[go: up one dir, main page]

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 PDF

Info

Publication number
CN107174950A
CN107174950A CN201710506514.8A CN201710506514A CN107174950A CN 107174950 A CN107174950 A CN 107174950A CN 201710506514 A CN201710506514 A CN 201710506514A CN 107174950 A CN107174950 A CN 107174950A
Authority
CN
China
Prior art keywords
graphene oxide
membrane
water
composite membrane
performance
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201710506514.8A
Other languages
Chinese (zh)
Inventor
杨禹
李媛
李航雨
侯立安
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing Normal University
Rocket Force University of Engineering of PLA
Original Assignee
Beijing Normal University
Rocket Force University of Engineering of PLA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Beijing Normal University, Rocket Force University of Engineering of PLA filed Critical Beijing Normal University
Priority to CN201710506514.8A priority Critical patent/CN107174950A/en
Publication of CN107174950A publication Critical patent/CN107174950A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/002Forward osmosis or direct osmosis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/10Testing of membranes or membrane apparatus; Detecting or repairing leaks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • B01D67/0009Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
    • B01D67/0011Casting solutions therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • B01D67/0009Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
    • B01D67/0013Casting processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • B01D67/0009Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
    • B01D67/0016Coagulation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081After-treatment of organic or inorganic membranes
    • B01D67/0088Physical treatment with compounds, e.g. swelling, coating or impregnation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12Composite membranes; Ultra-thin membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12Composite membranes; Ultra-thin membranes
    • B01D69/125In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/02Details relating to pores or porosity of the membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/36Hydrophilic membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/48Antimicrobial properties

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Dispersion Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The positive osmosis composite membrane of high-performance and preparation method being modified the invention discloses a kind of graphene oxide, belong to water-treatment technology field.Comprise the following steps:First by blending method, polysulfones, graphene oxide, Macrogol 600, Tween 80 and solvent are added in flask, casting solution is prepared, using phase inversion, graphene oxide/polysulfone supporting layer is made.Then the positive osmosis composite membrane of graphene oxide/polyamide is obtained in support layer surface composite polyamide active layer using interfacial polymerization mode.The positive osmosis composite membrane of graphene oxide/polyamide prepared by the present invention has the advantages that flux is high, reverse flux salt is small, resistance tocrocking is strong, its water flux is up to 9 12LMH, reverse flux salt is 2 4gMH, in antifouling property test, the flux fall caused by pollution is only 30% the 50% of unmodified membrane.

Description

一种氧化石墨烯改性的高性能正渗透复合膜及制备方法A high-performance forward osmosis composite membrane modified by graphene oxide and its preparation method

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

膜的分类Classification of membranes 水通量/LMHWater flux/LMH 反向盐通量/gMHReverse salt flux/gMH 接触角/°Contact angle/° 孔隙率Porosity 污染后通量下降幅度Decrease in flux after pollution GO/TFC膜GO/TFC membrane 11.2911.29 22 60.660.6 33%33% 11%11% TFC膜TFC membrane 5.95.9 88 47.3247.32 53%53% 25% 25%

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.

Claims (9)

