CN107174950A - The positive osmosis composite membrane of high-performance and preparation method that a kind of graphene oxide is modified - Google Patents
The positive osmosis composite membrane of high-performance and preparation method that a kind of graphene oxide is modified Download PDFInfo
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- 239000012528 membrane Substances 0.000 title claims abstract description 88
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 229910021389 graphene Inorganic materials 0.000 title claims abstract description 51
- 239000002131 composite material Substances 0.000 title claims abstract description 42
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 230000004907 flux Effects 0.000 claims abstract description 30
- 229920002492 poly(sulfone) Polymers 0.000 claims abstract description 24
- 239000004952 Polyamide Substances 0.000 claims abstract description 22
- 229920002647 polyamide Polymers 0.000 claims abstract description 22
- 238000005266 casting Methods 0.000 claims abstract description 17
- 150000003839 salts Chemical class 0.000 claims abstract description 12
- 230000002441 reversible effect Effects 0.000 claims abstract description 11
- 238000012360 testing method Methods 0.000 claims abstract description 9
- 235000010482 polyoxyethylene sorbitan monooleate Nutrition 0.000 claims abstract description 6
- 229920000053 polysorbate 80 Polymers 0.000 claims abstract description 6
- 239000002904 solvent Substances 0.000 claims abstract description 6
- 238000012695 Interfacial polymerization Methods 0.000 claims abstract description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract 2
- 238000009292 forward osmosis Methods 0.000 claims description 35
- 239000012071 phase Substances 0.000 claims description 18
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 12
- WZCQRUWWHSTZEM-UHFFFAOYSA-N 1,3-phenylenediamine Chemical compound NC1=CC=CC(N)=C1 WZCQRUWWHSTZEM-UHFFFAOYSA-N 0.000 claims description 9
- 229940018564 m-phenylenediamine Drugs 0.000 claims description 9
- 229910021642 ultra pure water Inorganic materials 0.000 claims description 9
- 239000012498 ultrapure water Substances 0.000 claims description 9
- 238000002715 modification method Methods 0.000 claims description 8
- UWCPYKQBIPYOLX-UHFFFAOYSA-N benzene-1,3,5-tricarbonyl chloride Chemical compound ClC(=O)C1=CC(C(Cl)=O)=CC(C(Cl)=O)=C1 UWCPYKQBIPYOLX-UHFFFAOYSA-N 0.000 claims description 7
- 238000003756 stirring Methods 0.000 claims description 7
- 239000011521 glass Substances 0.000 claims description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 6
- 229940057847 polyethylene glycol 600 Drugs 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021641 deionized water Inorganic materials 0.000 claims description 4
- 229920000728 polyester Polymers 0.000 claims description 4
- 238000009295 crossflow filtration Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 239000000654 additive Substances 0.000 claims description 2
- 230000000996 additive effect Effects 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 239000003607 modifier Substances 0.000 claims description 2
- 210000004379 membrane Anatomy 0.000 claims 19
- 210000002469 basement membrane Anatomy 0.000 claims 2
- 238000006116 polymerization reaction Methods 0.000 claims 2
- 239000002202 Polyethylene glycol Substances 0.000 claims 1
- 239000008346 aqueous phase Substances 0.000 claims 1
- 238000005470 impregnation Methods 0.000 claims 1
- 229920001223 polyethylene glycol Polymers 0.000 claims 1
- 150000003457 sulfones Chemical class 0.000 claims 1
- 238000003786 synthesis reaction Methods 0.000 claims 1
- 238000005516 engineering process Methods 0.000 abstract description 11
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- 239000010410 layer Substances 0.000 description 18
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 6
- 230000004048 modification Effects 0.000 description 5
- 238000012986 modification Methods 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 238000010612 desalination reaction Methods 0.000 description 4
- 238000011160 research Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000001728 nano-filtration Methods 0.000 description 3
- 238000001223 reverse osmosis Methods 0.000 description 3
- 239000011780 sodium chloride Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000002525 ultrasonication Methods 0.000 description 3
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- 230000002829 reductive effect Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical group CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 description 1
- -1 65.0%-80.0wt% Substances 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 241000589517 Pseudomonas aeruginosa Species 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000002457 bidirectional effect Effects 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000003859 lipid peroxidation Effects 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000009285 membrane fouling Methods 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000036542 oxidative stress Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000001509 sodium citrate Substances 0.000 description 1
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/002—Forward osmosis or direct osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/10—Testing of membranes or membrane apparatus; Detecting or repairing leaks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0011—Casting solutions therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0013—Casting processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0016—Coagulation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0081—After-treatment of organic or inorganic membranes
- B01D67/0088—Physical treatment with compounds, e.g. swelling, coating or impregnation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
- B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/02—Details relating to pores or porosity of the membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/36—Hydrophilic membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
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- B01D2325/48—Antimicrobial properties
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- Chemical & Material Sciences (AREA)
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- Engineering & Computer Science (AREA)
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种氧化石墨烯改性的高性能正渗透复合膜及制备方法,尤其是涉及一种高性能正渗透复合膜的制备方法。The invention relates to a high-performance forward osmosis composite membrane modified by graphene oxide and a preparation method thereof, in particular to a preparation method of a high-performance forward osmosis composite membrane.
