CN110882632A - Reverse osmosis membrane and preparation method thereof - Google Patents

Reverse osmosis membrane and preparation method thereof Download PDF

Info

Publication number
CN110882632A
CN110882632A CN201811052153.5A CN201811052153A CN110882632A CN 110882632 A CN110882632 A CN 110882632A CN 201811052153 A CN201811052153 A CN 201811052153A CN 110882632 A CN110882632 A CN 110882632A
Authority
CN
China
Prior art keywords
reverse osmosis
graphene oxide
osmosis membrane
membrane
support layer
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.)
Granted
Application number
CN201811052153.5A
Other languages
Chinese (zh)
Other versions
CN110882632B (en
Inventor
刘岩
姜恒
魏彦存
孟垂舟
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.)
ENN Science and Technology Development Co Ltd
Original Assignee
ENN Science and Technology Development Co Ltd
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 ENN Science and Technology Development Co Ltd filed Critical ENN Science and Technology Development Co Ltd
Priority to CN201811052153.5A priority Critical patent/CN110882632B/en
Publication of CN110882632A publication Critical patent/CN110882632A/en
Application granted granted Critical
Publication of CN110882632B publication Critical patent/CN110882632B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • B01D71/021Carbon
    • 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
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025Reverse osmosis; Hyperfiltration
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Nanotechnology (AREA)
  • Inorganic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

本发明公开一种反渗透膜及其制备方法,涉及过滤膜技术领域,以解决水处理过程中反渗透膜的产水量低的问题。所述反渗透膜包括:支撑层,所述支撑层包括平板超滤膜;形成在所述支撑层上的功能层,所述功能层包括堆叠搭接的氧化石墨烯片。所述反渗透膜的制备方法包括:将氧化石墨烯的分散液复合到支撑层的表面,形成复合膜;对复合膜进行配位离子强化,得到所需的反渗透膜。本发明的反渗透膜可以有效提高水处理过程中的产水量。

Figure 201811052153

The invention discloses a reverse osmosis membrane and a preparation method thereof, and relates to the technical field of filtration membranes, so as to solve the problem of low water production of the reverse osmosis membrane in the water treatment process. The reverse osmosis membrane includes: a support layer, which includes a flat ultrafiltration membrane; a functional layer formed on the support layer, and the functional layer includes stacked and overlapped graphene oxide sheets. The preparation method of the reverse osmosis membrane comprises: compounding the graphene oxide dispersion on the surface of the support layer to form a compound membrane; and strengthening the compound membrane with coordination ions to obtain the required reverse osmosis membrane. The reverse osmosis membrane of the present invention can effectively increase the water production in the water treatment process.

Figure 201811052153

Description

一种反渗透膜及其制备方法A kind of reverse osmosis membrane and preparation method thereof

技术领域technical field

本发明涉及过滤膜技术领域,尤其涉及一种反渗透膜及其制备方法。The invention relates to the technical field of filtration membranes, in particular to a reverse osmosis membrane and a preparation method thereof.

背景技术Background technique

水资源短缺是当今全球面临的最大挑战之一,地球70%被海水覆盖,淡水资源也存在严重的水污染问题,因此海水淡化和污水处理日益引起人们的关注。反渗透技术是指在一定的压力作用下,借助于反渗透膜的选择渗透性作用将溶液中的溶质与溶剂分开的分离方法。反渗透膜技术因其具有耗能低、结构稳定、分离性能优良等优点,在海水脱盐及水处理领域受到广泛的关注及应用。Water shortage is one of the biggest challenges facing the world today. 70% of the earth is covered by seawater, and freshwater resources also have serious water pollution problems. Therefore, desalination and sewage treatment are increasingly attracting people's attention. Reverse osmosis technology refers to a separation method that separates the solute and solvent in a solution by means of the selective permeability of the reverse osmosis membrane under a certain pressure. Reverse osmosis membrane technology has received extensive attention and application in the field of seawater desalination and water treatment due to its advantages of low energy consumption, stable structure, and excellent separation performance.

目前反渗透膜的功能层材料主要有醋酸纤维素、线性聚酰胺和芳香聚酰胺,采用这三类材料制作的反渗透膜,在水处理时存在产水量(经反渗透膜过滤后的水的产量)低的问题。At present, the functional layer materials of reverse osmosis membranes mainly include cellulose acetate, linear polyamide and aromatic polyamide. The reverse osmosis membrane made of these three types of materials has a water yield (the amount of water filtered by the reverse osmosis membrane) during water treatment. output) is low.

发明内容SUMMARY OF THE INVENTION

针对上述现有技术中所存在的问题,本发明的实施例提供一种反渗透膜及其制备方法,以解决水处理过程中反渗透膜的产水量低的问题。In view of the above problems in the prior art, the embodiments of the present invention provide a reverse osmosis membrane and a preparation method thereof, so as to solve the problem of low water production of the reverse osmosis membrane in the water treatment process.

为了实现上述目的,本发明的实施例采用如下技术方案:In order to achieve the above object, the embodiments of the present invention adopt the following technical solutions:

第一方面,本发明的实施例提供一种反渗透膜,包括:支撑层,所述支撑层包括平板超滤膜;形成在所述支撑层上的功能层,所述功能层包括堆叠搭接的氧化石墨烯片。In a first aspect, an embodiment of the present invention provides a reverse osmosis membrane, comprising: a support layer, the support layer comprising a flat ultrafiltration membrane; a functional layer formed on the support layer, the functional layer comprising a stack overlap of graphene oxide sheets.

本发明实施例提供的反渗透膜中,氧化石墨烯具备良好的亲水性及离子识别功能,功能层采用堆叠搭接的氧化石墨烯,使氧化石墨烯片层之间可形成具有选择性的二维纳米通道,为水分子提供了高速传输通道,从而实现高效的水处理,增加水处理过程中的产水量。同时,堆叠搭接的氧化石墨烯片形成的二维纳米通道可以阻止溶质大分子通过,并且具有平板超滤膜的支撑层也可以分离水中小孔径的溶质分子,因此,在功能层与支撑层的共同作用下,大大提高了反渗透膜的分离性能。In the reverse osmosis membrane provided by the embodiment of the present invention, graphene oxide has good hydrophilicity and ion recognition functions, and the functional layer adopts stacked and overlapped graphene oxide, so that a selective layer of graphene oxide can be formed between the graphene oxide sheets. Two-dimensional nanochannels provide high-speed transport channels for water molecules, thereby achieving efficient water treatment and increasing water production during water treatment. At the same time, the two-dimensional nanochannels formed by stacking and overlapping graphene oxide sheets can prevent the passage of solute macromolecules, and the support layer with a flat ultrafiltration membrane can also separate solute molecules with small pore sizes in water. Under the joint action of , the separation performance of the reverse osmosis membrane is greatly improved.

优选的,所述氧化石墨烯片的片径为8~20μm,层数为2~10。Preferably, the sheet diameter of the graphene oxide sheet is 8-20 μm, and the number of layers is 2-10.

优选的,所述功能层的厚度为0.1~0.5μm。Preferably, the thickness of the functional layer is 0.1-0.5 μm.

优选的,所述平板超滤膜的表面孔径为0.1~1μm。Preferably, the surface pore size of the flat ultrafiltration membrane is 0.1-1 μm.

优选的,所述功能层与所述支撑层通过粘接剂粘接,所述粘接剂包括聚乙二醇、聚乙烯吡咯烷酮和聚乙烯醇中的任意一种或几种。Preferably, the functional layer and the support layer are bonded by an adhesive, and the adhesive includes any one or more of polyethylene glycol, polyvinylpyrrolidone and polyvinyl alcohol.

第二方面,本发明的实施例还提供了一种反渗透膜的制备方法,用于制备如第一方面所述的反渗透膜,所述制备方法包括:将氧化石墨烯的分散液复合到支撑层的表面,形成复合膜;对所述复合膜进行配位离子强化,得到所需的反渗透膜。所述支撑层包括平板超滤膜。In a second aspect, embodiments of the present invention also provide a method for preparing a reverse osmosis membrane, which is used to prepare the reverse osmosis membrane according to the first aspect, the preparation method comprising: compounding a graphene oxide dispersion into a A composite membrane is formed on the surface of the support layer; the composite membrane is strengthened by coordination ions to obtain the desired reverse osmosis membrane. The support layer includes a flat ultrafiltration membrane.

本发明实施例所提供的反渗透膜的制备方法,通过对复合膜进行配位离子强化,利用化学交联进一步加固了功能层,使制备出的反渗透膜具有更高的稳定性和牢固性。通过本发明实施例所提供的反渗透膜的制备方法制备出的反渗透膜所具有的有益效果,与第一方面所提供的反渗透膜所能达到的有益效果相同,在此不做赘述。In the preparation method of the reverse osmosis membrane provided by the embodiment of the present invention, the composite membrane is strengthened by coordination ions, and the functional layer is further strengthened by chemical cross-linking, so that the prepared reverse osmosis membrane has higher stability and firmness. . The beneficial effects of the reverse osmosis membrane prepared by the method for preparing the reverse osmosis membrane provided by the embodiment of the present invention are the same as those that can be achieved by the reverse osmosis membrane provided in the first aspect, and are not repeated here.

优选的,所述将氧化石墨烯的分散液复合到支撑层的表面,形成复合膜的步骤,包括:将所述氧化石墨烯的分散液喷涂到所述支撑层的表面;其中,喷涂压力为0.1~0.5MPa,喷涂时间为1~10s。Preferably, the step of compounding the graphene oxide dispersion on the surface of the support layer to form a composite film includes: spraying the graphene oxide dispersion on the surface of the support layer; wherein the spraying pressure is 0.1~0.5MPa, spraying time is 1~10s.