1.一种氧化石墨烯改性的高性能正渗透复合膜及制备方法,其特征在于,包括如下步骤:1. A high-performance forward osmosis composite membrane and preparation method modified by graphene oxide, is characterized in that, comprises the steps: (1)氧化石墨烯/聚砜支撑层的制备(1) Preparation of graphene oxide/polysulfone support layer 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,超声至完全分散,加入聚砜材料,在一定温度下搅拌,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至完全脱泡;最后,将一定量的铸膜液倒在置有聚酯筛网的玻璃板上,用一定厚度的刮刀刮膜,浸入超纯水中凝固成膜,待膜自动从玻璃板上脱离后,在超纯水中浸泡至溶剂完全析出,即得到平板式氧化石墨烯/聚砜支撑层;Add N,N-dimethylformamide, polyethylene glycol 600, and Tween 80 into a three-necked flask according to a certain ratio, then add a certain amount of graphene oxide into the solution, ultrasonicate until completely dispersed, add poly The sulfone material is stirred at a certain temperature to obtain a uniform graphene oxide/polysulfone casting solution; then, the casting solution is kept at the reaction temperature until it is completely defoamed; finally, a certain amount of casting solution is poured into the Scrape the film with a scraper of a certain thickness on a glass plate with a polyester screen, immerse in ultra-pure water to solidify to form a film, and after the film is automatically detached from the glass plate, soak in ultra-pure water until the solvent is completely precipitated to obtain 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 利用界面聚合法在支撑层上合成聚酰胺层。基膜首先浸于一定浓度的间苯二胺(MPD)的水相中,将基膜从水相中取出后,用超纯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,即一定浓度的均苯三酰氯(TMC)的正己烷溶液,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。为使聚酰胺复合层聚合的更加牢固,将复合膜在干燥箱内进行热处理,取出,保存在去离子水中备用;The polyamide layer was synthesized on the support layer by interfacial polymerization. The basement membrane is first immersed in a certain concentration of m-phenylenediamine (MPD) in the water phase. After the basement membrane is taken out of the water phase, the solution on the back of the support layer is washed away with ultrapure water, and then both sides of the membrane are blotted dry with filter paper. Then soak the membrane in the oil phase, that is, a certain concentration of trimesoyl chloride (TMC) in n-hexane, take it out, and remove the excess oil phase to obtain a graphene oxide/polyamide forward osmosis composite membrane. In order to make the polyamide composite layer polymerized more firmly, the composite film is heat-treated in a drying oven, taken out, and stored in deionized water for later use; 为考察膜的性能,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 order to investigate the performance of the 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. 2.根据权利要求1所述的一种氧化石墨烯改性的高性能正渗透复合膜及制备方法,其特征在于步骤(1)中,制备氧化石墨烯/聚砜支撑层的材料有:膜材料为聚砜,8.0%~25.0wt%;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%;添加剂为聚乙二醇600,0~20.0wt%;增溶剂为吐温80,0.5%~2wt%。2. a kind of graphene oxide modified high-performance forward osmosis composite membrane and preparation method according to claim 1, it is characterized in that in step (1), the material of preparing graphene oxide/polysulfone support layer has: membrane The material is polysulfone, 8.0%-25.0wt%; the modifier is graphene oxide, 0-1.5wt%; the solvent is N,N-dimethylformamide, 65.0%-80.0wt%; the additive is polyethylene glycol Alcohol 600, 0-20.0wt%; solubilizer Tween 80, 0.5%-2wt%. 3.根据权利要求1所述的改性方法,其特征在于步骤(1)中聚砜材料添加之前,需要先将氧化石墨烯在溶液中超声分散均匀,超声时间为10~60min,再移至磁力搅拌器上搅拌3~10min。3. The modification method according to claim 1, characterized in that before adding the polysulfone material in step (1), it is necessary to disperse graphene oxide uniformly in the solution by ultrasonic, the ultrasonic time is 10-60min, and then move to Stir on a magnetic stirrer for 3 to 10 minutes. 4.根据权利要求1所述的改性方法,其特征在于步骤(1)聚砜材料添加之后,搅拌条件为:在50~70℃温度下搅拌溶解6~10h。4. The modification method according to claim 1, characterized in that in step (1) after the polysulfone material is added, the stirring condition is: stirring and dissolving at a temperature of 50-70° C. for 6-10 hours. 5.根据权利要求1所述的改性方法,其特征在于步骤(1)铸膜过程中,聚酯筛网的目数为80~120,刮刀厚度为50~200μm。5. The modification method according to claim 1, characterized in that in step (1) during film casting, the mesh of the polyester screen is 80-120, and the thickness of the scraper is 50-200 μm. 6.根据权利要求1所述的一种氧化石墨烯改性的高性能正渗透复合膜及制备方法,其特征在于步骤(2)中聚酰胺活性层的合成是通过水相的间苯二胺和油相的均苯三酰氯两种溶液在膜表面发生界面聚合反应得到,两种溶液的浓度分别为2~4wt%、0.15~0.25wt%。6. a kind of graphene oxide modified high-performance forward osmosis composite membrane and preparation method according to claim 1, it is characterized in that the synthesis of polyamide active layer is through the m-phenylenediamine of water phase in the step (2) Two solutions of trimesoyl chloride and oil phase are obtained by interfacial polymerization reaction on the membrane surface, and the concentrations of the two solutions are respectively 2-4wt% and 0.15-0.25wt%. 7.根据权利要求1所述的改性方法,其特征在于步骤(2)中将基膜从水相中取出后,为防止浸渍后的支撑层两侧均存在间苯二胺而造成双面聚合的问题,需用超纯水冲掉支撑层背面的溶液,然后用滤纸吸干膜两侧的水渍,再将膜浸泡于油相中,完成进一步的聚合。7. modification method according to claim 1, it is characterized in that after base film is taken out from aqueous phase in step (2), all there is m-phenylenediamine in the support layer both sides after the impregnation and cause double-sided For the problem of polymerization, it is necessary to wash off the solution on the back of the support layer with ultrapure water, then use filter paper to blot the water stains on both sides of the membrane, and then soak the membrane in the oil phase to complete further polymerization. 8.根据权利要求1所述的改性方法,其特征在于步骤(2)中为使聚酰胺复合层聚合的更加牢固,将复合膜在干燥箱内40-80℃热处理5~10min。8. The modification method according to claim 1, characterized in that in step (2), in order to make the polyamide composite layer polymerized more firmly, the composite film is heat-treated in a drying oven at 40-80°C for 5-10min. 9.根据权利要求1所述的改性方法,其特征在于为测试膜的性能,将制备好的正渗透复合膜置于错流过滤系统中进行试验,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,结果得出:水通量可达9-12LMH,反向盐通量为2-4gMH,在抗污染测试中,污染引起的水通量下降幅度为未改性膜的30%-50%。9. The modification method according to claim 1, characterized in that for the performance of the test membrane, the prepared forward osmosis composite membrane is placed in a cross-flow filtration system for testing, and the forward osmosis composite membrane modified by graphene oxide is investigated. The water flux, reverse salt flux and anti-pollution performance of the membrane, the results show that the water flux can reach 9-12LMH, and the reverse salt flux is 2-4gMH. In the anti-pollution test, the water flux caused by pollution The decrease in amount was 30%-50% of the unmodified membrane.
CN201710506514.8A 2017-06-28 2017-06-28 The positive osmosis composite membrane of high-performance and preparation method that a kind of graphene oxide is modified Pending CN107174950A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710506514.8A CN107174950A (en) 2017-06-28 2017-06-28 The positive osmosis composite membrane of high-performance and preparation method that a kind of graphene oxide is modified