背景技术Background technique
我国是一个水资源极度匮乏的国家,人均占有量仅为世界平均水平的四分之一。人口的日益增长和工业的迅速发展,使得水资源短缺问题日益严重。水处理技术的发展为人们解决水资源短缺问题提供了方向。膜分离技术作为一种高效、环保、节能的新型分离技术在水处理技术中占据重要地位。其主要包括微滤、超滤、纳滤、反渗透、正渗透等。其中,反渗透较其它几种技术发展较为成熟,但由于其操作压力高、能耗高、膜污染严重,在实际应用中具有一定的局限性。纳滤膜能截留小分子有机物及盐类,操作压力低,但污染问题也较为严重。与反渗透和纳滤等膜分离技术相比,正渗透技术具有低能耗、高脱盐率、抗污染能力强等优点,近年来引起了广泛关注。my country is a country that is extremely scarce in water resources, and the per capita water resources are only a quarter of the world's average level. The increasing population and the rapid development of industry make the problem of water shortage increasingly serious. The development of water treatment technology provides a direction for people to solve the problem of water shortage. As a new separation technology with high efficiency, environmental protection and energy saving, membrane separation technology occupies an important position in water treatment technology. It mainly includes microfiltration, ultrafiltration, nanofiltration, reverse osmosis, forward osmosis, etc. Among them, reverse osmosis is more mature than other technologies, but due to its high operating pressure, high energy consumption, and serious membrane fouling, it has certain limitations in practical application. The nanofiltration membrane can intercept small molecular organic matter and salts, and the operating pressure is low, but the pollution problem is also relatively serious. Compared with membrane separation technologies such as reverse osmosis and nanofiltration, forward osmosis technology has the advantages of low energy consumption, high desalination rate, and strong anti-pollution ability, and has attracted widespread attention in recent years.
目前,正渗透技术的研究主要集中在两个方面:高性能膜材料的制备和高效率汲取液的选择。膜是整个正渗透分离过程的核心,因此制备高性能的膜材料对于提高系统的整体性能至关重要。聚砜、醋酸纤维素等都是最常用的制膜材料。其中,聚砜以其良好的化学稳定性、热稳定性、成膜机械性而应用广泛。但是在实际应用中,常规的聚砜膜孔径较大、孔隙率较小、膜表面较粗糙,造成水通量小、脱盐效果差,易污染等问题。因此,开发制备高性能的正渗透膜具有重要意义。At present, the research of forward osmosis technology mainly focuses on two aspects: the preparation of high-performance membrane materials and the selection of high-efficiency draw liquid. Membranes are the core of the entire forward osmosis separation process, so the preparation of high-performance membrane materials is crucial to improving the overall performance of the system. Polysulfone and cellulose acetate are the most commonly used membrane materials. Among them, polysulfone is widely used because of its good chemical stability, thermal stability, and film-forming mechanical properties. However, in practical applications, the conventional polysulfone membrane has large pore size, small porosity, and rough membrane surface, resulting in problems such as low water flux, poor desalination effect, and easy pollution. Therefore, it is of great significance to develop and prepare high-performance forward osmosis membranes.