优选的,所述对所述复合膜进行配位离子强化,得到所需的反渗透膜的步骤,包括:将所述复合膜放入反应溶液中进行配位离子强化反应;所述反应溶液包括配位离子水溶液和与所述配位离子水溶液等体积的乙醇;用乙醇对所述复合膜进行冲淋,再将所述复合膜静置一定时间,得到所需的反渗透膜。Preferably, the step of performing coordination ion strengthening on the composite membrane to obtain the desired reverse osmosis membrane includes: placing the composite membrane in a reaction solution for a coordination ion strengthening reaction; the reaction solution includes A coordinating ion aqueous solution and an equal volume of ethanol with the coordinating ion aqueous solution; rinsing the composite membrane with ethanol, and then allowing the composite membrane to stand for a certain period of time to obtain the desired reverse osmosis membrane.

优选的,所述配位离子水溶液包括氯化钙溶液、氯化镁溶液和氯化铝溶液中的任意一种或几种,所述配位离子水溶液中的溶质的质量百分数为3~10%。Preferably, the complex ion aqueous solution includes any one or more of calcium chloride solution, magnesium chloride solution and aluminum chloride solution, and the mass percentage of the solute in the complex ion aqueous solution is 3-10%.

优选的,所述配位离子强化反应的时间为1~4小时。Preferably, the time for the coordination ion-enhanced reaction is 1 to 4 hours.

优选的,在所述将氧化石墨烯的分散液复合到支撑层的表面,形成复合膜的步骤之前,还包括制作所述氧化石墨烯的分散液的步骤,该步骤包括:将氧化石墨烯分散于分散剂中,并加入扩层稳定剂,形成分散液前体;向所述分散液前体中加入碱溶液,使所述分散液前体的PH值达到7~9,得到所需的氧化石墨烯的分散液。Preferably, before the step of compounding the graphene oxide dispersion on the surface of the support layer to form a composite film, it also includes the step of making the graphene oxide dispersion, and the step includes: dispersing the graphene oxide In the dispersant, and adding a layer-stretching stabilizer to form a dispersion liquid precursor; adding an alkaline solution to the dispersion liquid precursor, so that the PH value of the dispersion liquid precursor reaches 7 to 9 to obtain the desired oxidation Graphene dispersion.

优选的,所述氧化石墨烯的分散液中氧化石墨烯的质量浓度为Preferably, the mass concentration of graphene oxide in the dispersion of graphene oxide is

0.1~5mg/ml。0.1~5mg/ml.

优选的,所述分散剂包括超纯水、乙醇和N-甲基吡咯烷酮中的任意一种。Preferably, the dispersing agent includes any one of ultrapure water, ethanol and N-methylpyrrolidone.

优选的,所述扩层稳定剂包括脱氧胆酸钠、十二烷基苯磺酸钠和聚苯乙烯磺酸钠中的任意一种,所述氧化石墨烯的分散液中扩层稳定剂的质量百分数为0.1~5%。Preferably, the layer expansion stabilizer includes any one of sodium deoxycholate, sodium dodecylbenzenesulfonate and sodium polystyrene sulfonate, and the layer expansion stabilizer in the graphene oxide dispersion The mass percentage is 0.1 to 5%.

优选的,在所述将氧化石墨烯的分散液复合到支撑层的表面,形成复合膜的步骤之前,还包括对所述支撑层的平板超滤膜进行处理的步骤,该步骤包括:将所述平板超滤膜放入粘接剂的水溶液中,浸泡后晾干;其中,所述粘接剂的水溶液中,粘接剂的质量百分数为1~10%。Preferably, before the step of compounding the graphene oxide dispersion on the surface of the support layer to form a compound membrane, it also includes the step of processing the flat ultrafiltration membrane of the support layer, and the step includes: The flat ultrafiltration membrane is put into an aqueous solution of a binder, soaked and then air-dried; wherein, in the aqueous solution of the binder, the mass percentage of the binder is 1-10%.

优选的,在所述将氧化石墨烯的分散液复合到支撑层的表面,形成复合膜的步骤之后,以及,在所述对所述复合膜进行配位离子强化,得到所需的反渗透膜的步骤之前,还包括对所述复合膜进行热还原处理的步骤,该步骤包括:将所述复合膜在60~80℃条件下真空加热30~45min后,放至室温。Preferably, after the step of compounding the graphene oxide dispersion on the surface of the support layer to form a compound membrane, and after the coordination ion strengthening of the compound membrane, the desired reverse osmosis membrane is obtained It also includes the step of thermal reduction treatment on the composite film before the step of the method, and the step includes: heating the composite film in a vacuum at 60-80° C. for 30-45 min, and then placing it to room temperature.

附图说明Description of drawings

为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其它的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the following briefly introduces the accompanying drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only These are some embodiments of the present invention, and for those of ordinary skill in the art, other drawings can also be obtained from these drawings without creative effort.

图1为本发明实施例中反渗透膜的示意图;Fig. 1 is the schematic diagram of the reverse osmosis membrane in the embodiment of the present invention;

图2为本发明实施例中反渗透膜的功能层表面电镜图;Fig. 2 is the surface electron microscope image of the functional layer of the reverse osmosis membrane in the embodiment of the present invention;

图3为本发明实施例中反渗透膜的断面电镜图;Fig. 3 is the cross-sectional electron microscope view of the reverse osmosis membrane in the embodiment of the present invention;

图4为本发明实施例中反渗透膜的制备方法的流程图。FIG. 4 is a flow chart of a method for preparing a reverse osmosis membrane in an embodiment of the present invention.

附图标记:Reference number:

1-功能层,2-支撑层。1-functional layer, 2-support layer.

具体实施方式Detailed ways

正如背景技术所述,采用醋酸纤维素、线性聚酰胺和芳香聚酰胺等材料制作的反渗透膜,在水处理时存在产水量低的问题,并且,在制备过程中材料溶剂化效应差,不能采用溶液法制备,需要进行界面聚合,反应复杂,缺陷率高;由于反渗透过程操作压力高,材料极易压密,导致产水量低、膜堵塞等多重问题,因此有必要探索新型的功能层材料。As mentioned in the background art, reverse osmosis membranes made of materials such as cellulose acetate, linear polyamide and aromatic polyamide have the problem of low water production during water treatment, and the material solvation effect is poor during the preparation process, which cannot be Preparation by solution method requires interfacial polymerization, complex reaction and high defect rate; due to the high operating pressure in the reverse osmosis process, the material is easily compacted, resulting in multiple problems such as low water production and membrane blockage, so it is necessary to explore new functional layers. Material.

氧化石墨烯(Graphene Oxide,GO)是石墨烯的一种衍生物,通常由改进的Hummers法制得,其结构可以看作是石墨烯的表面和边缘镶嵌着大量的含氧官能团(如羟基、羧基、环氧基和羰基等),该结构和水通道蛋白的结构类似,具备良好的亲水性及离子识别功能,兼具高比表面积和高反应活性,因此氧化石墨烯是一种理想的分离膜材料。Graphene oxide (Graphene Oxide, GO) is a derivative of graphene, usually prepared by the modified Hummers method. , epoxy group and carbonyl group, etc.), the structure is similar to that of aquaporins, with good hydrophilicity and ion recognition functions, both high specific surface area and high reactivity, so graphene oxide is an ideal separation membrane material.

基于上述现状,本发明的实施例提出一种反渗透膜及其制备方法,以解决水处理过程中存在的产水量低的问题。请参阅图1和图3,该反渗透膜包括:支撑层2,支撑层2包括平板超滤膜;形成在支撑层2上的功能层1,功能层1包括堆叠搭接的氧化石墨烯片。图3反渗透膜的断面电镜图中,右上部分为支撑层2的断面,中部沿图片对角线从左上至右下倾斜的部分为功能层1的断面,左下部分为功能层1的表面。Based on the above situation, the embodiments of the present invention propose a reverse osmosis membrane and a preparation method thereof, so as to solve the problem of low water production in the water treatment process. Please refer to FIG. 1 and FIG. 3 , the reverse osmosis membrane includes: a support layer 2, which includes a flat ultrafiltration membrane; a functional layer 1 formed on the support layer 2, and the functional layer 1 includes stacked and overlapped graphene oxide sheets . In the cross-sectional electron microscope picture of the reverse osmosis membrane in Fig. 3, the upper right part is the section of the support layer 2, the part inclined from the upper left to the lower right in the middle part along the diagonal of the picture is the section of the functional layer 1, and the lower left part is the surface of the functional layer 1.

本发明实施例提供的反渗透膜中,氧化石墨烯具备良好的亲水性及离子识别功能,功能层1采用堆叠搭接的氧化石墨烯,形成层状薄膜,使氧化石墨烯片层之间可形成具有选择性的二维纳米通道,为水分子提供了高速传输通道,从而实现高效的水处理,增加水处理过程中的产水量。同时,堆叠搭接的氧化石墨烯形成的二维纳米通道可以阻止大分子通过,并且具有平板超滤膜的支撑层2也可以分离水中小孔径的溶质分子,因此,在功能层1与支撑层2的共同作用下,大大提高了反渗透膜的分离性能。另外,氧化石墨烯片层间由于存在较强的氢键,所以具有很好的力学性能及较高的机械强度,可以在较高的操作压力下连续运行,也具有良好的耐清洗能力。In the reverse osmosis membrane provided by the embodiment of the present invention, graphene oxide has good hydrophilicity and ion recognition functions, and the functional layer 1 adopts stacked and overlapped graphene oxide to form a layered film, so that the graphene oxide sheets are formed between the graphene oxide sheets. Selective two-dimensional nanochannels can be formed, providing high-speed transport channels for water molecules, thereby achieving efficient water treatment and increasing water production during water treatment. At the same time, the two-dimensional nanochannels formed by stacking and overlapping graphene oxide can prevent the passage of macromolecules, and the support layer 2 with the flat ultrafiltration membrane can also separate the solute molecules with small pore size in water. Under the joint action of 2, the separation performance of the reverse osmosis membrane is greatly improved. In addition, due to the strong hydrogen bonds between the graphene oxide sheets, it has good mechanical properties and high mechanical strength, can run continuously under high operating pressure, and also has good cleaning resistance.

