CN103480281A - Organic-inorganic ultrafiltration composite membrane and preparation method thereof - Google Patents
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Abstract
一种有机-无机超滤复合膜及其制备方法。复合膜由以重量份计的下列组分组成:15~20份聚合物树脂、占聚合物树脂0.02~2.0%的硅烷功能化氧化石墨烯、75~90份N-N二甲基乙酰胺和1~3份聚乙烯吡咯烷酮。本发明的优点是:制膜工艺简单,容易实现;经超声加机械搅拌使得硅烷功能化氧化石墨烯很好地分散到聚合物基体中;并且由于硅烷功能化氧化石墨烯与聚合物基体间超强的结合性能、超高的比表面以及表面较多的长聚合物链,使其能很好地分散在聚合物基体中,另外,硅烷功能化氧化石墨烯表面丰富的含氧官能团又能很好地增强超滤复合膜的亲水性,进而协同改善超滤复合膜的机械性能及抗污染性能。An organic-inorganic ultrafiltration composite membrane and a preparation method thereof. The composite film is composed of the following components in parts by weight: 15-20 parts of polymer resin, silane functionalized graphene oxide accounting for 0.02-2.0% of polymer resin, 75-90 parts of N-N dimethylacetamide and 1- 3 parts polyvinylpyrrolidone. The advantages of the present invention are: the film-making process is simple and easy to realize; the silane functionalized graphene oxide is well dispersed into the polymer matrix through ultrasonic and mechanical stirring; Strong binding performance, ultra-high specific surface area and long polymer chains on the surface make it well dispersed in the polymer matrix. In addition, the abundant oxygen-containing functional groups on the surface of silane-functionalized graphene oxide can be easily Better enhance the hydrophilicity of the ultrafiltration composite membrane, and then synergistically improve the mechanical properties and anti-pollution performance of the ultrafiltration composite membrane.
Description
技术领域technical field
本发明属于超滤膜功能化改性技术领域,特别是涉及一种硅烷功能化氧化石墨烯改性的有机-无机超滤复合膜及其制备方法。The invention belongs to the technical field of functional modification of ultrafiltration membranes, and in particular relates to a silane functionalized graphene oxide modified organic-inorganic ultrafiltration composite membrane and a preparation method thereof.
背景技术Background technique
有机聚合物作为一种综合性能优异的超滤膜材料,具有良好的化学稳定性、热稳定性和多孔性,但是由于其表面能低,并且具有极强烈的疏水性,因此易导致表面污染,从而严重地影响了产品的性能。近年来,针对聚合物超滤膜易污染问题,对其亲水性共混改性的研究逐渐活跃,已报道的改性材料主要有SiO2、Fe2O3、Al2O3、TiO2和低维碳纳米材料如氧化碳纳米管和石墨烯衍生物等无机材料。虽然利用这些材料对聚合物超滤膜改性后可使膜的渗透通量提高,功能性能得到较大改善,然而,这些方法也存在一些缺点,主要表现在:(1)改性材料与聚合物基体间的弱界面结合增加了界面缺陷,致使改性后的超滤复合膜机械强度有所下降;(2)由于无机粒子表面缺少丰富的官能团,因此粒子之间容易发生团聚,从而影响超滤复合膜的性能。因此,寻求一种既能增加超滤复合膜的机械性能又能强化其抗污染性能的方法十分必要。As an ultrafiltration membrane material with excellent comprehensive performance, organic polymer has good chemical stability, thermal stability and porosity, but due to its low surface energy and strong hydrophobicity, it is easy to cause surface pollution. Thereby seriously affecting the performance of the product. In recent years, in view of the problem of easy fouling of polymer ultrafiltration membranes, the research on its hydrophilic blending modification has gradually become active. The reported modified materials mainly include SiO 2 , Fe 2 O 3 , Al 2 O 3 , TiO 2 And low-dimensional carbon nanomaterials such as carbon oxide nanotubes and inorganic materials such as graphene derivatives. Although the use of these materials to modify the polymer ultrafiltration membrane can increase the permeation flux of the membrane and greatly improve the functional performance, however, these methods also have some shortcomings, which are mainly manifested in: (1) The relationship between the modified material and the polymerization The weak interfacial bonding between the substrates increases the interfacial defects, resulting in a decrease in the mechanical strength of the modified ultrafiltration composite membrane; (2) due to the lack of abundant functional groups on the surface of inorganic particles, the particles are prone to agglomeration, which affects the ultrafiltration composite membrane. performance of composite membranes. Therefore, it is necessary to find a method that can not only increase the mechanical properties of ultrafiltration composite membranes but also strengthen their anti-fouling properties.