聚酰胺复合膜具有非对称性的特殊结构,由水相(间苯二胺)的含胺基官能团与油相(均苯三酰氯)的含酰氯基团在多孔支撑层表面聚合而成。聚酰胺复合层能够使膜表面粗糙度降低,亲水性提高,从而增加膜的水通量以及抗污染性能。另外,聚酰胺复合膜可以实现对多孔支撑层和超薄活性层的双向优化,通过采用各自最优条件实现膜性能整体提高。The polyamide composite membrane has an asymmetric special structure, which is formed by polymerizing the amine-containing functional groups of the water phase (m-phenylenediamine) and the acid chloride groups of the oil phase (trimesyl chloride) on the surface of the porous support layer. The polyamide composite layer can reduce the surface roughness of the membrane and improve the hydrophilicity, thereby increasing the water flux and anti-pollution performance of the membrane. In addition, the polyamide composite membrane can achieve bidirectional optimization of the porous support layer and the ultra-thin active layer, and the overall performance of the membrane can be improved by using the respective optimal conditions.
对多孔支撑层进行改性是提高正渗透膜性能的另一重要途径,常用的改性方法有:共混改性、表面接枝改性、涂覆改性、等离子体改性。其中,共混改性是指将固相物质加入到铸膜液中形成三相空间来制备正渗透膜,方法操作简单,效果明显,能够直接改变膜的基体结构,如孔径大小,孔壁粗糙度等,以此提高膜的性能。Modifying the porous support layer is another important way to improve the performance of the forward osmosis membrane. The commonly used modification methods include: blending modification, surface graft modification, coating modification, and plasma modification. Among them, blending modification refers to adding solid phase substances into the casting solution to form a three-phase space to prepare the forward osmosis membrane. The method is simple to operate and the effect is obvious. It can directly change the matrix structure of the membrane, such as the pore size and the roughness of the pore wall. Degree, etc., in order to improve the performance of the membrane.
近年来,纳米材料以其较高的比表面积和优异的物理化学特性成为膜技术领域研究的热点。其中,氧化石墨烯作为一种由碳原子构成的片状结构的纳米材料,具有大量羧基、羟基、环氧基等亲水性官能团。同时氧化石墨烯能够破坏细胞膜或者诱导氧化应激杀死细菌,内含的羟基自由基亦能够加剧生物细胞的脂质过氧化,对于膜表面生物膜的形成具有明显的抑制作用。因此,基于聚酰胺复合膜的特殊结构以及氧化石墨烯的亲水性及抑菌性,将氧化石墨烯与膜材料共混制备正渗透支撑层,再通过界面聚合聚酰胺层,进而有效提高正渗透膜的渗透和脱盐性能,以及膜的抗污染性,为膜技术在水处理中的广泛应有提供技术支持。In recent years, nanomaterials have become a research hotspot in the field of membrane technology due to their high specific surface area and excellent physical and chemical properties. Among them, graphene oxide, as a sheet-like nanomaterial composed of carbon atoms, has a large number of hydrophilic functional groups such as carboxyl groups, hydroxyl groups, and epoxy groups. At the same time, graphene oxide can destroy cell membranes or induce oxidative stress to kill bacteria, and the contained hydroxyl radicals can also intensify the lipid peroxidation of biological cells, which has a significant inhibitory effect on the formation of biofilms on the membrane surface. Therefore, based on the special structure of the polyamide composite membrane and the hydrophilicity and antibacterial properties of graphene oxide, the forward osmosis support layer was prepared by blending graphene oxide and membrane materials, and then the polyamide layer was polymerized through the interface to effectively improve the forward osmosis. The permeability and desalination performance of the permeable membrane, as well as the anti-fouling property of the membrane, provide technical support for the extensive use of membrane technology in water treatment.
发明内容Contents of the invention
本发明的目的是针对现有正渗透膜存在的通量低、脱盐效果差、抗污染性能低的问题,制备一种高性能的正渗透复合膜并提供其制备方法。The object of the present invention is to prepare a high-performance forward osmosis composite membrane and provide a preparation method for the problems of low flux, poor desalination effect and low anti-pollution performance of the existing forward osmosis membrane.
一种氧化石墨烯改性的高性能正渗透复合膜及制备方法,具体操作步骤完成如下:A high-performance forward osmosis composite membrane modified by graphene oxide and its preparation method, the specific operation steps are as follows:
1.氧化石墨烯/聚砜支撑层的制备1. Preparation of graphene oxide/polysulfone support layer
高性能平板式氧化石墨烯/聚砜共混正渗透膜铸膜液配方的组成为:膜材料为聚砜, 8.0%~25.0wt%;添加剂为聚乙二醇600,0~20.0wt%;改性剂为氧化石墨烯,0~1.5wt%;溶剂为N,N-二甲基甲酰胺,65.0%~80.0wt%;增溶剂为吐温80,0.5%~2wt%。The composition of the high-performance planar graphene oxide/polysulfone blended forward osmosis membrane casting liquid formula is as follows: the membrane material is polysulfone, 8.0%-25.0wt%; the additive is polyethylene glycol 600, 0-20.0wt%; The modifier is graphene oxide, 0-1.5wt%, the solvent is N,N-dimethylformamide, 65.0%-80.0wt%, and the solubilizer is Tween 80, 0.5%-2wt%.