功能层1的结构是由片状结构的氧化石墨烯堆叠搭接构成,因而堆叠的平整性及搭接的紧密性对功能层1的分离性能影响很大,决定平整性和紧密性的主要因素是氧化石墨烯的基本片状尺寸及处理方法。其中,氧化石墨烯片的片径大小,对堆叠后功能层1稳定性影响较大,片径过小,氧化石墨烯片搭接较差,极易脱落;片径过大,在制备过程中,分散液中氧化石墨烯易发生团聚、析出沉淀,因此,选用合适尺寸的氧化石墨烯片对与形成性能良好的反渗透膜非常重要。示例性的,氧化石墨烯片的片径可以为8~20μm,或者氧化石墨烯片的片径也可以选用8~10μm、8~15μm、10~15μm、12~17μm、15~20μm等,氧化石墨烯片的层数可以为2~10,也可以选用层数为2~5、5~10、2~8、8~10、4~7或6~9的氧化石墨烯片。The structure of the functional layer 1 is composed of graphene oxide in a sheet-like structure stacked and overlapped, so the flatness of the stack and the tightness of the overlap have a great influence on the separation performance of the functional layer 1, and the main factors that determine the flatness and tightness. It is the basic sheet size and processing method of graphene oxide. Among them, the size of the graphene oxide sheet has a great influence on the stability of the functional layer 1 after stacking. , the graphene oxide in the dispersion is prone to agglomeration and precipitation. Therefore, the selection of graphene oxide sheets of suitable size is very important for the formation of reverse osmosis membranes with good performance. Exemplarily, the sheet diameter of the graphene oxide sheet may be 8-20 μm, or the sheet diameter of the graphene oxide sheet may also be 8-10 μm, 8-15 μm, 10-15 μm, 12-17 μm, 15-20 μm, etc. The number of layers of the graphene sheet can be 2-10, and a graphene oxide sheet with the number of layers of 2-5, 5-10, 2-8, 8-10, 4-7 or 6-9 can also be selected.

由上述氧化石墨烯片堆叠搭接形成的功能层1的厚度可在0.1~0.5μm的范围,例如可以为0.1μm、0.2μm、0.3μm、0.4μm、0.5μm等。The thickness of the functional layer 1 formed by stacking and overlapping the graphene oxide sheets can be in the range of 0.1-0.5 μm, for example, 0.1 μm, 0.2 μm, 0.3 μm, 0.4 μm, 0.5 μm, and the like.

在一些实施例中,选用的平板超滤膜的表面孔径可为0.1~1μm。In some embodiments, the surface pore size of the selected flat ultrafiltration membrane may be 0.1-1 μm.

在一些实施例中,功能层1与支撑层2可通过粘接剂粘接,粘接剂可包括聚乙二醇、聚乙烯吡咯烷酮和聚乙烯醇中的任意一种或几种,也就是说,可以选用上述的其中一种粘接剂,也可以选用上述的两种或两种以上的混合物作为粘接剂。In some embodiments, the functional layer 1 and the support layer 2 may be bonded by an adhesive, and the adhesive may include any one or more of polyethylene glycol, polyvinylpyrrolidone and polyvinyl alcohol, that is, , one of the above-mentioned adhesives can be selected, or a mixture of two or more of the above-mentioned adhesives can be selected as the adhesives.

请参阅图4,本发明的实施例还提供了一种反渗透膜的制备方法,用于制备如上所述的反渗透膜,该制备方法包括:将氧化石墨烯的分散液复合到支撑层2的表面,形成复合膜,其中支撑层包括平板超滤膜;对复合膜进行配位离子强化,得到所需的反渗透膜。Referring to FIG. 4 , an embodiment of the present invention also provides a method for preparing a reverse osmosis membrane for preparing the above-mentioned reverse osmosis membrane, the preparation method comprising: compounding a graphene oxide dispersion to the support layer 2 The surface of the composite membrane is formed, wherein the support layer includes a flat ultrafiltration membrane; the composite membrane is strengthened by coordination ions to obtain the required reverse osmosis membrane.

氧化石墨烯堆叠成膜后,其在水相中膜结构稳定性较差,易发生层叠结构解体,重新分散于溶剂中,从而导致其分离性能的丧失。本发明实施例所提供的反渗透膜的制备方法,通过对复合膜进行配位离子强化,利用化学交联进一步加固了功能层1,使制备出的反渗透膜具有更高的稳定性和牢固性。通过本发明实施例所提供的反渗透膜的制备方法制备出的反渗透膜所具有的有益效果,与上述所提供的反渗透膜所能达到的有益效果相同,在此不做赘述。After graphene oxide is stacked to form a film, its membrane structure in the aqueous phase is less stable, and the laminated structure is prone to disintegration and re-dispersion in the solvent, resulting in the loss of its separation performance. In the preparation method of the reverse osmosis membrane provided by the embodiment of the present invention, the composite membrane is strengthened by coordination ions, and the functional layer 1 is further strengthened by chemical cross-linking, so that the prepared reverse osmosis membrane has higher stability and firmness. sex. The beneficial effects of the reverse osmosis membrane prepared by the method for preparing the reverse osmosis membrane provided in the embodiment of the present invention are the same as those that can be achieved by the reverse osmosis membrane provided above, and will not be repeated here.

请参阅图4,在一些实施例中,在将氧化石墨烯的分散液复合到支撑层2的表面,形成复合膜的步骤之前,还包括制作氧化石墨烯的分散液的步骤,该步骤包括:S11,将氧化石墨烯分散于分散剂中,并加入扩层稳定剂,形成分散液前体;S12,向分散液前体中加入碱溶液,例如氨水、强氧化钠溶液等,使分散液前体的PH值达到7~9,得到所需的氧化石墨烯的分散液。Please refer to FIG. 4, in some embodiments, before the step of compounding the dispersion of graphene oxide on the surface of the support layer 2 to form the compound film, it also includes the step of making the dispersion of graphene oxide, and the step includes: S11, dispersing graphene oxide in a dispersant, and adding a layer expansion stabilizer to form a dispersion liquid precursor; S12, adding an alkaline solution, such as ammonia water, strong sodium oxide solution, etc., to the dispersion liquid precursor to make the dispersion liquid The pH value of the body reaches 7 to 9, and the desired dispersion of graphene oxide is obtained.

在一些实施例中,制备的氧化石墨烯的分散液中氧化石墨烯的质量浓度为0.1~5mg/ml,例如可以为0.1mg/ml、5mg/ml、2.5mg/ml、1mg/ml、2mg/ml、3mg/ml、4mg/ml等。In some embodiments, the mass concentration of graphene oxide in the prepared graphene oxide dispersion is 0.1-5 mg/ml, for example, 0.1 mg/ml, 5 mg/ml, 2.5 mg/ml, 1 mg/ml, 2 mg /ml, 3mg/ml, 4mg/ml, etc.

氧化石墨烯可以分散于多种试剂,但是氧化石墨烯片在试剂中的分散状态将直接影响到功能层1的性能,因此需要选择合适的分散剂,以提高氧化石墨烯的分散效果。示例性的,可以选取水、乙醇、和N-甲基吡咯烷酮中的任意一种作为分散剂,以提高氧化石墨烯的分散效果。实际操作过程中,还可以通过对溶液进行搅拌、超声处理的方式,使氧化石墨烯的分散效果更好。Graphene oxide can be dispersed in a variety of reagents, but the dispersion state of graphene oxide sheets in the reagent will directly affect the performance of functional layer 1, so it is necessary to select a suitable dispersant to improve the dispersion effect of graphene oxide. Exemplarily, any one of water, ethanol, and N-methylpyrrolidone can be selected as the dispersant to improve the dispersion effect of graphene oxide. In the actual operation process, the dispersion effect of graphene oxide can also be improved by stirring and ultrasonically treating the solution.

由于氧化石墨烯易发生团聚,导致截留率降低,因此,在一些实施例中,可以在氧化石墨烯的分散液中加入少量的扩层稳定剂,以便于氧化石墨烯的平整搭接,从而增加水通量,同时也更利于分散液的稳定性,减小制备加工的难度。扩层稳定剂可以选用脱氧胆酸钠、十二烷基苯磺酸钠和聚苯乙烯磺酸钠中的任意一种,氧化石墨烯的分散液中扩层稳定剂的质量百分数可以为0.1~5%。Since graphene oxide is prone to agglomeration, resulting in a decrease in the retention rate, in some embodiments, a small amount of layer-expanding stabilizer may be added to the graphene oxide dispersion to facilitate the smooth lap joint of graphene oxide, thereby increasing the The water flux is also more conducive to the stability of the dispersion and reduces the difficulty of preparation and processing. The layer expansion stabilizer can be selected from any one of sodium deoxycholate, sodium dodecylbenzenesulfonate and sodium polystyrene sulfonate, and the mass percentage of the layer expansion stabilizer in the graphene oxide dispersion can be 0.1~ 5%.

请参阅图4,在一些实施例中,在将氧化石墨烯的分散液复合到支撑层2的表面,形成复合膜的步骤之前,还包括对支撑层2的平板超滤膜进行处理的步骤,该步骤包括:S2,将平板超滤膜放入粘接剂的水溶液中,浸泡后晾干。其中,粘接剂的水溶液中,粘接剂的质量百分数为1~10%,例如可以为1%、3%、5%、6%、8%或10%等。上述粘接剂可以选用聚乙二醇、聚乙烯吡咯烷酮和聚乙烯醇中的任意一种或几种。Referring to FIG. 4, in some embodiments, before the step of compounding the dispersion of graphene oxide on the surface of the support layer 2 to form the compound membrane, it also includes the step of processing the flat ultrafiltration membrane of the support layer 2, The step includes: S2, placing the flat ultrafiltration membrane in the aqueous solution of the adhesive, soaking it and then drying it. Wherein, in the aqueous solution of the adhesive, the mass percentage of the adhesive is 1-10%, for example, 1%, 3%, 5%, 6%, 8%, or 10%. The above-mentioned adhesive can be selected from any one or more of polyethylene glycol, polyvinylpyrrolidone and polyvinyl alcohol.