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710506514.8A CN107174950A (en) 2017-06-28 2017-06-28 The positive osmosis composite membrane of high-performance and preparation method that a kind of graphene oxide is modified

Publications (1)

Publication Number Publication Date
CN107174950A true CN107174950A (en) 2017-09-19

Family

ID=59845386

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710506514.8A Pending CN107174950A (en) 2017-06-28 2017-06-28 The positive osmosis composite membrane of high-performance and preparation method that a kind of graphene oxide is modified

Country Status (1)

Country Link
CN (1) CN107174950A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107789994A (en) * 2017-11-16 2018-03-13 清华大学 Positive permeability and separation film and preparation method thereof
CN109647223A (en) * 2018-11-14 2019-04-19 天津大学 A kind of preparation method of the compound forward osmosis membrane in high activity site
CN110508164A (en) * 2019-08-07 2019-11-29 大连理工大学 A kind of preparation method of graphene oxide composite film with stable structure
CN111318178A (en) * 2020-02-27 2020-06-23 江苏大学 A kind of graphene oxide/attapulgite composite film and its preparation method and application
CN114437339A (en) * 2020-11-03 2022-05-06 天津工业大学 Preparation method and application of high-absorbance honeycomb polyamide membrane
CN115888430A (en) * 2022-11-09 2023-04-04 江苏德环环保集团有限公司 Graphene oxide/aminated attapulgite intercalation compound surface modified forward osmosis membrane and preparation method thereof
CN117582831A (en) * 2023-12-29 2024-02-23 苏诺特(苏州)材料科技有限公司 Preparation method of forward osmosis membrane

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103861472A (en) * 2014-03-28 2014-06-18 东华大学 Preparation method of amino-modified graphene oxide composite positive permeable film
CN104528886A (en) * 2015-01-23 2015-04-22 中科安源(北京)科技有限公司 Outdoor portable emergency drinking water device and application method thereof
CN105664732A (en) * 2014-02-26 2016-06-15 宁波莲华环保科技股份有限公司 Method for preparing organic forward osmosis membrane
US20160303518A1 (en) * 2015-04-15 2016-10-20 Korea Research Institute Of Chemical Technology Nanocomposite ultrafiltration membrane containing graphene oxide or reduced graphene oxide and preparation method thereof
CN106215715A (en) * 2016-09-09 2016-12-14 中国海洋大学 A kind of high flux is combined the preparation method of forward osmosis membrane

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105664732A (en) * 2014-02-26 2016-06-15 宁波莲华环保科技股份有限公司 Method for preparing organic forward osmosis membrane
CN103861472A (en) * 2014-03-28 2014-06-18 东华大学 Preparation method of amino-modified graphene oxide composite positive permeable film
CN104528886A (en) * 2015-01-23 2015-04-22 中科安源(北京)科技有限公司 Outdoor portable emergency drinking water device and application method thereof
US20160303518A1 (en) * 2015-04-15 2016-10-20 Korea Research Institute Of Chemical Technology Nanocomposite ultrafiltration membrane containing graphene oxide or reduced graphene oxide and preparation method thereof
CN106215715A (en) * 2016-09-09 2016-12-14 中国海洋大学 A kind of high flux is combined the preparation method of forward osmosis membrane