发明内容Contents of the invention
为了解决上述问题,本发明的目的在于提供一种能够提高其机械性能和抗污染性能的硅烷功能化氧化石墨烯改性的有机-无机超滤复合膜及其制备方法。In order to solve the above problems, the object of the present invention is to provide a silane-functionalized graphene oxide modified organic-inorganic ultrafiltration composite membrane capable of improving its mechanical properties and anti-pollution properties and its preparation method.
为了达到上述目的,本发明提供的有机-无机超滤复合膜由以重量份计的下列组分组成:In order to achieve the above object, the organic-inorganic ultrafiltration composite membrane provided by the invention is made up of the following components in parts by weight:
所述的聚合物树脂选自聚偏氟乙烯、聚丙烯腈、聚砜和聚氨酯中的一种。The polymer resin is selected from one of polyvinylidene fluoride, polyacrylonitrile, polysulfone and polyurethane.
2、根据权利要求1所述的有机-无机超滤复合膜,其特征在于:所述的硅烷功能化氧化石墨烯中的硅烷为γ-氨丙基三乙氧基硅烷(KH550)。2. The organic-inorganic ultrafiltration composite membrane according to claim 1, characterized in that the silane in the silane-functionalized graphene oxide is γ-aminopropyltriethoxysilane (KH550).
3、一种如权利要求1所述的有机-无机超滤复合膜的制备方法,其特征在于:所述的制备方法包括按顺序进行的下列步骤:3. A method for preparing an organic-inorganic ultrafiltration composite membrane as claimed in claim 1, characterized in that: said preparation method comprises the following steps in order:
1)将按照上述重量比称取的硅烷功能化氧化石墨烯加入到N-N二甲基乙酰胺中,然后超声处理0.5~2小时以使其分散均匀;1) Add the silane-functionalized graphene oxide weighed according to the above weight ratio to N-N dimethylacetamide, and then ultrasonically treat it for 0.5-2 hours to make it uniformly dispersed;
2)然后加入按照上述重量比称取的聚合物树脂和聚乙烯吡咯烷酮,之后机械搅拌5~24小时而得到硅烷功能化氧化石墨烯分散均匀的铸膜液;2) Then add the polymer resin and polyvinylpyrrolidone weighed according to the above weight ratio, and then mechanically stir for 5 to 24 hours to obtain a casting solution in which silane-functionalized graphene oxide is uniformly dispersed;
3)将上述铸膜液在20~30℃下静止放置1~3天以进行脱泡,然后在15~30℃下进行刮膜,待刮膜后的铸膜液在空气中挥发10~100秒后将其慢慢放入去离子水凝固液中成膜;3) Put the above-mentioned casting solution at 20-30°C for 1-3 days to defoam, then scrape the film at 15-30°C, and volatilize the casting solution in the air for 10-100 After a few seconds, slowly put it into the deionized water coagulation solution to form a film;
4)从凝固液中取出膜用去离子水冲洗干净,制得硅烷功能化氧化石墨烯改性的有机-无机超滤复合膜。4) The membrane was taken out from the coagulation solution and rinsed with deionized water to prepare a silane-functionalized graphene oxide-modified organic-inorganic ultrafiltration composite membrane.