在一些实施例中,支撑层2的平板超滤膜可以为聚砜或者聚醚砜材料。由于氧化石墨烯的分散液和支撑层2的平板超滤膜(聚砜/聚醚砜膜)的表面张力有差异,如果直接将氧化石墨烯的分散液复合在支撑层2上,可能会出现分散液在支撑层2表面呈雾滴状无法成膜的情况,因此需要对支撑层2进行处理,利用聚乙二醇、聚乙烯吡咯烷酮和聚乙烯醇等两亲物质作为粘接剂对支撑层2进行表面改性,改善支撑层2的表面粗糙度,使支撑层2表面张力更接近氧化石墨烯分散液的表面张力,微观上粘接剂的亲油基团与支撑层2结合,亲水基团可以与后续复合到支撑层2表面的氧化石墨烯结合,使支撑层2与功能层1牢牢“粘”在一起。因此,对支撑层2进行预先处理,有利于氧化石墨烯在支撑层2表面的铺展,也有利于二者粘接牢固。In some embodiments, the flat ultrafiltration membrane of the support layer 2 may be a polysulfone or polyethersulfone material. Due to the difference in surface tension between the graphene oxide dispersion and the flat ultrafiltration membrane (polysulfone/polyethersulfone membrane) of the support layer 2, if the graphene oxide dispersion is directly compounded on the support layer 2, there may be When the dispersion liquid is in the form of mist droplets on the surface of the support layer 2 and cannot form a film, the support layer 2 needs to be treated, and amphiphilic substances such as polyethylene glycol, polyvinylpyrrolidone and polyvinyl alcohol are used as adhesives to the support layer. 2. Surface modification is performed to improve the surface roughness of the support layer 2, so that the surface tension of the support layer 2 is closer to the surface tension of the graphene oxide dispersion. The group can be combined with the graphene oxide that is subsequently compounded to the surface of the support layer 2, so that the support layer 2 and the functional layer 1 are firmly "stick" together. Therefore, pre-processing the support layer 2 is beneficial to the spreading of graphene oxide on the surface of the support layer 2, and is also conducive to the firm adhesion of the two.

请参阅图4,在一些实施例中,将氧化石墨烯的分散液复合到支撑层2的表面,形成复合膜的步骤,包括:S3,将氧化石墨烯的分散液喷涂到支撑层2的表面。实际操作时,可以采用喷涂法制备氧化石墨烯的复合膜,使用喷枪作为喷涂工具,依靠喷涂压力来实现氧化石墨烯片堆叠连续成膜,喷涂工具的压力及支撑层2的表面张力都对复合膜的结构有影响,示例性的,喷涂压力在0.1~0.5MPa,喷涂效果较好,所述喷涂压力也可以为0.1MPa、0.5MPa、MPa、0.25MPa、0.3MPa等。喷涂时间可以为1~10s,例如喷涂1s、10s、5s、2s、3s、6s、7s或者8s。喷涂时间越长、氧化石墨烯的分散液浓度越高,形成的功能层厚度越厚。Referring to FIG. 4, in some embodiments, the step of compounding the dispersion of graphene oxide on the surface of the support layer 2 to form a composite film includes: S3, spraying the dispersion of graphene oxide onto the surface of the support layer 2 . In actual operation, the composite film of graphene oxide can be prepared by spraying method, using a spray gun as a spraying tool, and relying on the spraying pressure to achieve continuous film formation of graphene oxide sheets stacked, the pressure of the spraying tool and the surface tension of the support layer 2 are both effective for the composite film. The structure of the film has an influence. Exemplarily, the spraying pressure is 0.1-0.5MPa, and the spraying effect is better. The spraying pressure can also be 0.1MPa, 0.5MPa, MPa, 0.25MPa, 0.3MPa, etc. The spraying time can be 1-10s, for example, spraying is 1s, 10s, 5s, 2s, 3s, 6s, 7s or 8s. The longer the spraying time and the higher the dispersion concentration of graphene oxide, the thicker the thickness of the formed functional layer.

请参阅图4,在一些实施例中,在将氧化石墨烯的分散液复合到支撑层2的表面,形成复合膜的步骤之后,以及,在对复合膜进行配位离子强化,得到所需的反渗透膜的步骤之前,还包括对复合膜进行热还原处理的步骤,该步骤包括:S4,将复合膜在60~80℃条件下真空加热30~45min后,放至室温。因为氧化石墨烯具有亲水基团,其所形成的功能层1在水环境中应用,容易发生氧化石墨烯漂浮分离,经过热还原步骤之后,可以增加氧化石墨烯的稳定性,起到加固功能层1的作用。Referring to FIG. 4 , in some embodiments, after the step of compounding the graphene oxide dispersion on the surface of the support layer 2 to form a compound film, and after performing coordination ion strengthening on the compound film, the desired Before the step of the reverse osmosis membrane, it also includes the step of thermal reduction treatment on the composite membrane, and the step includes: S4 , heating the composite membrane in a vacuum at 60-80° C. for 30-45 minutes, and then placing it to room temperature. Because graphene oxide has hydrophilic groups, the functional layer 1 formed by it is applied in an aqueous environment, and graphene oxide floats and separates easily. After the thermal reduction step, the stability of graphene oxide can be increased and the function of reinforcement can be achieved. The role of layer 1.

初步制备完成的氧化石墨烯复合膜虽然已经具备分离功能,但是由于氧化石墨烯含有大量的亲水基团,长时间的水环境运行,氧化石墨烯片易于随水流失引发功能层1结构崩塌,也容易由于粘接剂等两亲物质随水流失引发功能层1剥离,因此可对形成的复合膜进行进一步加固。请参阅图4,在一些实施例中,对复合膜进行配位离子强化,得到所需的反渗透膜的步骤,包括:S51,将复合膜放入反应溶液中进行配位离子强化反应;反应溶液包括配位离子水溶液和与配位离子水溶液等体积的乙醇;S52,用乙醇对复合膜进行冲淋,再将复合膜静置一定时间,得到所需的反渗透膜。Although the graphene oxide composite membrane prepared initially has a separation function, because graphene oxide contains a large number of hydrophilic groups and operates in a water environment for a long time, the graphene oxide sheet is easily lost with water and causes the structure of functional layer 1 to collapse. It is also easy to cause the functional layer 1 to peel off due to the loss of amphiphilic substances such as adhesives with water, so that the formed composite film can be further reinforced. Referring to FIG. 4 , in some embodiments, the steps of performing coordination ion strengthening on the composite membrane to obtain a desired reverse osmosis membrane include: S51 , placing the composite membrane in a reaction solution to perform a coordination ion strengthening reaction; reaction The solution includes an aqueous solution of complex ions and an equal volume of ethanol with the aqueous solution of complex ions; S52, the composite membrane is rinsed with ethanol, and then the composite membrane is allowed to stand for a certain period of time to obtain the desired reverse osmosis membrane.

在一些实施例中,配位离子水溶液可以包括氯化钙溶液、氯化镁溶液和氯化铝溶液中的任意一种或几种,也就是说,可以选用上述的其中一种配位离子水溶液,也可以选用含有上述的两种或两种以上溶液的混合液作为配位离子水溶液。配位离子水溶液中的溶质的质量百分数为3~10%,例如溶质的质量百分数可以为3%、10%、6%、7%或5%等。In some embodiments, the complex ion aqueous solution may include any one or more of calcium chloride solution, magnesium chloride solution and aluminum chloride solution, that is to say, one of the above-mentioned complex ion aqueous solutions may be selected, or A mixed solution containing two or more of the above solutions can be selected as the complex ion aqueous solution. The mass percentage of the solute in the complex ion aqueous solution is 3 to 10%, for example, the mass percentage of the solute may be 3%, 10%, 6%, 7%, or 5%.

实际操作时,配位离子强化反应可以在室温下进行,反应时间可以为1~4小时。达到反应时间后,可以将复合膜取出,用乙醇对复合膜进行冲淋,冲洗掉多余的反应离子,从而终止反应。In actual operation, the coordination ion-enhanced reaction can be carried out at room temperature, and the reaction time can be 1 to 4 hours. After the reaction time is reached, the composite membrane can be taken out, and the composite membrane can be rinsed with ethanol to rinse off excess reactive ions, thereby terminating the reaction.

氧化石墨烯是在片状基面上引入了大量的含氧基团,包括羟基和环氧基团,而在氧化石墨烯片层的边缘部位分布羧基、羰基。通过配位离子强化反应,可以利用二价金属离子(如钙、镁、铝离子)将两片氧化石墨烯片的边缘键合,达到化学交联强化的效果。同时,对于氧化石墨烯片状基面的羟基、支撑层2表面粘接剂等两亲物质的羟基,也可达到化学交联强化的效果,从而实现功能层1体积交联,增大了其牢固性。如图2所示,图中“折皱”处表明氧化石墨烯已经成功附着到了支撑层2表面,形成稳定牢固的功能层1。In graphene oxide, a large number of oxygen-containing groups, including hydroxyl and epoxy groups, are introduced on the sheet-like base, while carboxyl and carbonyl groups are distributed at the edge of the graphene oxide sheet. Through the coordination ion strengthening reaction, divalent metal ions (such as calcium, magnesium, aluminum ions) can be used to bond the edges of two graphene oxide sheets to achieve the effect of chemical cross-linking strengthening. At the same time, for the hydroxyl groups of the graphene oxide sheet-like base surface and the hydroxyl groups of the amphiphilic substances such as the adhesive on the surface of the support layer 2, the effect of chemical crosslinking can also be strengthened, thereby realizing the volume crosslinking of the functional layer 1 and increasing its firmness. As shown in Figure 2, the "wrinkle" in the figure indicates that the graphene oxide has been successfully attached to the surface of the support layer 2 to form a stable and firm functional layer 1.

下面给出几个应用本发明的方法制备反渗透膜的示例,以便于本领域技术人员更好地理解本发明的内容。Several examples of applying the method of the present invention to prepare a reverse osmosis membrane are given below, so that those skilled in the art can better understand the content of the present invention.

