, stir vigorously for 15 minutes ± 1 minute, the pH value of the mixed solution is 8-9, slightly alkaline.
所述的超细疏水性二氧化硅粉体的焙烧是在高温炉中进行的,高温炉升温速度为5℃/分钟,升温时间为45分钟,至焙烧温度250℃±3℃,焙烧恒温保温时间为30分钟±1分钟,焙烧后在空气中自然冷却至20℃±3℃,冷却速度为2.5℃/分钟,冷却时间为90分钟。The calcination of the superfine hydrophobic silica powder is carried out in a high-temperature furnace, the heating rate of the high-temperature furnace is 5°C/min, and the heating time is 45 minutes, until the calcination temperature is 250°C ± 3°C, and the calcination is kept at a constant temperature. The time is 30 minutes ± 1 minute. After calcination, it is naturally cooled to 20°C ± 3°C in the air, the cooling rate is 2.5°C/min, and the cooling time is 90 minutes.
所述的改性溶剂乙二醇溶解、改性剂γ-氨丙基三乙氧基硅烷添加是在加热状态下进行的,加热温度为198℃±0.5℃,乙二醇溶解时间为1分钟±0.2分钟,γ-氨丙基三乙氧基硅烷添加混合搅拌时间为120分钟±1分钟。The dissolution of the modified solvent ethylene glycol and the addition of the modifier γ-aminopropyltriethoxysilane are carried out under heating, the heating temperature is 198°C±0.5°C, and the ethylene glycol dissolution time is 1 minute ±0.2 minutes, γ-aminopropyltriethoxysilane was added and the mixing time was 120 minutes±1 minute.
所述的超细疏水性二氧化硅的形貌是高分散性的非晶白色粉末,其粒径尺寸为60—70nm。The shape of the ultrafine hydrophobic silicon dioxide is highly dispersed amorphous white powder, and its particle size is 60-70nm.
效果:Effect:
本发明与背景技术相比具有明显的先进性,采用了合理的化学物质配比,精选纯度控制,催化剂、溶剂、改性添加剂、改性溶剂的优化使用,溶胶、凝胶、酸碱度pH值的控制调节,烘干、研磨、过筛、焙烧、冷却、疏水改性处理、化合反应、抽滤、烘干、检测分析对比,以正硅酸乙酯为原料,以氯化氨为催化剂,以去离子水为反应剂,以无水乙醇为溶剂,以盐酸、氨水为pH值调节剂,以γ—氨丙基三乙氧基硅烷为疏水改性剂,以乙二醇为改性溶剂,最终得到高纯度的超细疏水性二氧化硅白色粉末,产物颗粒分布均匀,形貌接近球形,粒径为60—70纳米,产物疏水性能好,可与多种同类材料及高分子材料匹配,该制取方法使用设备少,工艺流程短,焙烧温度低,环境污染小,产收率高,可达97%,纯度好,纯度可达98%,是十分理想的超细疏水性二氧化硅白色粉末的制取方法。Compared with the background technology, the present invention has obvious advances, adopts reasonable chemical substance ratio, selected purity control, optimized use of catalyst, solvent, modified additive, modified solvent, sol, gel, pH value The control and adjustment of drying, grinding, sieving, roasting, cooling, hydrophobic modification treatment, compound reaction, suction filtration, drying, detection and analysis comparison, using ethyl orthosilicate as raw material and ammonium chloride as catalyst, Deionized water is used as a reactant, absolute ethanol is used as a solvent, hydrochloric acid and ammonia water are used as pH regulators, γ-aminopropyltriethoxysilane is used as a hydrophobic modifier, and ethylene glycol is used as a modifying solvent Finally, high-purity ultra-fine hydrophobic silica white powder is obtained. The product particles are evenly distributed, the shape is close to spherical, and the particle size is 60-70 nm. The product has good hydrophobicity and can be matched with a variety of similar materials and polymer materials. , the preparation method uses less equipment, short process flow, low roasting temperature, low environmental pollution, high yield, up to 97%, good purity, up to 98%, and is an ideal superfine hydrophobic carbon dioxide Preparation method of silicon white powder.