首先将N,N-二甲基甲酰胺、聚乙二醇600、吐温80按照一定的比例加入到三口烧瓶中,然后将一定量的氧化石墨烯加入到溶液中,超声10~60min,使氧化石墨烯在溶液中均匀分散;超声结束后,将溶液移至磁力搅拌器上,搅拌3~10min,加入聚砜材料,在50~70℃温度下搅拌溶解6~10h,得到均匀的氧化石墨烯/聚砜铸膜液;然后,将铸膜液在反应温度下静止 4~8h,脱除铸膜液中的气泡;最后,将一定量的铸膜液倒在置有目数为80~120的聚酯筛网的玻璃板上,用厚度为50~200μm的刮刀刮制成膜,浸入超纯水中凝固成膜,待膜自动从玻璃板脱离后,在超纯水中浸泡24~72h,每隔6小时换一次水,即得到平板式氧化石墨烯/聚砜支撑层。First, add N,N-dimethylformamide, polyethylene glycol 600, and Tween 80 into a three-necked flask according to a certain ratio, and then add a certain amount of graphene oxide into the solution, and ultrasonicate for 10 to 60 minutes to make Graphene oxide is uniformly dispersed in the solution; after ultrasonication, move the solution to a magnetic stirrer, stir for 3-10 minutes, add polysulfone material, stir and dissolve at 50-70°C for 6-10 hours, and obtain uniform graphite oxide ethylene/polysulfone casting solution; then, the casting solution was left to stand still at the reaction temperature for 4 to 8 hours to remove the air bubbles in the casting solution; finally, a certain amount of casting solution was poured into the Use a scraper with a thickness of 50-200 μm to form a film on a glass plate of 120 polyester mesh, immerse in ultra-pure water to solidify to form a film, and after the film is automatically separated from the glass plate, soak in ultra-pure water for 24-24 μm After 72 hours, the water was changed every 6 hours to obtain a flat graphene oxide/polysulfone support layer.
2.氧化石墨烯/聚酰胺复合膜的制备2. Preparation of graphene oxide/polyamide composite membrane
由界面聚合法在支撑层上合成聚酰胺层。首先将基膜浸于2~4wt%的间苯二胺(MPD)水相中3~5min,将基膜从水相中取出后,用超纯水冲掉支撑层背面溶液,再用滤纸吸干膜两侧的水渍;然后将膜浸泡于油相中,即浓度为0.15~0.25wt%的均苯三酰氯(TMC)的正己烷溶液, 1~3min后取出,并去除多余的油相。即得到氧化石墨烯/聚酰胺正渗透复合膜。为使聚酰胺复合层聚合的更加牢固,将复合膜在干燥箱内以40-80℃热处理5~10min,取出,保存在去离子水中备用。The polyamide layer was synthesized on the support layer by interfacial polymerization. First, immerse the base film in 2-4wt% m-phenylenediamine (MPD) water phase for 3-5 minutes, take the base film out of the water phase, wash off the solution on the back of the support layer with ultrapure water, and then absorb it with filter paper. Water stains on both sides of the dry film; then soak the film in the oil phase, that is, the n-hexane solution of trimesoyl chloride (TMC) with a concentration of 0.15 to 0.25 wt%, take it out after 1 to 3 minutes, and remove the excess oil phase . That is, the graphene oxide/polyamide forward osmosis composite membrane is obtained. In order to make the polyamide composite layer polymerized more firmly, heat-treat the composite film in a drying oven at 40-80°C for 5-10 minutes, take it out, and store it in deionized water for later use.
在氧化石墨烯改性的高性能正渗透复合膜的制备过程中,通过控制铸膜液中聚砜、聚乙二醇600、氧化石墨烯的混合比例以及铸膜液搅拌溶解温度等指标,对制备条件进行优化,进而控制所制备的共混正渗透膜的结构与性能。将制备好的正渗透复合膜置于错流过滤系统中进行测试,考察氧化石墨烯改性的正渗透复合膜的水通量、反向盐通量以及抗污染性能。In the preparation process of the high-performance forward osmosis composite membrane modified by graphene oxide, by controlling the mixing ratio of polysulfone, polyethylene glycol 600, and graphene oxide in the casting solution and the stirring and dissolving temperature of the casting solution, the The preparation conditions were optimized to control the structure and performance of the prepared blended forward osmosis membrane. The prepared forward osmosis composite membrane was tested in a cross-flow filtration system to investigate the water flux, reverse salt flux and anti-pollution performance of the graphene oxide modified forward osmosis composite membrane.