示例1Example 1

制备氧化石墨烯的分散液的过程中,将片径为8~10μm、层数为2~5的氧化石墨烯片分散于超纯水中,氧化石墨烯的质量浓度为1mg/ml,对溶液进行磁力搅拌5min,超声分散30min,并加入质量分数1%的脱氧胆酸钠水溶液1ml,混合均匀,形成分散液前体。将分散液前体静置1h,加入浓度25%的氨水调节分散液前体的PH值,使其PH值达到8.5,并将溶液稳定30min,得到所需的氧化石墨烯的分散液。In the process of preparing the dispersion liquid of graphene oxide, graphene oxide sheets with a sheet diameter of 8 to 10 μm and a number of layers of 2 to 5 are dispersed in ultrapure water, and the mass concentration of graphene oxide is 1 mg/ml. Magnetic stirring was performed for 5 minutes, ultrasonic dispersion was carried out for 30 minutes, and 1 ml of an aqueous solution of sodium deoxycholate with a mass fraction of 1% was added, and the mixture was uniformly mixed to form a dispersion liquid precursor. The dispersion liquid precursor was allowed to stand for 1 hour, and 25% ammonia water was added to adjust the pH value of the dispersion liquid precursor to make the pH value reach 8.5, and the solution was stabilized for 30 minutes to obtain the required graphene oxide dispersion liquid.

对支撑层2进行处理的过程中,选用孔径0.1μm的聚砜平板超滤膜作为支撑层2,将平板超滤膜在质量浓度为5%的聚乙烯醇水溶液中浸泡两个小时后,取出放置24h晾干。In the process of processing the support layer 2, a polysulfone flat ultrafiltration membrane with a pore size of 0.1 μm was selected as the support layer 2, and the flat ultrafiltration membrane was soaked in a polyvinyl alcohol aqueous solution with a mass concentration of 5% for two hours, and then taken out. Leave to dry for 24h.

利用喷枪将氧化石墨烯的分散液喷涂到支撑层2的表面,形成复合膜,其中,喷涂压力为0.2MPa,喷涂时间为5s。The graphene oxide dispersion is sprayed onto the surface of the support layer 2 by a spray gun to form a composite film, wherein the spraying pressure is 0.2 MPa and the spraying time is 5s.

对复合膜进行热还原后处理的过程中,将完成喷涂的复合膜放入真空烘箱80℃下热处理30min,然后放至室温。In the process of thermal reduction post-treatment of the composite film, the composite film after spraying was put into a vacuum oven for heat treatment at 80° C. for 30 min, and then brought to room temperature.

对复合膜进行配位离子强化的过程中,配置质量浓度为5%的氯化钙水溶液,并向该氯化钙水溶液中加入与之等体积的乙醇,将热还原后处理后的复合膜浸入乙醇与氯化钙溶液的混合液中,反应1h后,将复合膜取出,并用乙醇反复淋洗,淋洗后将复合膜放置24h,得到所需制备的反渗透膜,其中,反渗透膜功能层1的厚度为0.2μm。In the process of coordinating ion strengthening of the composite membrane, a calcium chloride aqueous solution with a mass concentration of 5% is prepared, and an equal volume of ethanol is added to the calcium chloride aqueous solution, and the composite membrane after thermal reduction is immersed in the solution. In the mixed solution of ethanol and calcium chloride solution, after reacting for 1 hour, the composite membrane was taken out and rinsed repeatedly with ethanol. After rinsing, the composite membrane was placed for 24 hours to obtain the required reverse osmosis membrane. Among them, the reverse osmosis membrane function The thickness of layer 1 is 0.2 μm.

示例2Example 2

制备氧化石墨烯的分散液的过程中,将片径为15~20μm、层数为5~8的氧化石墨烯片分散于N-甲基吡咯烷酮中,氧化石墨烯的质量浓度为1mg/ml,对溶液进行磁力搅拌5min,超声分散30min,并加入质量分数1%的脱氧胆酸钠水溶液2ml,混合均匀,形成分散液前体。将分散液前体静置1h,加入浓度25%的氨水调节分散液前体的PH值,使其PH值达到8.5,并将溶液稳定30min,得到所需的氧化石墨烯的分散液。In the process of preparing the dispersion liquid of graphene oxide, graphene oxide sheets with a sheet diameter of 15 to 20 μm and a number of layers of 5 to 8 are dispersed in N-methylpyrrolidone, and the mass concentration of graphene oxide is 1 mg/ml, The solution was magnetically stirred for 5 minutes, ultrasonically dispersed for 30 minutes, and 2 ml of an aqueous solution of sodium deoxycholate with a mass fraction of 1% was added, and the mixture was uniformly mixed to form a dispersion liquid precursor. The dispersion liquid precursor was allowed to stand for 1 hour, and 25% ammonia water was added to adjust the pH value of the dispersion liquid precursor to make the pH value reach 8.5, and the solution was stabilized for 30 minutes to obtain the required graphene oxide dispersion liquid.

对支撑层2进行处理的过程中,选用孔径0.1μm的聚砜平板超滤膜作为支撑层2,将平板超滤膜在质量浓度为5%的聚乙烯醇水溶液中浸泡两个小时后,取出放置24h晾干。In the process of processing the support layer 2, a polysulfone flat ultrafiltration membrane with a pore size of 0.1 μm was selected as the support layer 2, and the flat ultrafiltration membrane was soaked in a polyvinyl alcohol aqueous solution with a mass concentration of 5% for two hours, and then taken out. Leave to dry for 24h.

利用喷枪将氧化石墨烯的分散液喷涂到支撑层2的表面,形成复合膜,其中,喷涂压力为0.4MPa,喷涂时间为8s。The graphene oxide dispersion was sprayed onto the surface of the support layer 2 by a spray gun to form a composite film, wherein the spraying pressure was 0.4 MPa and the spraying time was 8s.

对复合膜进行热还原后处理的过程中,将完成喷涂的复合膜放入真空烘箱80℃下热处理45min,然后放至室温。In the process of thermal reduction post-treatment of the composite film, the composite film after spraying was put into a vacuum oven for heat treatment at 80° C. for 45 min, and then placed at room temperature.

对复合膜进行配位离子强化的过程中,配置质量浓度为5%的氯化钙水溶液,并向该氯化钙水溶液中加入与之等体积的乙醇,将热还原后处理后的复合膜浸入乙醇与氯化钙溶液的混合液中,反应1h后,将复合膜取出,并用乙醇反复淋洗,淋洗后将复合膜放置24h,得到所需制备的反渗透膜,其中,反渗透膜功能层1的厚度为0.25μm。In the process of coordinating ion strengthening of the composite membrane, a calcium chloride aqueous solution with a mass concentration of 5% is prepared, and an equal volume of ethanol is added to the calcium chloride aqueous solution, and the composite membrane after thermal reduction is immersed in the solution. In the mixed solution of ethanol and calcium chloride solution, after reacting for 1 hour, the composite membrane was taken out and rinsed repeatedly with ethanol. After rinsing, the composite membrane was placed for 24 hours to obtain the required reverse osmosis membrane. Among them, the reverse osmosis membrane function The thickness of layer 1 is 0.25 μm.

示例3Example 3

制备氧化石墨烯的分散液的过程中,将片径为15~20μm、层数为8~10的氧化石墨烯片分散于乙醇中,氧化石墨烯的质量浓度为5mg/ml,对溶液进行磁力搅拌5min,超声分散20min,并加入质量分数3%的脱氧胆酸钠水溶液2ml,混合均匀,形成分散液前体。将分散液前体静置1h,加入浓度25%的氨水调节分散液前体的PH值,使其PH值达到8.5,并将溶液稳定30min,得到所需的氧化石墨烯的分散液。In the process of preparing the dispersion liquid of graphene oxide, graphene oxide sheets with a sheet diameter of 15 to 20 μm and a number of layers of 8 to 10 are dispersed in ethanol, and the mass concentration of graphene oxide is 5 mg/ml, and the solution is subjected to a magnetic force. Stir for 5 minutes, ultrasonically disperse for 20 minutes, add 2 ml of a 3% sodium deoxycholate aqueous solution by mass, and mix uniformly to form a dispersion liquid precursor. The dispersion liquid precursor was allowed to stand for 1 hour, and 25% ammonia water was added to adjust the pH value of the dispersion liquid precursor to make the pH value reach 8.5, and the solution was stabilized for 30 minutes to obtain the required graphene oxide dispersion liquid.

对支撑层2进行处理的过程中,选用孔径0.1μm的聚醚砜平板超滤膜作为支撑层2,将平板超滤膜在质量浓度为5%的聚乙烯醇水溶液中浸泡两个小时后,取出放置24h晾干。In the process of processing the support layer 2, a polyethersulfone flat ultrafiltration membrane with a pore size of 0.1 μm was selected as the support layer 2, and the flat ultrafiltration membrane was soaked in a polyvinyl alcohol aqueous solution with a mass concentration of 5% for two hours. Take it out and let it dry for 24 hours.

利用喷枪将氧化石墨烯的分散液喷涂到支撑层2的表面,形成复合膜,其中,喷涂压力为0.2MPa,喷涂时间为3s。The graphene oxide dispersion was sprayed onto the surface of the support layer 2 by a spray gun to form a composite film, wherein the spraying pressure was 0.2 MPa and the spraying time was 3s.

对复合膜进行热还原后处理的过程中,将完成喷涂的复合膜放入真空烘箱80℃下热处理45min,然后放至室温。In the process of thermal reduction post-treatment of the composite film, the composite film after spraying was put into a vacuum oven for heat treatment at 80° C. for 45 min, and then placed at room temperature.