附图说明 Description of drawings
图1为超细疏水性二氧化硅白色粉末制取工艺流程图Figure 1 is a process flow chart for the preparation of superfine hydrophobic silica white powder
图2为焙烧温度与时间坐标关系图Fig. 2 is the coordinate diagram of roasting temperature and time
图3为改性过程中的冷凝回流图Figure 3 is the condensation reflux diagram during the modification process
图4为溶胶的pH值与凝胶时间坐标关系图Figure 4 is the pH value of the sol and the gel time coordinate diagram
图5为溶胶的pH值与产物粒径坐标关系图Fig. 5 is the pH value of sol and product particle size coordinate diagram
图6为去离子水与正硅酸乙酯的量的比值n与凝胶时间坐标关系图Fig. 6 is the ratio n of the amount of deionized water and tetraethyl orthosilicate and the gel time coordinate diagram
图7为去离子水与正硅酸乙酯的量的比值n与产物粒径坐标关系图Fig. 7 is the ratio n of the amount of deionized water and tetraethyl orthosilicate and the coordinate relationship diagram of product particle size
图8为溶液温度与凝胶时间坐标关系图Figure 8 is a graph of solution temperature and gel time coordinates
图9为溶液温度与产物粒径坐标关系图Fig. 9 is a coordinate relationship diagram between solution temperature and product particle size
图10为超细疏水性二氧化硅粉末透射电镜1×104倍形貌图Figure 10 is a 1×10 4x image of ultrafine hydrophobic silica powder transmission electron microscope
图11为超细疏水性二氧化硅粉末粒径分布图Figure 11 is a particle size distribution diagram of ultrafine hydrophobic silica powder
图12为超细疏水性二氧化硅粉末X—射线衍射强度图Figure 12 is an X-ray diffraction intensity diagram of ultrafine hydrophobic silicon dioxide powder
图13为改性时间与羟基紫外线吸收率对比图Figure 13 is a comparison chart of modification time and hydroxyl UV absorption rate
图中所示,件号清单如下:As shown in the figure, the part number list is as follows:
1、电加热套 2、四口烧瓶 3、搅拌器 4、冷凝回流管1.
5、出水管 6、空气口 7、进水管 8、滴液漏斗5.
9、温度计9. Thermometer
实施方式:Implementation method:
以下结合附图对本发明做进一步说明:The present invention will be further described below in conjunction with accompanying drawing:
图1所示,制取超细疏水性二氧化硅粉末要严格按工艺流程图进行,各制取参数要严格控制,按序操作。As shown in Figure 1, the production of ultrafine hydrophobic silica powder must be carried out strictly according to the process flow chart, and each production parameter must be strictly controlled and operated in sequence.
对制取所需的化学物质材料正硅酸乙酯、无水乙醇、去离子水、氯化氨、氨水、盐酸、乙二醇、γ—氨丙基三乙氧基硅烷要严格精选,并进行纯度控制,不能有杂质介入,防止生成副产物。The chemical materials required for the production of tetraethyl orthosilicate, absolute ethanol, deionized water, ammonium chloride, ammonia water, hydrochloric acid, ethylene glycol, γ-aminopropyltriethoxysilane must be strictly selected, And the purity control is carried out, no impurities can intervene, and by-products are prevented from being generated.
对所需的化学物质要严格按照配比称量控制,不得超出最大最小范围。The required chemical substances must be strictly controlled according to the proportioning and weighing, and must not exceed the maximum and minimum ranges.
溶胶—凝胶是连续进行的,酸碱度pH值的酸碱性对溶胶—凝胶有很大影响,要严格操作控制,并在溶胶—凝胶时要用强力搅拌器剧烈搅拌,搅拌器转数为500转/分钟,不得间歇,防止沉淀,各化学物质将产生化合反应,生成二氧化硅产物。The sol-gel is carried out continuously, and the acidity and alkalinity of the pH value has a great influence on the sol-gel, so strict operation control is required, and a strong stirrer must be used to stir vigorously during the sol-gel, and the number of revolutions of the stirrer The speed is 500 rpm, no intermittent, to prevent precipitation, each chemical substance will produce a compound reaction to form a silica product.