有益效果:Beneficial effect:
本发明中氧化石墨烯/聚酰胺复合膜的优点在于:由氧化石墨烯共混的聚砜支撑层具有结构稳定、孔隙率高、膜孔小、亲水性高等特点,可同时保证复合膜具有较高的膜通量和较低的反向盐通量。另外,根据已有研究报道的氧化石墨烯具有杀菌作用,以及对膜亲水性的提高,可使制备的氧化石墨烯/聚酰胺复合膜具有很强的抗生物污染性能。The advantage of the graphene oxide/polyamide composite membrane in the present invention is that the polysulfone support layer blended with graphene oxide has the characteristics of stable structure, high porosity, small membrane pores, and high hydrophilicity, which can simultaneously ensure that the composite membrane has Higher membrane flux and lower reverse salt flux. In addition, according to existing research reports, graphene oxide has a bactericidal effect and improves the hydrophilicity of the membrane, so that the prepared graphene oxide/polyamide composite membrane has strong anti-biological fouling properties.
具体实施方式detailed description
下面将结合本发明具体实施例,对本发明的技术方案进行验证,所验证的实施例仅为本发明的部分实施例。基于本发明中的实施例,本领域研究人员在没有做出任何创造性劳动前提下所获得的其他实施例,都属于本发明保护的范围。In the following, the technical solutions of the present invention will be verified in combination with specific embodiments of the present invention, and the verified embodiments are only part of the embodiments of the present invention. Based on the embodiments of the present invention, other embodiments obtained by researchers in the field without any creative effort all belong to the protection scope of the present invention.
实施例1Example 1
首先将N,N-二甲基甲酰胺、聚乙二醇600、吐温80分别按照70wt%、13.3wt%、1wt%的比例加入到三口烧瓶中,然后将0.2wt%的单层超纯氧化石墨烯加入到溶液中,超声30min,使氧化石墨烯在溶液中充分均匀分散,超声结束后,将溶液移至磁力搅拌器上,搅拌5min后加入聚砜材料,在70℃温度下搅拌溶解8h,得到均匀的氧化石墨烯/聚砜铸膜液;然后,铸膜液在反应温度下静止5h,脱除铸膜液中的气泡;最后,将一定量的铸膜液倒在置有目数为 100的聚酯筛网的玻璃板上,用厚度为50μm的刮刀刮制成膜,浸入超纯水中凝固成膜,待膜自动从玻璃板脱离后,在超纯水中浸泡72h,每隔6小时换一次水,即得到平板式氧化石墨烯 /聚砜支撑层。First, N,N-dimethylformamide, polyethylene glycol 600, and Tween 80 were added to a three-necked flask at the ratio of 70wt%, 13.3wt%, and 1wt%, respectively, and then 0.2wt% of a single-layer ultrapure Graphene oxide was added to the solution, and the graphene oxide was fully and uniformly dispersed in the solution by ultrasonication for 30 minutes. After the ultrasonication was over, the solution was moved to a magnetic stirrer, and polysulfone material was added after stirring for 5 minutes, and stirred and dissolved at a temperature of 70°C. 8h to obtain a uniform graphene oxide/polysulfone casting solution; then, the casting solution was left at the reaction temperature for 5h to remove the air bubbles in the casting solution; finally, a certain amount of casting solution was poured into a Use a scraper with a thickness of 50 μm to form a film on a glass plate with 100 polyester screens, immerse in ultrapure water to solidify to form a film, and after the film is automatically detached from the glass plate, immerse in ultrapure water for 72 hours. Change the water every 6 hours to obtain a flat graphene oxide/polysulfone support layer.