对复合膜进行配位离子强化的过程中,配置质量浓度为10%的氯化镁水溶液,并向该氯化钙水溶液中加入与之等体积的乙醇,将热还原后处理后的复合膜浸入乙醇与氯化钙溶液的混合液中,反应1h后,将复合膜取出,并用乙醇反复淋洗,淋洗后将复合膜放置24h,得到所需制备的反渗透膜,其中,反渗透膜功能层1的厚度为0.5μm。During the coordination ion strengthening process of the composite membrane, a magnesium chloride aqueous solution with a mass concentration of 10% was prepared, and an equal volume of ethanol was added to the calcium chloride aqueous solution, and the composite membrane after thermal reduction was immersed in ethanol and ethanol. In the mixed solution of calcium chloride solution, after reacting for 1 hour, the composite membrane was taken out and rinsed repeatedly with ethanol. After rinsing, the composite membrane was placed for 24 hours to obtain the required reverse osmosis membrane. Among them, the reverse osmosis membrane functional layer 1 The thickness is 0.5 μm.

示例4Example 4

制备氧化石墨烯的分散液的过程中,将片径为8~10μm、层数为4~6的氧化石墨烯片分散于超纯水中,氧化石墨烯的质量浓度为3mg/ml,对溶液进行磁力搅拌5min,超声分散30min,并加入质量分数1%的脱氧胆酸钠水溶液1ml,混合均匀,形成分散液前体。将分散液前体静置1h,加入浓度25%的氨水调节分散液前体的PH值,使其PH值达到7,并将溶液稳定30min,得到所需的氧化石墨烯的分散液。In the process of preparing the dispersion liquid of graphene oxide, graphene oxide sheets with a sheet diameter of 8 to 10 μm and a number of layers of 4 to 6 are dispersed in ultrapure water, and the mass concentration of graphene oxide is 3 mg/ml. Magnetic stirring was performed for 5 minutes, ultrasonic dispersion was carried out for 30 minutes, and 1 ml of an aqueous solution of sodium deoxycholate with a mass fraction of 1% was added, and the mixture was uniformly mixed to form a dispersion liquid precursor. The dispersion liquid precursor was allowed to stand for 1 hour, 25% ammonia water was added to adjust the pH value of the dispersion liquid precursor to make the pH value reach 7, and the solution was stabilized for 30 minutes to obtain the required graphene oxide dispersion liquid.

对支撑层2进行处理的过程中,选用孔径0.1μm的聚砜平板超滤膜作为支撑层2,将平板超滤膜在质量浓度为5%的聚乙二醇水溶液中浸泡两个小时后,取出放置24h晾干。In the process of processing the support layer 2, a polysulfone flat ultrafiltration membrane with a pore size of 0.1 μm was selected as the support layer 2, and the flat ultrafiltration membrane was soaked in a polyethylene glycol aqueous solution with a mass concentration of 5% for two hours. Take it out and let it dry for 24 hours.

利用喷枪将氧化石墨烯的分散液喷涂到支撑层2的表面,形成复合膜,其中,喷涂压力为0.2MPa,喷涂时间为2s。The graphene oxide dispersion is sprayed onto the surface of the support layer 2 by a spray gun to form a composite film, wherein the spraying pressure is 0.2 MPa, and the spraying time is 2s.

对复合膜进行热还原后处理的过程中,将完成喷涂的复合膜放入真空烘箱80℃下热处理30min,然后放至室温。In the process of thermal reduction post-treatment of the composite film, the composite film after spraying was put into a vacuum oven for heat treatment at 80° C. for 30 min, and then brought to room temperature.

对复合膜进行配位离子强化的过程中,配置质量浓度为5%的氯化钙水溶液,并向该氯化钙水溶液中加入与之等体积的乙醇,将热还原后处理后的复合膜浸入乙醇与氯化钙溶液的混合液中,反应1h后,将复合膜取出,并用乙醇反复淋洗,淋洗后将复合膜放置24h,得到所需制备的反渗透膜,其中,反渗透膜功能层1的厚度为0.3μm。In the process of coordinating ion strengthening of the composite membrane, a calcium chloride aqueous solution with a mass concentration of 5% is prepared, and an equal volume of ethanol is added to the calcium chloride aqueous solution, and the composite membrane after thermal reduction is immersed in the solution. In the mixed solution of ethanol and calcium chloride solution, after reacting for 1 hour, the composite membrane was taken out and rinsed repeatedly with ethanol. After rinsing, the composite membrane was placed for 24 hours to obtain the required reverse osmosis membrane. Among them, the reverse osmosis membrane function The thickness of layer 1 is 0.3 μm.

示例5Example 5

制备氧化石墨烯的分散液的过程中,将片径为8~10μm、层数为5~10的氧化石墨烯片分散于超纯水中,氧化石墨烯的质量浓度为3mg/ml,对溶液进行磁力搅拌5min,超声分散30min,并加入质量分数1%的十二烷基苯磺酸钠水溶液2ml,混合均匀,形成分散液前体。将分散液前体静置1h,加入浓度25%的氨水调节分散液前体的PH值,使其PH值达到9,并将溶液稳定30min,得到所需的氧化石墨烯的分散液。In the process of preparing the dispersion liquid of graphene oxide, graphene oxide sheets with a sheet diameter of 8 to 10 μm and a number of layers of 5 to 10 are dispersed in ultrapure water, and the mass concentration of graphene oxide is 3 mg/ml. Magnetic stirring was performed for 5 minutes, ultrasonic dispersion was performed for 30 minutes, and 2 ml of an aqueous solution of sodium dodecylbenzenesulfonate with a mass fraction of 1% was added, and the mixture was uniformly mixed to form a dispersion liquid precursor. The dispersion liquid precursor was allowed to stand for 1 hour, and the pH value of the dispersion liquid precursor was adjusted by adding ammonia water with a concentration of 25% to make the pH value reach 9, and the solution was stabilized for 30 minutes to obtain the required graphene oxide dispersion liquid.

对支撑层2进行处理的过程中,选用孔径0.1μm的聚砜平板超滤膜作为支撑层2,将平板超滤膜在质量浓度为5%的聚乙烯醇水溶液中浸泡两个小时后,取出放置24h晾干。In the process of processing the support layer 2, a polysulfone flat ultrafiltration membrane with a pore size of 0.1 μm was selected as the support layer 2, and the flat ultrafiltration membrane was soaked in a polyvinyl alcohol aqueous solution with a mass concentration of 5% for two hours, and then taken out. Leave to dry for 24h.

利用喷枪将氧化石墨烯的分散液喷涂到支撑层2的表面,形成复合膜,其中,喷涂压力为0.3MPa,喷涂时间为9s。The graphene oxide dispersion was sprayed onto the surface of the support layer 2 by a spray gun to form a composite film, wherein the spraying pressure was 0.3 MPa and the spraying time was 9s.

对复合膜进行热还原后处理的过程中,将完成喷涂的复合膜放入真空烘箱80℃下热处理30min,然后放至室温。In the process of thermal reduction post-treatment of the composite film, the composite film after spraying was put into a vacuum oven for heat treatment at 80° C. for 30 min, and then brought to room temperature.

对复合膜进行配位离子强化的过程中,配置质量浓度为5%的氯化钙水溶液,并向该氯化钙水溶液中加入与之等体积的乙醇,将热还原后处理后的复合膜浸入乙醇与氯化钙溶液的混合液中,反应1h后,将复合膜取出,并用乙醇反复淋洗,淋洗后将复合膜放置24h,得到所需制备的反渗透膜,其中,反渗透膜功能层1的厚度为0.5μm。In the process of coordinating ion strengthening of the composite membrane, a calcium chloride aqueous solution with a mass concentration of 5% is prepared, and an equal volume of ethanol is added to the calcium chloride aqueous solution, and the composite membrane after thermal reduction is immersed in the solution. In the mixed solution of ethanol and calcium chloride solution, after reacting for 1 hour, the composite membrane was taken out and rinsed repeatedly with ethanol. After rinsing, the composite membrane was placed for 24 hours to obtain the required reverse osmosis membrane. Among them, the reverse osmosis membrane function The thickness of layer 1 is 0.5 μm.

示例6Example 6

制备氧化石墨烯的分散液的过程中,将片径为10~15μm、层数为2~10的氧化石墨烯片分散于超纯水中,氧化石墨烯的质量浓度为0.1mg/ml,对溶液进行磁力搅拌5min,超声分散30min,并加入质量分数0.1%的聚苯乙烯磺酸钠水溶液3ml,混合均匀,形成分散液前体。将分散液前体静置1h,加入浓度25%的氨水调节分散液前体的PH值,使其PH值达到8,并将溶液稳定30min,得到所需的氧化石墨烯的分散液。In the process of preparing the dispersion liquid of graphene oxide, graphene oxide sheets with a sheet diameter of 10 to 15 μm and a number of layers of 2 to 10 are dispersed in ultrapure water, and the mass concentration of graphene oxide is 0.1 mg/ml. The solution was magnetically stirred for 5 minutes, ultrasonically dispersed for 30 minutes, and 3 ml of an aqueous solution of sodium polystyrene sulfonate with a mass fraction of 0.1% was added, and the mixture was uniformly mixed to form a dispersion liquid precursor. The dispersion liquid precursor was allowed to stand for 1 hour, and the pH value of the dispersion liquid precursor was adjusted by adding ammonia water with a concentration of 25%, so that the pH value reached 8, and the solution was stabilized for 30 minutes to obtain the required graphene oxide dispersion liquid.

对支撑层2进行处理的过程中,选用孔径0.5μm的聚醚砜平板超滤膜作为支撑层2,将平板超滤膜在质量浓度为1%的聚乙烯吡咯烷酮水溶液中浸泡两个小时后,取出放置24h晾干。In the process of processing the support layer 2, a polyethersulfone flat ultrafiltration membrane with a pore size of 0.5 μm was selected as the support layer 2, and the flat ultrafiltration membrane was immersed in a polyvinylpyrrolidone aqueous solution with a mass concentration of 1% for two hours. Take it out and let it dry for 24h.

利用喷枪将氧化石墨烯的分散液喷涂到支撑层2的表面,形成复合膜,其中,喷涂压力为0.1MPa,喷涂时间为10s。The graphene oxide dispersion was sprayed onto the surface of the support layer 2 by a spray gun to form a composite film, wherein the spraying pressure was 0.1 MPa and the spraying time was 10s.