二氧化硅产物的焙烧是在高温炉中进行的,焙烧温度为250℃±3℃,并恒温保温30分钟±1分钟,然后取出在空气中自然冷却,焙烧工艺是十分重要的,要严格进行操作。The calcination of the silica product is carried out in a high-temperature furnace, the calcination temperature is 250°C ± 3°C, and the temperature is kept at a constant temperature for 30 minutes ± 1 minute, and then it is taken out and cooled naturally in the air. The calcination process is very important and must be strictly carried out. operate.
二氧化硅的改性是以γ—氨丙基三乙氧基硅烷为改性剂,以乙二醇为改性溶剂,经加热、抽滤、烘干,最终得到产物——超细疏水性二氧化硅白色粉末,改性工艺是决定二氧化硅疏水性的关键,以改变其表面的物理、化学性能。The modification of silica is based on γ-aminopropyltriethoxysilane as the modifier and ethylene glycol as the modifying solvent. After heating, suction filtration and drying, the final product - ultrafine hydrophobic Silica white powder, modification process is the key to determine the hydrophobicity of silica, in order to change the physical and chemical properties of its surface.
对制取所需的设备:混合容器、玛瑙研钵、产物舟、增力搅拌器、烧杯、研磨棒,烘箱、高温焙烧炉、筛网、循环水式真空抽滤泵、检测仪器、产物容器等要保持洁净,不得有污染。Equipment required for preparation: mixing container, agate mortar, product boat, booster stirrer, beaker, grinding rod, oven, high temperature roasting furnace, screen, circulating water vacuum filter pump, testing instrument, product container Keep it clean and free from contamination.
在制取超细疏水性二氧化硅白色粉末的过程中,由于溶胶、凝胶、调节pH值、抽滤、剧烈搅拌、高温焙烧、化合反应、改性处理、研磨、过筛、烘干、冷却,也会使制取的超细疏水性白色粉末的形貌发生微量变化,但不影响其化学物理性能、不影响与其他同类化学物质的匹配效果。In the process of preparing superfine hydrophobic silica white powder, due to sol, gel, pH adjustment, suction filtration, vigorous stirring, high temperature roasting, compound reaction, modification treatment, grinding, sieving, drying, Cooling will also slightly change the morphology of the prepared ultrafine hydrophobic white powder, but it will not affect its chemical and physical properties, nor will it affect the matching effect with other similar chemical substances.
制取超细疏水性二氧化硅白色粉末的化学物质配比是在一个预先设置的数值范围内进行确定的,以克、毫升为计量单位,在进行工业化制取时,以千克、升为计量单位。The ratio of chemical substances for preparing superfine hydrophobic silica white powder is determined within a preset value range, with grams and milliliters as measurement units, and for industrial production, kilograms and liters as measurement units unit.
图2所示,是高温炉焙烧升温、恒温、保温、冷却坐标关系图,当高温炉温度由A点常温20℃±3℃升至250℃±3℃时,升温速度为5℃/分钟,需时45分钟,相交于B点,恒温保温30分钟±1分钟,保温时段为B—C段,恒温保温后为冷却时段,即从C点降至D点,至常温20℃±3℃,在空气中自然冷却,速度为2.5℃/分钟,冷却时间为90分钟。As shown in Figure 2, it is a coordinate diagram of the high-temperature furnace roasting temperature rise, constant temperature, heat preservation, and cooling. When the temperature of the high-temperature furnace rises from the normal temperature of point A at 20°C±3°C to 250°C±3°C, the heating rate is 5°C/min. It takes 45 minutes, intersects at point B, and keeps warm for 30 minutes ± 1 minute. The holding period is B-C section. After constant temperature holding, it is the cooling period, that is, from point C to point D, to
图3所示,为改性过程中的冷凝回流图,四口烧瓶2置于电加热套1上,四口烧瓶2的左上部为温度计9、中上部为滴液漏斗8、搅拌器3、右上部为冷凝回流管4,冷凝回流管4的上部为空气口6、上侧部为进水管7,下侧部为出水管5,改性过程中,开启冷凝回流管4,进水管7进水,出水管5出水,形成流动的水流冷凝。As shown in Fig. 3, it is the condensation reflux diagram in the modification process, the four-
图4所示,溶胶、凝胶时酸碱度pH值与凝胶时间成反比,当pH值为9时,凝胶化时间缩短,当pH值为3时,反应缓慢,凝胶化时间拉长。As shown in Figure 4, the pH value of the sol and gel is inversely proportional to the gelation time. When the pH value is 9, the gelation time is shortened. When the pH value is 3, the reaction is slow and the gelation time is prolonged.
