CN115608163A - A method for preparing symmetrical polyamide membranes in a solvent-free environment - Google Patents
A method for preparing symmetrical polyamide membranes in a solvent-free environment Download PDFInfo
- Publication number
- CN115608163A CN115608163A CN202211462288.5A CN202211462288A CN115608163A CN 115608163 A CN115608163 A CN 115608163A CN 202211462288 A CN202211462288 A CN 202211462288A CN 115608163 A CN115608163 A CN 115608163A
- Authority
- CN
- China
- Prior art keywords
- symmetrical
- membrane
- acyl chloride
- polyamide
- gas
- 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
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/26—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
- C08G69/32—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids from aromatic diamines and aromatic dicarboxylic acids with both amino and carboxylic groups aromatically bound
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0006—Organic membrane manufacture by chemical reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/56—Polyamides, e.g. polyester-amides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/02—Details relating to pores or porosity of the membranes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
一种无溶剂环境制备对称聚酰胺膜的方法,分别取胺类化合物和酰氯类化合物作为原料,将其分别置于40~100℃温度环境中进行气相化处理,过程中将实时产生的气相胺类化合物和气相酰氯类化合物分别输送至内部夹持有对称多孔基底膜的密闭膜具中,并使气相胺类化合物和气相酰氯类化合物分别位于密闭膜具内对称多孔基底膜的一侧,该气相胺类化合物和气相酰氯类化合物将在对称多孔基底膜上于40~100℃温度条件下进行聚合反应30~180min,即制得成品对称聚酰胺膜。本发明的制备方法全程不使用任何溶剂,减少了环境污染,降低了成本,制得的聚酰胺膜结构疏松,具有完全对称结构,膜层结合度高,不易剥离,且分离性能优异。
A method for preparing symmetrical polyamide membranes in a solvent-free environment. Amine compounds and acyl chloride compounds are used as raw materials, and they are respectively placed in a temperature environment of 40-100°C for gas-phase treatment. During the process, the gas-phase amines generated in real time The gas-phase amine compounds and gas-phase acyl chloride compounds are transported to the closed membrane with a symmetrical porous basement membrane inside, and the gas-phase amine compounds and gas-phase acyl chlorides are respectively located on one side of the symmetrical porous basement membrane in the closed membrane. Gas-phase amine compounds and gas-phase acyl chloride compounds will be polymerized on the symmetrical porous base membrane at a temperature of 40-100°C for 30-180 minutes to obtain a finished symmetrical polyamide membrane. The preparation method of the present invention does not use any solvent in the whole process, reduces environmental pollution and cost, and the prepared polyamide membrane has a loose structure, a completely symmetrical structure, a high degree of membrane layer bonding, is not easy to peel off, and has excellent separation performance.
Description
技术领域technical field
本发明涉及膜分离技术领域,具体的说是一种无溶剂聚合法制备对称聚酰胺膜的方法。The invention relates to the technical field of membrane separation, in particular to a method for preparing a symmetrical polyamide membrane by a solventless polymerization method.
背景技术Background technique
聚酰胺膜已广泛应用于分离领域,如从混合气体中分离出二氧化碳、从混合气体中分离出氢气或海水淡化等方向。聚酰胺膜的传统制备方法为界面聚合法,即将胺类化合物溶解在去离子水或离子液体中记作A相溶液,再将酰氯类化合物溶解在有机溶剂(如正己烷、正十二烷和正十六烷等)中记作B相溶液。多孔基底由无纺布层和聚砜层组成。多孔基底聚砜层侧先浸渍在A相溶液中一定时间后晾干,再使同一侧浸渍在B相溶液中一定时间后晾干,接着在一定温度(40~90℃)下聚合一定时间后在多孔基底聚砜层上生成致密的聚酰胺层,制得聚酰胺膜。这种方法所制备的聚酰胺膜由三层结构组成,即最上面的聚酰胺层,中间的聚砜层和最下面的无纺布层,因此,传统界面聚合法制备的聚酰胺膜为非对称膜,真正起分离作用的为最上层的聚酰胺层。