对复合膜进行热还原后处理的过程中,将完成喷涂的复合膜放入真空烘箱60℃下热处理40min,然后放至室温。In the process of thermal reduction post-treatment of the composite film, the composite film after spraying was put into a vacuum oven for heat treatment at 60° C. for 40 min, and then brought to room temperature.

对复合膜进行配位离子强化的过程中,配置质量浓度为3%的氯化铝水溶液,并向该氯化钙水溶液中加入与之等体积的乙醇,将热还原后处理后的复合膜浸入乙醇与氯化钙溶液的混合液中,反应4h后,将复合膜取出,并用乙醇反复淋洗,淋洗后将复合膜放置24h,得到所需制备的反渗透膜,其中,反渗透膜功能层1的厚度为0.2μm。In the process of coordinating ion strengthening of the composite membrane, an aqueous solution of aluminum chloride with a mass concentration of 3% is prepared, and an equal volume of ethanol is added to the aqueous calcium chloride solution, and the composite membrane after thermal reduction is immersed in the solution. In the mixed solution of ethanol and calcium chloride solution, after reacting for 4 hours, the composite membrane was taken out and rinsed repeatedly with ethanol. After rinsing, the composite membrane was placed for 24 hours to obtain the required reverse osmosis membrane. Among them, the reverse osmosis membrane function The thickness of layer 1 is 0.2 μm.

示例7Example 7

制备氧化石墨烯的分散液的过程中,将片径为10~15μm、层数为3~7的氧化石墨烯片分散于乙醇中,氧化石墨烯的质量浓度为2.5mg/ml,对溶液进行磁力搅拌5min,超声分散30min,并加入质量分数5%的脱氧胆酸钠水溶液1ml,混合均匀,形成分散液前体。将分散液前体静置1h,加入浓度25%的氨水调节分散液前体的PH值,使其PH值达到8,并将溶液稳定30min,得到所需的氧化石墨烯的分散液。In the process of preparing the dispersion liquid of graphene oxide, graphene oxide sheets with a sheet diameter of 10 to 15 μm and a number of layers of 3 to 7 are dispersed in ethanol, and the mass concentration of graphene oxide is 2.5 mg/ml. Magnetic stirring for 5 minutes, ultrasonic dispersion for 30 minutes, and adding 1 ml of an aqueous solution of sodium deoxycholate with a mass fraction of 5%, and mixing uniformly to form a dispersion liquid precursor. The dispersion liquid precursor was allowed to stand for 1 hour, and the pH value of the dispersion liquid precursor was adjusted by adding ammonia water with a concentration of 25%, so that the pH value reached 8, and the solution was stabilized for 30 minutes to obtain the required graphene oxide dispersion liquid.

对支撑层2进行处理的过程中,选用孔径1μm的聚醚砜平板超滤膜作为支撑层2,将平板超滤膜在质量浓度为10%的聚乙烯吡咯烷酮水溶液中浸泡两个小时后,取出放置24h晾干。In the process of treating the support layer 2, a polyethersulfone flat ultrafiltration membrane with a pore size of 1 μm was selected as the support layer 2, and the flat ultrafiltration membrane was soaked in an aqueous solution of polyvinylpyrrolidone with a mass concentration of 10% for two hours, and then taken out. Leave to dry for 24h.

利用喷枪将氧化石墨烯的分散液喷涂到支撑层2的表面,形成复合膜,其中,喷涂压力为0.5MPa,喷涂时间为1s。The graphene oxide dispersion is sprayed onto the surface of the support layer 2 by a spray gun to form a composite film, wherein the spray pressure is 0.5 MPa, and the spray time is 1 s.

对复合膜进行热还原后处理的过程中,将完成喷涂的复合膜放入真空烘箱70℃下热处理35min,然后放至室温。In the process of thermal reduction post-treatment of the composite film, the composite film after spraying was put into a vacuum oven for heat treatment at 70° C. for 35 min, and then placed at room temperature.

对复合膜进行配位离子强化的过程中,配置质量浓度为7%的氯化铝水溶液,并向该氯化钙水溶液中加入与之等体积的乙醇,将热还原后处理后的复合膜浸入乙醇与氯化钙溶液的混合液中,反应2.5h后,将复合膜取出,并用乙醇反复淋洗,淋洗后将复合膜放置24h,得到所需制备的反渗透膜,其中,反渗透膜功能层1的厚度为0.2μm。In the process of coordinating ion strengthening of the composite membrane, an aqueous solution of aluminum chloride with a mass concentration of 7% is prepared, and an equal volume of ethanol is added to the aqueous calcium chloride solution, and the composite membrane after thermal reduction is immersed in the solution. In the mixed solution of ethanol and calcium chloride solution, after reacting for 2.5 hours, the composite membrane was taken out and rinsed repeatedly with ethanol. After rinsing, the composite membrane was placed for 24 hours to obtain the required reverse osmosis membrane. Among them, the reverse osmosis membrane The thickness of the functional layer 1 was 0.2 μm.

对上述示例中制备得到的反渗透膜进行性能测试,测试设备为通用死端杯状反渗透膜评价设备,测试操作条件为25℃,测试压力为2MPa,测试液为1000ppm(parts permillion,百万分比浓度)的NaCl水溶液,取样在反渗透膜稳定运行30min后进行。具体测试过程参阅现有技术,此处不做赘述。测试结果如表1所示。The performance test of the reverse osmosis membrane prepared in the above example is carried out. The test equipment is a universal dead-end cup reverse osmosis membrane evaluation equipment. Sampling was carried out after the reverse osmosis membrane ran stably for 30 min. For the specific testing process, refer to the prior art, which will not be repeated here. The test results are shown in Table 1.

表1Table 1

示例编号example number 脱盐率(%)Desalination rate (%) 水通量(L/M<sup>2</sup>/H)Water flux (L/M<sup>2</sup>/H) 11 9595 165165 22 9797 157157 33 9999 104104 44 97.897.8 125125 55 97.597.5 115115 66 9595 170170 77 9797 145145

目前市售商用反渗透膜的死端测试性能约为脱盐率95~97%,水通量为35~50L/M2/H,对比本发明实施例中的测试结果数据,采用本发明的方法制备的反渗透膜的提高水通量的优势非常明显。At present, the dead-end test performance of commercially available reverse osmosis membranes is about 95-97% of the salt rejection, and the water flux is 35-50 L/M 2 /H. Compared with the test results data in the examples of the present invention, the method of the present invention is adopted. The advantage of the prepared reverse osmosis membrane to improve water flux is very obvious.

对于上述示例,还进行了变压测试实验,实验条件与反渗透膜性能测试的条件相似,所不同的是,测试压力为变化压力,即分别对不同压力下反渗透膜的性能进行测试,测试结果表明,本发明实施例的反渗透膜具有良好的耐压性能。由于各示例的测试结果趋势相同,下面仅列出示例3所制备的反渗透膜的测试结果作为参考,具体见表2。For the above example, a variable pressure test experiment was also carried out, and the experimental conditions were similar to those of the reverse osmosis membrane performance test. The results show that the reverse osmosis membrane of the embodiment of the present invention has good pressure resistance performance. Since the test results of each example have the same trend, only the test results of the reverse osmosis membrane prepared in Example 3 are listed below as a reference, see Table 2 for details.

表2Table 2

测试压力(MPa)Test pressure (MPa) 脱盐率(%)Desalination rate (%) 水通量(L/M<sup>2</sup>/H)Water flux (L/M<sup>2</sup>/H) 1.51.5 9797 9797 22 9999 104104 33 9999 120120 55 9999 119119

从表2中可以看出,随着测试压力的逐步提高,本发明实施例的反渗透膜的脱盐率和水通量皆上升,并且,反渗透膜没有发生高压引起功能层压密现象,也没有产水量减小、功能层失效或者脱盐率急剧下滑的现象,说明本发明实施例的反渗透膜可以耐受高操作压力,具有良好的耐压性能。As can be seen from Table 2, with the gradual increase of the test pressure, the salt rejection and water flux of the reverse osmosis membrane of the embodiment of the present invention both increase, and the reverse osmosis membrane does not have the phenomenon of high pressure-induced functional layer densification. There is no phenomenon of reduced water production, failure of functional layer or sharp decline of salt rejection, indicating that the reverse osmosis membrane of the embodiment of the present invention can withstand high operating pressure and has good pressure resistance performance.

采用本发明实施例提供的制备方法制作的反渗透膜,具备良好的脱盐率和较高水通量,可以在较高的操作压力下连续运行,具有良好的耐清洗能力,并且制备方法简单,膜寿命周期长,利于大规模生产和广泛应用,适用于超纯水制备、海水淡化等领域。The reverse osmosis membrane produced by the preparation method provided in the embodiment of the present invention has good desalination rate and high water flux, can operate continuously under high operating pressure, has good cleaning resistance, and has a simple preparation method, The membrane has a long life cycle, which is conducive to large-scale production and wide application, and is suitable for ultrapure water preparation, seawater desalination and other fields.

以上所述,仅为本发明的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应以所述权利要求的保护范围为准。The above are only specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto. Any person skilled in the art can easily think of changes or substitutions within the technical scope disclosed by the present invention. should be included within the protection scope of the present invention. Therefore, the protection scope of the present invention should be based on the protection scope of the claims.