图5所示,溶胶、凝胶时pH值为3时,产物粒径小,为23nm,pH为9时,产物粒径大,为96nm..As shown in Figure 5, when the pH value of sol and gel is 3, the particle size of the product is small, 23nm, and when the pH is 9, the particle size of the product is large, 96nm..
图6、7所示,去离子水与正硅酸乙酯的量的比值为n,即n=50毫升∶5毫升,n值的大小将会影响凝胶时间和产物的粒径,当n大于10时,n值越大去离子水量越多,缩聚物浓度降低,溶胶粘度下降,凝胶时间越长,n值与产物粒径成正比,n值越大,粒径越大;n小于10时,n值越大,水量越多,凝胶时间越短,且n值与产物粒径成反比,n值越大粒径越小;n=10时凝胶时间最短,凝胶时间为30分钟,产物平均粒径最小,为63.5nm.,n=10为最佳。Shown in Fig. 6, 7, the ratio of the amount of deionized water and tetraethyl orthosilicate is n, i.e. n=50 milliliters: 5 milliliters, the size of n value will affect the particle diameter of gel time and product, when n When it is greater than 10, the larger the n value, the more deionized water, the lower the concentration of the polycondensate, the lower the viscosity of the sol, and the longer the gel time. The n value is proportional to the particle size of the product. The larger the n value, the larger the particle size; At 10, the larger the n value, the more water, the shorter the gel time, and the n value is inversely proportional to the particle size of the product, the larger the n value, the smaller the particle size; the gel time is the shortest when n=10, and the gel time is After 30 minutes, the average particle size of the product is the smallest, which is 63.5nm., and n=10 is the best.
图8所示,溶液温度为60℃时,凝胶时间为50分钟,温度越高,凝胶时间越短,成反比。As shown in Figure 8, when the solution temperature is 60°C, the gel time is 50 minutes, and the higher the temperature, the shorter the gel time, which is inversely proportional.
图9所示,溶液温度为60℃时,产物平均粒径为63.5nm,当温度升高,产物粒径越大,成正比。As shown in Figure 9, when the solution temperature is 60°C, the average particle size of the product is 63.5nm. When the temperature rises, the particle size of the product increases, which is proportional.
图10所示,为疏水性二氧化硅白色粉末透射电镜1×104倍形貌,产物为疏水性非晶粉状物,其颗粒尺寸为60—70nm。As shown in Figure 10, it is the 1×10 4 times appearance of the hydrophobic silicon dioxide white powder transmission electron microscope, and the product is a hydrophobic amorphous powder with a particle size of 60-70nm.
图11所示,为产物粒径分布状态,粒径主要集中在60—70nm。As shown in Figure 11, it is the particle size distribution state of the product, and the particle size is mainly concentrated at 60-70nm.
图12所示,为产物X—射线衍射峰强度状态图,纵坐标为相对强度指数,横坐标为X—射线衍射峰强度2θ角,2θ=21°处有一个馒头峰,强度数字为35。As shown in Figure 12, it is a product X-ray diffraction peak intensity state diagram, the ordinate is the relative intensity index, and the abscissa is the 2θ angle of the X-ray diffraction peak intensity, there is a steamed bun peak at 2θ=21°, and the intensity number is 35.
图13所示,为改性时间与羟基紫外线吸收率对比表,改性处理与产物吸收率成曲线关系,改性时间为2小时,紫外线吸收率最小可为4.1%,其数值为0.0058,其物理化学性能最好。As shown in Figure 13, it is a comparison table of modification time and hydroxyl ultraviolet absorption rate. The modification treatment has a curvilinear relationship with the product absorption rate. The modification time is 2 hours, and the ultraviolet absorption rate can be at least 4.1%, and its value is 0.0058. The physical and chemical properties are the best.