本发明提供的有机-无机超滤复合膜是采用γ-氨丙基三乙氧基硅烷(KH550)功能化的氧化石墨烯来增强聚合物超滤膜的机械性能和抗污染性能,一方面通过氧化石墨烯中丰富的含氧官能团来增强超滤复合膜的亲水性,进而增强其抗污染性能,另一方面在充分保留氧化石墨烯官能团的同时引入长聚合物链,使聚合物链充分深入到聚合物基体中,因此能够很好地增强功能化氧化石墨烯与聚合物基体间的界面结合性,并极大地提高了功能化氧化石墨烯在聚合物基体中的分散性,从而实现超滤复合膜的机械性能和抗污染性能协同增强。The organic-inorganic ultrafiltration composite membrane provided by the invention uses graphene oxide functionalized with γ-aminopropyltriethoxysilane (KH550) to enhance the mechanical properties and anti-pollution properties of the polymer ultrafiltration membrane. The abundant oxygen-containing functional groups in graphene oxide enhance the hydrophilicity of the ultrafiltration composite membrane, thereby enhancing its anti-pollution performance. On the other hand, while fully retaining the functional groups of graphene oxide, long polymer chains are introduced to make the polymer chain fully It penetrates deep into the polymer matrix, so it can well enhance the interfacial bonding between the functionalized graphene oxide and the polymer matrix, and greatly improve the dispersion of the functionalized graphene oxide in the polymer matrix, so as to achieve ultra- The mechanical properties and antifouling performance of the filter composite membrane are synergistically enhanced.
本发明的优点是:制膜工艺简单,容易实现;经超声加机械搅拌使得硅烷功能化氧化石墨烯很好地分散到聚合物基体中;并且由于硅烷功能化氧化石墨烯与聚合物基体间超强的结合性能、超高的比表面以及表面较多的长聚合物链,使其能很好地分散在聚合物基体中,另外,硅烷功能化氧化石墨烯表面丰富的含氧官能团又能很好地增强超滤复合膜的亲水性,进而显著改善超滤复合膜的机械性能及抗污染性能。此外,硅烷功能化氧化石墨烯的加入对聚合物树脂原来的优良特性没有影响,还增加了膜的空间联系,延长了膜的使用寿命。The advantages of the present invention are: the film-making process is simple and easy to realize; the silane functionalized graphene oxide is well dispersed into the polymer matrix through ultrasonic and mechanical stirring; Strong binding performance, ultra-high specific surface area and long polymer chains on the surface make it well dispersed in the polymer matrix. In addition, the abundant oxygen-containing functional groups on the surface of silane-functionalized graphene oxide can be easily It can well enhance the hydrophilicity of the ultrafiltration composite membrane, and then significantly improve the mechanical properties and anti-pollution performance of the ultrafiltration composite membrane. In addition, the addition of silane-functionalized graphene oxide has no effect on the original excellent properties of the polymer resin, but also increases the spatial connection of the membrane and prolongs the service life of the membrane.
具体实施方式Detailed ways
实施例1Example 1
将0.075gγ-氨丙基三乙氧基硅烷功能化氧化石墨烯超声分散于84g作为溶剂的N-N二甲基乙酰胺中,2h后加入15g聚偏氟乙烯和1g作为致孔剂的聚乙烯吡咯烷酮,之后在450℃的水浴中加热搅拌24h,静置脱泡24h,采用自制刮刀控制一定的液膜厚度在洁净的玻璃板上刮膜,预蒸发30秒后,浸入去离子水中凝固,并反复换水以脱出溶剂和致孔剂,最后即可制成所述的硅烷功能化氧化石墨烯改性的有机-无机超滤复合膜。0.075g of γ-aminopropyltriethoxysilane functionalized graphene oxide was ultrasonically dispersed in 84g of N-N dimethylacetamide as a solvent, and 15g of polyvinylidene fluoride and 1g of polyvinylpyrrolidone as a porogen were added after 2h , then heat and stir in a water bath at 450°C for 24 hours, let stand for degassing for 24 hours, use a self-made scraper to control a certain thickness of the liquid film and scrape the film on a clean glass plate, pre-evaporate for 30 seconds, immerse in deionized water to solidify, and repeat The water is changed to remove the solvent and the porogen, and finally the silane functionalized graphene oxide modified organic-inorganic ultrafiltration composite membrane can be prepared.