Claims (16)

1. A reverse osmosis membrane, comprising:
a support layer comprising a flat ultrafiltration membrane;
a functional layer formed on the support layer, the functional layer comprising stacked overlapping graphene oxide sheets.
2. The reverse osmosis membrane according to claim 1, wherein the graphene oxide sheets have a sheet diameter of 8 to 20 μm and a number of layers of 2 to 10.
3. The reverse osmosis membrane according to claim 1, wherein the functional layer has a thickness of 0.1 to 0.5 μm.
4. The reverse osmosis membrane according to claim 1, wherein the surface pore size of the flat ultrafiltration membrane is 0.1-1 μm.
5. The reverse osmosis membrane of claim 1, wherein the functional layer is bonded to the support layer by an adhesive comprising any one or more of polyethylene glycol, polyvinylpyrrolidone, and polyvinyl alcohol.
6. A method for producing a reverse osmosis membrane, which is used for producing the reverse osmosis membrane according to any one of claims 1 to 5, comprising:
compounding the dispersion liquid of the graphene oxide on the surface of the supporting layer to form a composite film; the support layer comprises a flat ultrafiltration membrane;
and (3) performing coordination ion reinforcement on the composite membrane to obtain the required reverse osmosis membrane.
7. The method for preparing a reverse osmosis membrane according to claim 6, wherein the step of forming a composite membrane by compositing the dispersion of graphene oxide on the surface of the support layer comprises: spraying the dispersion of graphene oxide onto the surface of the support layer;
wherein the spraying pressure is 0.1-0.5 MPa, and the spraying time is 1-10 s.
8. The method of preparing a reverse osmosis membrane according to claim 6, wherein the step of subjecting the composite membrane to complex ion strengthening to obtain the desired reverse osmosis membrane comprises:
putting the composite membrane into a reaction solution to carry out a coordination ion strengthening reaction; the reaction solution comprises a coordination ion aqueous solution and ethanol with the same volume as the coordination ion aqueous solution;
and (3) showering the composite membrane by using ethanol, and standing the composite membrane for a certain time to obtain the required reverse osmosis membrane.
9. The preparation method of a reverse osmosis membrane according to claim 8, characterized in that the complex ion aqueous solution comprises one or more of a calcium chloride solution, a magnesium chloride solution and an aluminum chloride solution, and the mass percentage of solute in the complex ion aqueous solution is 3-10%.
10. The method for producing a reverse osmosis membrane according to claim 8, wherein the time for the complex ion strengthening reaction is 1 to 4 hours.
11. The method for preparing a reverse osmosis membrane according to claim 6, further comprising a step of preparing the dispersion liquid of graphene oxide before the step of forming the composite membrane by compositing the dispersion liquid of graphene oxide on the surface of the support layer, wherein the step of preparing the dispersion liquid of graphene oxide comprises:
dispersing graphene oxide in a dispersing agent, and adding a layer expanding stabilizer to form a dispersion liquid precursor;
and adding an alkali solution into the dispersion liquid precursor to enable the pH value of the dispersion liquid precursor to reach 7-9, so as to obtain the required dispersion liquid of the graphene oxide.
12. The method for preparing a reverse osmosis membrane according to claim 11, wherein the mass concentration of graphene oxide in the graphene oxide dispersion liquid is 0.1-5 mg/ml.
13. A method of manufacturing a reverse osmosis membrane according to claim 11, wherein the dispersant comprises any one of ultrapure water, ethanol, and N-methylpyrrolidone.
14. The preparation method of a reverse osmosis membrane according to claim 11, wherein the layer-expanding stabilizer comprises any one of sodium deoxycholate, sodium dodecylbenzenesulfonate and sodium polystyrene sulfonate, and the mass percentage of the layer-expanding stabilizer in the graphene oxide dispersion is 0.1-5%.
15. The method for preparing a reverse osmosis membrane according to claim 6, further comprising a step of treating the flat ultrafiltration membrane of the support layer before the step of forming the composite membrane by compositing the dispersion of graphene oxide on the surface of the support layer, wherein the step comprises: putting the flat ultrafiltration membrane into an aqueous solution of an adhesive, soaking and then airing; wherein in the aqueous solution of the adhesive, the mass percent of the adhesive is 1-10%.
16. The method for preparing a reverse osmosis membrane according to claim 6, further comprising a step of performing thermal reduction treatment on the composite membrane after the step of forming the composite membrane by compositing the dispersion of graphene oxide on the surface of the support layer and before the step of performing coordinated ion strengthening on the composite membrane to obtain the desired reverse osmosis membrane, wherein the step of performing thermal reduction treatment on the composite membrane comprises: and (3) heating the composite film at the temperature of 60-80 ℃ in vacuum for 30-45 min, and then cooling to room temperature.
CN201811052153.5A 2018-09-10 2018-09-10 A kind of reverse osmosis membrane and preparation method thereof Expired - Fee Related CN110882632B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811052153.5A CN110882632B (en) 2018-09-10 2018-09-10 A kind of reverse osmosis membrane and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811052153.5A CN110882632B (en) 2018-09-10 2018-09-10 A kind of reverse osmosis membrane and preparation method thereof

Publications (2)

Publication Number Publication Date
CN110882632A true CN110882632A (en) 2020-03-17
CN110882632B CN110882632B (en) 2022-03-11

Family

ID=69745149

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811052153.5A Expired - Fee Related CN110882632B (en) 2018-09-10 2018-09-10 A kind of reverse osmosis membrane and preparation method thereof

Country Status (1)

Country Link
CN (1) CN110882632B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111533117A (en) * 2020-05-13 2020-08-14 四川大学 Metal ion crosslinked high-strength stable graphene oxide membrane and preparation method thereof

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012177033A2 (en) * 2011-06-20 2012-12-27 주식회사 엘지화학 Reverse osmosis membrane having superior salt rejection and permeate flow, and method for manufacturing same
WO2014168629A1 (en) * 2013-04-12 2014-10-16 General Electric Company Membranes comprising graphene
WO2015048442A1 (en) * 2013-09-26 2015-04-02 The Regents Of The University Of Colorado, A Body Corporate Novel nano-patterned thin film membranes and thin film composite membranes, and methods using same
CN104619403A (en) * 2012-09-26 2015-05-13 东丽株式会社 Composite semipermeable membrane
WO2015142938A1 (en) * 2014-03-17 2015-09-24 Washington University Composite nanostructures having a crumpled graphene oxide shell
US20160038885A1 (en) * 2014-08-08 2016-02-11 University Of Southern California High performance membranes for water reclamation using polymeric and nanomaterials
CN107638805A (en) * 2017-11-03 2018-01-30 宁波日新恒力科技有限公司 A kind of coating modified reverse osmosis membrane preparation method of graphene oxide/polyvinyl alcohol

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012177033A2 (en) * 2011-06-20 2012-12-27 주식회사 엘지화학 Reverse osmosis membrane having superior salt rejection and permeate flow, and method for manufacturing same
CN104619403A (en) * 2012-09-26 2015-05-13 东丽株式会社 Composite semipermeable membrane
WO2014168629A1 (en) * 2013-04-12 2014-10-16 General Electric Company Membranes comprising graphene
WO2015048442A1 (en) * 2013-09-26 2015-04-02 The Regents Of The University Of Colorado, A Body Corporate Novel nano-patterned thin film membranes and thin film composite membranes, and methods using same
US20160214069A1 (en) * 2013-09-26 2016-07-28 The Regents Of The University Of Colorado, A Body Corporate Novel nano-patterned thin film membranes and thin film composite membranes, and methods using same
WO2015142938A1 (en) * 2014-03-17 2015-09-24 Washington University Composite nanostructures having a crumpled graphene oxide shell
US20160038885A1 (en) * 2014-08-08 2016-02-11 University Of Southern California High performance membranes for water reclamation using polymeric and nanomaterials
CN107638805A (en) * 2017-11-03 2018-01-30 宁波日新恒力科技有限公司 A kind of coating modified reverse osmosis membrane preparation method of graphene oxide/polyvinyl alcohol

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111533117A (en) * 2020-05-13 2020-08-14 四川大学 Metal ion crosslinked high-strength stable graphene oxide membrane and preparation method thereof

Also Published As

Publication number Publication date
CN110882632B (en) 2022-03-11

Similar Documents

Publication Publication Date Title
CN103272491B (en) Preparation method for in situ self-assembled organic/inorganic hybrid membrane based on coordination
CN109092087B (en) A kind of graphene oxide modified polyamide composite nanofiltration membrane and preparation method thereof
CN103977718B (en) Positive osmosis composite membrane of a kind of high water flux and preparation method thereof
CN103877871B (en) A kind of composite separating film, its preparation method and application
CN103706264B (en) LBL self-assembly graphene oxide NF membrane and preparation method thereof
CN106064023A (en) The preparation of a kind of functional graphene oxide composite membrane and application
CN106110910A (en) A kind of infiltration vaporization separation film and preparation method thereof
CN104548974B (en) A kind of preparation method of zinc-oxide nano composite hyperfiltration membrane
CN103301758B (en) Preparation method of graphene/polypyrrole composited forward osmosis membrane
CN106823854A (en) A kind of preparation method of polymer-based metal organic backbone hybridized film
CN102580562A (en) Method for preparing polyvinylidene fluoride composite cellulose acetate forward osmosis membrane
CN106621856A (en) Stable-structure high-performance graphene oxide nanofiltration composite membrane and preparation method thereof
CN103480283B (en) Preparation method of hydrophilic ethylene/vinyl alcohol copolymer composite flat plate ultrafiltration membrane
CN108159894A (en) A kind of preparation method of polyvinyl alcohol composite nanometer filtering film
CN107737530A (en) A kind of modified graphene oxide/dissaving polymer composite membrane, preparation method and application
CN106621831A (en) Method for performing fast in-situ conversion on microfiltration or ultrafiltration membrane into nanofiltration membrane
CN112934007B (en) Method for preparing ZIF-8/GO composite gas separation membrane by converting ZIF-8 precursor
CN107297156A (en) A kind of preparation method of the compound forward osmosis membrane based on interfacial polymerization
CN115888441B (en) Composite nanofiltration membrane and preparation method thereof
CN117000067A (en) Crosslinked graphene oxide/covalent organic framework nanofiltration membrane and preparation method thereof
CN110882632A (en) Reverse osmosis membrane and preparation method thereof
CN105921034A (en) Preparation and application of graphene oxide-modified cellulose acetate forward osmosis membrane
CN105582816A (en) Preparation method of forward osmosis membrane modified with oxidized graphene
CN106914144A (en) A kind of method that reverse diffusion technique prepares hydrotalcite composite membrane
CN115693017A (en) Diaphragm slurry, preparation method thereof, and diaphragm for alkaline water electrolysis

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
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20220311