实施例1:Example 1:
各制取设备处于准工作状态;All production equipment is in ready working condition;
按配比精选称取正硅酸乙酯5毫升,无水乙醇50毫升,去离子水50毫升,氯化氨0.5毫升,氨水0.20毫升,盐酸0.3毫升,乙二醇50毫升,γ—氨丙基三乙氧基硅烷0.5毫升;Select and weigh 5 milliliters of tetraethyl orthosilicate, 50 milliliters of absolute ethanol, 50 milliliters of deionized water, 0.5 milliliters of ammonium chloride, 0.20 milliliters of ammonia water, 0.3 milliliters of hydrochloric acid, 50 milliliters of ethylene glycol, γ-aminopropyl 0.5 ml of triethoxysilane;
溶胶,将化学物质正硅酸乙酯5毫升置于三口烧瓶中,加入无水乙醇50毫升,5分钟后,滴入去离子水50毫升,搅拌均匀,使其澄清;Sol, put 5 milliliters of the chemical substance ethyl orthosilicate in a three-necked flask, add 50 milliliters of absolute ethanol, after 5 minutes, drop in 50 milliliters of deionized water, stir evenly, and make it clear;
调节pH值:加热温度60℃±1℃Adjust pH value:
加入氯化氨0.5毫升,盐酸0.3毫升,剧烈搅拌3分钟±0.3分钟,恒温保温12分钟±1分钟,pH值=3—4,偏酸性;Add 0.5 ml of ammonium chloride, 0.3 ml of hydrochloric acid, stir vigorously for 3 minutes ± 0.3 minutes, keep warm at constant temperature for 12 minutes ± 1 minute, pH value = 3-4, slightly acidic;
加入氨水0.20毫升,搅拌器剧烈搅拌15分钟,pH=8—9,偏碱性;Add 0.20 ml of ammonia water, stir vigorously with a stirrer for 15 minutes, pH = 8-9, slightly alkaline;
凝胶,成湿性凝胶产物;Gel, forming a wet gel product;
烘干,烘箱中进行,烘干温度60℃±1℃,时间90分钟±1分钟,成干性凝胶产物;Drying is carried out in an oven, the drying temperature is 60°C ± 1°C, and the drying time is 90 minutes ± 1 minute to form a dry gel product;
研磨、过筛,180目筛网,反复进行;Grinding, sieving, 180 mesh screen, repeated;
焙烧,将二氧化硅粉末置于产物舟内,并一起放入高温炉中焙烧:焙烧温度为250℃±3℃,恒温保温30分钟±1分钟,成干性凝胶产物;Roasting, put the silica powder in the product boat, and put them together in a high-temperature furnace for roasting: the roasting temperature is 250°C ± 3°C, and the temperature is kept at a constant temperature for 30 minutes ± 1 minute to form a dry gel product;
冷却,取出干性凝胶产物后在空气中冷却;Cooling, cooling in air after taking out the dry gel product;
改性:modified:
加入改性溶剂:二氧化硅粉末+改性溶剂乙二醇50毫升,溶解;Add modified solvent: silicon dioxide powder + modified
加入改性添加剂:γ—氨丙基三乙氧基硅烷,0.5毫升;Add modification additive: γ-aminopropyltriethoxysilane, 0.5 ml;
改性化合反应:加热状态下进行,加热温度198℃±0.5℃,时间120分钟±1分钟;Modification and compounding reaction: carried out under heating, the heating temperature is 198°C ± 0.5°C, and the time is 120 minutes ± 1 minute;
抽滤:将改性混合溶液在循环水式真空泵中抽滤,抽滤后成粘稠状白色产物。Suction filtration: The modified mixed solution is suction-filtered in a circulating water-type vacuum pump, and a viscous white product is formed after suction filtration.
烘箱中烘干:将粘稠状白色产物置于烘箱中,温度为200℃±1℃,烘干60分钟±1分钟,烘干后成超细疏水性二氧化硅白色粉末;Drying in an oven: put the viscous white product in an oven at a temperature of 200°C ± 1°C, and dry for 60 minutes ± 1 minute. After drying, it will become an ultrafine hydrophobic silicon dioxide white powder;
收集产物:将超细疏水性二氧化硅白色粉末置于产物容器中,从而完成了制取的全过程。Collecting the product: Put the superfine hydrophobic silicon dioxide white powder in the product container, thus completing the whole process of preparation.
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