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107789994A (en) * 2017-11-16 2018-03-13 清华大学 Positive permeability and separation film and preparation method thereof
CN109647223A (en) * 2018-11-14 2019-04-19 天津大学 A kind of preparation method of the compound forward osmosis membrane in high activity site
CN110508164A (en) * 2019-08-07 2019-11-29 大连理工大学 A kind of preparation method of graphene oxide composite film with stable structure
CN111318178A (en) * 2020-02-27 2020-06-23 江苏大学 A kind of graphene oxide/attapulgite composite film and its preparation method and application
CN111318178B (en) * 2020-02-27 2022-04-26 江苏大学 Graphene oxide/attapulgite composite membrane and preparation method and application thereof
CN114437339A (en) * 2020-11-03 2022-05-06 天津工业大学 Preparation method and application of high-absorbance honeycomb polyamide membrane
CN114437339B (en) * 2020-11-03 2023-07-21 天津工业大学 A kind of preparation method and application of honeycomb polyamide film with high light absorption rate
CN115888430A (en) * 2022-11-09 2023-04-04 江苏德环环保集团有限公司 Graphene oxide/aminated attapulgite intercalation compound surface modified forward osmosis membrane and preparation method thereof
CN115888430B (en) * 2022-11-09 2023-11-14 江苏德环环保集团有限公司 Graphene oxide/amination attapulgite intercalation compound surface modified forward osmosis membrane and preparation method thereof
CN117582831A (en) * 2023-12-29 2024-02-23 苏诺特(苏州)材料科技有限公司 Preparation method of forward osmosis membrane
CN117582831B (en) * 2023-12-29 2024-08-16 苏诺特(苏州)材料科技有限公司 Preparation method of forward osmosis membrane

Similar Documents

Publication Publication Date Title
CN107174950A (en) The positive osmosis composite membrane of high-performance and preparation method that a kind of graphene oxide is modified
CN104801208B (en) Sodium alginate-flaky ZIF-8 hybrid composite membrane, and preparation and application thereof
US20200122092A1 (en) Composite reverse osmosis membrane and preparation method thereof
CN105597552B (en) The method that the high salt-stopping rate forward osmosis membrane of high water flux and one-step method prepare the forward osmosis membrane
CN104906966A (en) Cellulose acetate/functionalized graphene mixed media hollow fiber positive osmotic membrane
CN108479396A (en) Based on nano zinc oxide modified positive osmosis composite membrane and preparation method
CN103212309B (en) Preparation method of supportless forward osmosis membrane
CN101513593B (en) Hydrophilic polyvinyl chloride membrane and preparation method thereof
CN104107638B (en) Forward osmosis membrane and preparation method thereof
CN103785301B (en) A kind of Cellulose acetate forward osmotic membrane material and preparation method thereof
CN101327408B (en) Method for preparing antimicrobial modified polyvinyl alcohol-nonwoven compound microporous filtering film
CN113797763B (en) Cellulose gel layer modified loose nanofiltration membrane for high-flux dye separation and preparation method and application thereof
CN104941466A (en) Preparation method of mesoporous carbon organic composite film for removing macromolecular hepatotoxins in water
JP2014521499A (en) Polyamide-based reverse osmosis separation membrane excellent in initial permeate flow rate and method for producing the same
CN102580561B (en) Tubular composite nanofiltration membrane
CN111420563A (en) Hybrid composite reverse osmosis/nanofiltration membrane, preparation method and application thereof
CN104906967A (en) Cellulose acetate/nano titanium dioxide mixed media hollow fiber positive osmotic membrane
CN114887486A (en) Mannitol-based polyester loose composite nanofiltration membrane and preparation method and application thereof
CN115350603A (en) Polyvinylidene fluoride-based thin-layer composite nanofiltration membrane and preparation method thereof
CN104107641B (en) Forward osmosis organic-inorganic composite membrane and preparation method thereof
CN105582816A (en) Preparation method of forward osmosis membrane modified with oxidized graphene
CN110743383A (en) A kind of modification method for improving the permeation flux of polyamide composite membrane
CN112619438B (en) Methanol-resistant polyamide reverse osmosis membrane and preparation method thereof
CN113578065A (en) Based on MXene-TiO2Method for preparing modified nanofiltration membrane
CN109012180A (en) A kind of preparation method with the clever structure composite forward osmosis membrane of figure

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20170919