将制备好的支撑层首先浸于3.5wt%的间苯二胺(MPD)的水相中5min,将基膜从水相中取出后,用去离子水冲掉支撑层背面的溶液,再用滤纸吸干膜两侧的水渍;然后将膜浸泡于油相中,即浓度为0.15wt%的均苯三酰氯(TMC)的正己烷溶液,2min后取出,并去除多余的油相,得到氧化石墨烯/聚酰胺正渗透复合膜(GO/TFC膜)。利用2M NaCl溶液作为驱动液,去离子水作为原料液,在1h的测试时间里,所制备膜的平均水通量达到11.29LMH,反向盐通量为2.1gMH。The prepared support layer was first immersed in the water phase of 3.5wt% m-phenylenediamine (MPD) for 5min, after the base film was taken out from the water phase, the solution on the back of the support layer was washed away with deionized water, and then Filter paper blots the water stains on both sides of the film; then the film is soaked in the oil phase, i.e. the n-hexane solution of trimesoyl chloride (TMC) with a concentration of 0.15wt%, is taken out after 2min, and the excess oil phase is removed to obtain Graphene oxide/polyamide forward osmosis composite membrane (GO/TFC membrane). Using 2M NaCl solution as the driving solution and deionized water as the raw material solution, the average water flux of the prepared membrane reached 11.29LMH and the reverse salt flux was 2.1gMH during the test time of 1h.
为测试氧化石墨烯正渗透复合膜的抗污染性能,本实施例利用铜绿假单胞菌作为污染微生物,采用合成废水模拟二级出水(配水成分为:1.2mM柠檬酸钠、0.8mM NH4Cl、0.5mM NaHCO3、0.2mM K2HPO4、8.0mM NaCl、0.2mM CaCl2·H2O、0.15mM MgSO4·7H2O,微生物浓度为5×107CFU/L),对膜进行抗污染实验研究。利用2M NaCl作为驱动液,合成废水作为原料液。连续运行两天污染实验后,经过计算,由生物污染引起的水通量下降幅度为11%。In order to test the anti-pollution performance of the graphene oxide forward osmosis composite membrane, this example uses Pseudomonas aeruginosa as the polluting microorganism, and uses synthetic wastewater to simulate the secondary effluent (water composition: 1.2mM sodium citrate, 0.8mM NH 4 Cl , 0.5mM NaHCO 3 , 0.2mM K 2 HPO 4 , 8.0mM NaCl, 0.2mM CaCl 2 ·H 2 O, 0.15mM MgSO 4 ·7H 2 O, the microbial concentration is 5×10 7 CFU/L), the membrane was tested Experimental research on anti-pollution. 2M NaCl was used as the driving solution, and synthetic wastewater was used as the raw material solution. After running the pollution experiment for two consecutive days, it was calculated that the decrease in water flux caused by biofouling was 11%.
实施例2Example 2
基于实施例1中的改性方法,不同之处仅在于制备支撑层的过程中,没有加入氧化石墨烯,得到聚砜聚酰胺正渗透复合膜(TFC膜)。同样的,对所制备的正渗透膜进行测试,在1h的测试时间里,膜的平均水通量为5.9LMH,反向盐通量为8gMH;在生物污染实验中,经过连续运行两天的污染实验,由生物污染引起的水通量下降幅度为25%。Based on the modification method in Example 1, the only difference is that graphene oxide is not added during the preparation of the support layer to obtain a polysulfone polyamide forward osmosis composite membrane (TFC membrane). Similarly, the prepared forward osmosis membrane was tested. In the test time of 1h, the average water flux of the membrane was 5.9LMH, and the reverse salt flux was 8gMH; In the pollution experiment, the water flux decreased by 25% due to biofouling.
实施例1-2氧化石墨烯改性的正渗透复合膜以及未添加氧化石墨烯的正渗透复合膜各项测试数据详细对比如表1。Example 1-2 The detailed comparison of the test data of the forward osmosis composite membrane modified by graphene oxide and the forward osmosis composite membrane without graphene oxide is shown in Table 1.
表1Table 1
表中可以看出,由氧化石墨烯改性后的正渗透复合膜,水通量大幅提高、反向盐通量减小;而接触角降低,说明GO改性后的膜亲水性提高;孔隙率增加,说明对膜的孔径结构大大改善;通过抗污染测试,GO/TFC膜的抗污染性能优于传统的TFC膜。It can be seen from the table that the water flux of the forward osmosis composite membrane modified by graphene oxide is greatly increased, and the reverse salt flux is reduced; while the contact angle is reduced, indicating that the hydrophilicity of the membrane modified by GO is improved; The increase in porosity indicates that the pore structure of the membrane is greatly improved; through the anti-fouling test, the anti-fouling performance of the GO/TFC membrane is better than that of the traditional TFC membrane.
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