将上述有机-无机超滤复合膜在去离子水中浸泡3天,然后利用机械拉伸装置和渗透过滤装置测试该超滤复合膜的机械强度与抗污染性能,结果表明本实施例提供的超滤复合膜的机械强度比纯聚偏氟乙烯膜提高了42.86%,并且抗污染性能明显提高,不可逆污染系数下降约60%。The organic-inorganic ultrafiltration composite membrane was soaked in deionized water for 3 days, and then the mechanical strength and anti-pollution performance of the ultrafiltration composite membrane were tested by using a mechanical stretching device and a permeation filtration device. The results showed that the ultrafiltration provided by this embodiment The mechanical strength of the composite membrane is 42.86% higher than that of the pure polyvinylidene fluoride membrane, and the anti-pollution performance is significantly improved, and the irreversible pollution coefficient is reduced by about 60%.
实施例2Example 2
将0.15gγ-氨丙基三乙氧基硅烷功能化氧化石墨烯超声分散于83g N-N二甲基乙酰胺中,1h后加入15g聚丙烯腈和1g聚乙烯吡咯烷酮,之后在50℃的水浴中加热搅拌30h,静置脱泡24h,采用自制刮刀控制一定的液膜厚度在洁净的玻璃板上刮膜,预蒸发30秒后,浸入去离子水中凝固,并反复换水以脱出溶剂和致孔剂,最后即可制成所述的硅烷功能化氧化石墨烯改性的有机-无机超滤复合膜。0.15g of γ-aminopropyltriethoxysilane functionalized graphene oxide was ultrasonically dispersed in 83g of N-N dimethylacetamide, 15g of polyacrylonitrile and 1g of polyvinylpyrrolidone were added after 1h, and then heated in a water bath at 50°C Stir for 30 hours, stand for defoaming for 24 hours, use a self-made scraper to control a certain thickness of the liquid film on a clean glass plate, pre-evaporate for 30 seconds, immerse in deionized water to solidify, and change the water repeatedly to remove the solvent and porogen , and finally the silane functionalized graphene oxide modified organic-inorganic ultrafiltration composite membrane can be prepared.
将上述有机-无机超滤复合膜在去离子水中浸泡4天,然后利用机械拉伸装置和渗透过滤装置测试该超滤复合膜的机械强度与抗污染性能,结果表明本实施例提供的超滤复合膜的机械强度比纯聚丙烯腈膜提高了50%,并且抗污染性能明显提高,不可逆污染系数下降约40%。The organic-inorganic ultrafiltration composite membrane was soaked in deionized water for 4 days, and then the mechanical strength and anti-pollution performance of the ultrafiltration composite membrane were tested by using a mechanical stretching device and a osmotic filtration device. The results showed that the ultrafiltration provided by this embodiment The mechanical strength of the composite membrane is 50% higher than that of the pure polyacrylonitrile membrane, and the anti-pollution performance is significantly improved, and the irreversible pollution coefficient is reduced by about 40%.
实施例3Example 3
将0.1gγ-氨丙基三乙氧基硅烷功能化氧化石墨烯超声分散于77g N-N二甲基乙酰胺中,2h后加入20g聚砜和3g聚乙烯吡咯烷酮,之后在40℃的水浴中加热搅拌20h,静置脱泡30h,采用自制刮刀控制一定的液膜厚度在洁净的玻璃板上刮膜,预蒸发30秒后,浸入去离子水中凝固,并反复换水以脱出溶剂和致孔剂,最后即可制成所述的硅烷功能化氧化石墨烯改性的有机-无机超滤复合膜。Ultrasonic dispersion of 0.1g of γ-aminopropyltriethoxysilane functionalized graphene oxide in 77g of N-N dimethylacetamide, 20g of polysulfone and 3g of polyvinylpyrrolidone was added after 2h, and then heated and stirred in a water bath at 40°C 20h, stand for defoaming for 30h, use a self-made scraper to control a certain thickness of the liquid film and scrape the film on a clean glass plate, pre-evaporate for 30 seconds, immerse in deionized water to solidify, and change the water repeatedly to remove the solvent and porogen. Finally, the silane functionalized graphene oxide modified organic-inorganic ultrafiltration composite membrane can be prepared.
将上述有机-无机超滤复合膜在去离子水中浸泡4天,然后利用机械拉伸装置和渗透过滤装置测试该超滤复合膜的机械强度与抗污染性能,结果表明本实施例提供的超滤复合膜的机械强度比纯聚砜膜提高了35.68%,并且抗污染性能明显提高,不可逆污染系数下降约60%。The organic-inorganic ultrafiltration composite membrane was soaked in deionized water for 4 days, and then the mechanical strength and anti-pollution performance of the ultrafiltration composite membrane were tested by using a mechanical stretching device and a osmotic filtration device. The results showed that the ultrafiltration provided by this embodiment The mechanical strength of the composite membrane is 35.68% higher than that of the pure polysulfone membrane, and the anti-pollution performance is significantly improved, and the irreversible pollution coefficient is reduced by about 60%.
实施例4Example 4
将0.2gγ-氨丙基三乙氧基硅烷功能化氧化石墨烯超声分散于79g N-N二甲基乙酰胺中,2h后加入20g聚氨酯和3g聚乙烯吡咯烷酮,之后在45℃的水浴中加热搅拌30h,静置脱泡24h,采用自制刮刀控制一定的液膜厚度在洁净的玻璃板上刮膜,预蒸发30秒后,浸入去离子水中凝固,并反复换水以脱出溶剂和致孔剂,最后即可制成所述的硅烷功能化氧化石墨烯改性的有机-无机超滤复合膜。Ultrasonic dispersion of 0.2g of γ-aminopropyltriethoxysilane functionalized graphene oxide in 79g of N-N dimethylacetamide, 20g of polyurethane and 3g of polyvinylpyrrolidone was added after 2h, and then heated and stirred in a water bath at 45°C for 30h , stand for defoaming for 24 hours, use a self-made scraper to control a certain thickness of the liquid film on a clean glass plate, scrape the film on a clean glass plate, pre-evaporate for 30 seconds, immerse in deionized water to solidify, and change the water repeatedly to remove the solvent and porogen, and finally The organic-inorganic ultrafiltration composite membrane modified by the silane functionalized graphene oxide can be prepared.
将上述有机-无机超滤复合膜在去离子水中浸泡3天,然后利用机械拉伸装置和渗透过滤装置测试该超滤复合膜的机械强度与抗污染性能,结果表明本实施例提供的超滤复合膜的机械强度比纯聚氨酯膜提高了65.71%,并且抗污染性能明显提高,不可逆污染系数下降约30%。The organic-inorganic ultrafiltration composite membrane was soaked in deionized water for 3 days, and then the mechanical strength and anti-pollution performance of the ultrafiltration composite membrane were tested by using a mechanical stretching device and a permeation filtration device. The results showed that the ultrafiltration provided by this embodiment The mechanical strength of the composite membrane is 65.71% higher than that of the pure polyurethane membrane, and the anti-pollution performance is significantly improved, and the irreversible pollution coefficient is reduced by about 30%.
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3650056B2 (en) * | 2001-11-08 | 2005-05-18 | コリア リサーチ インスティチュート オブ ケミカル テクノロジー | Super water-repellent organic / inorganic composite film |
CN102827386A (en) * | 2012-08-21 | 2012-12-19 | 江苏大学 | Preparation method of polyether-ether-ketone/graphene oxide nano-composite film |
CN103084074A (en) * | 2013-01-16 | 2013-05-08 | 天津工业大学 | Hydrophilic polyvinylidene fluoride modified separation membrane and preparation method thereof |
-
2013
- 2013-08-09 CN CN201310345495.7A patent/CN103480281A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3650056B2 (en) * | 2001-11-08 | 2005-05-18 | コリア リサーチ インスティチュート オブ ケミカル テクノロジー | Super water-repellent organic / inorganic composite film |
CN102827386A (en) * | 2012-08-21 | 2012-12-19 | 江苏大学 | Preparation method of polyether-ether-ketone/graphene oxide nano-composite film |
CN103084074A (en) * | 2013-01-16 | 2013-05-08 | 天津工业大学 | Hydrophilic polyvinylidene fluoride modified separation membrane and preparation method thereof |
Non-Patent Citations (1)
Title |
---|
王宗花等: "基于纳米材料有机一无机复合超滤膜的研究进展", 《工程塑料应用》, vol. 40, no. 1, 31 January 2012 (2012-01-31), pages 86 - 90 * |
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