这种传统制备工艺的缺点在于:Polyamide membranes have been widely used in the field of separation, such as separating carbon dioxide from mixed gases, separating hydrogen from mixed gases, or seawater desalination, etc. The traditional preparation method of polyamide membrane is the interfacial polymerization method, that is, the amine compound is dissolved in deionized water or ionic liquid as a phase A solution, and then the acid chloride compound is dissolved in an organic solvent (such as n-hexane, n-dodecane and n-dodecane). Hexadecane, etc.) is recorded as the B-phase solution. The porous substrate consists of a nonwoven layer and a polysulfone layer. The side of the polysulfone layer of the porous substrate is first immersed in the A phase solution for a certain period of time and then dried, then the same side is immersed in the B phase solution for a certain period of time and then dried, and then polymerized at a certain temperature (40~90°C) for a certain period of time A dense polyamide layer is formed on a porous substrate polysulfone layer to obtain a polyamide membrane. The polyamide membrane prepared by this method is composed of a three-layer structure, namely the uppermost polyamide layer, the middle polysulfone layer and the lowermost non-woven layer. Therefore, the polyamide membrane prepared by the traditional interfacial polymerization method is non-toxic Symmetrical membrane, the uppermost polyamide layer really plays a role in separation. The disadvantages of this traditional preparation process are:
1、传统界面聚合法制备的聚酰胺膜中的聚酰胺层结构致密,不利于分子穿过,因此气体分子渗透量或水通量较小。2、由于胺类化合物和酰氯类化合物的传统界面聚合过程为剧烈的放热反应,故生成的聚酰胺层表面呈现出叶状或结节状,使聚酰胺膜均一性差,分离性能不稳定。3、传统界面聚合法制备的聚酰胺膜为非对称膜,不但聚酰胺层容易从基底上脱离,而且聚酰胺膜的分离操作只有从聚酰胺层侧进行。4、传统界面聚合法制备聚酰胺膜的过程需使用有毒、易燃的有机溶剂,存在环境污染问题;或使用价格较高的离子液体,制备成本较高。1. The polyamide layer structure in the polyamide membrane prepared by the traditional interfacial polymerization method is dense, which is not conducive to the passage of molecules, so the permeation of gas molecules or water flux is small. 2. Since the traditional interfacial polymerization process of amine compounds and acid chloride compounds is a violent exothermic reaction, the surface of the formed polyamide layer presents a leaf-like or nodular shape, resulting in poor uniformity of the polyamide membrane and unstable separation performance. 3. The polyamide membrane prepared by the traditional interfacial polymerization method is an asymmetric membrane, not only the polyamide layer is easily detached from the substrate, but also the separation operation of the polyamide membrane can only be carried out from the polyamide layer side. 4. The process of preparing polyamide membrane by traditional interfacial polymerization requires the use of toxic and flammable organic solvents, which has environmental pollution problems; or the use of high-priced ionic liquids, resulting in high preparation costs.
因此,如何对现有的制备工艺进行改进,使其能够低成本、快速、高效地制备出结构均匀的聚酰胺膜,对于降低环境污染,提高聚酰胺膜的分离性能来说实为必要。Therefore, how to improve the existing preparation process so that it can prepare polyamide membranes with uniform structure at low cost, quickly and efficiently is necessary to reduce environmental pollution and improve the separation performance of polyamide membranes.
发明内容Contents of the invention
本发明的技术目的为:在不使用任何溶剂的条件下,制备一种结构疏松,具有完全对称结构,膜层结合度高,不易剥离,且分离性能优异的聚酰胺膜,来减少环境污染,降低成本。The technical purpose of the present invention is: to prepare a polyamide membrane with a loose structure, a completely symmetrical structure, a high degree of membrane bonding, not easy to peel off, and excellent separation performance without using any solvent, so as to reduce environmental pollution. cut costs.
本发明为解决上述技术问题所采用的技术方案为:一种无溶剂环境制备对称聚酰胺膜的方法,按照一定的摩尔配比,分别取胺类化合物和酰氯类化合物作为原料,将称取的胺类化合物和酰氯类化合物分别置于40~100℃温度环境中进行气相化处理,在该气相化处理的过程中,将实时产生的气相胺类化合物和气相酰氯类化合物分别输送至内部夹持有对称多孔基底膜的密闭膜具中,并使气相胺类化合物和气相酰氯类化合物分别位于密闭膜具内对称多孔基底膜的一侧,该气相胺类化合物和气相酰氯类化合物将在对称多孔基底膜上于40~100℃温度条件下进行聚合反应30~180min,即制得成品对称聚酰胺膜。The technical scheme adopted by the present invention to solve the above-mentioned technical problems is: a method for preparing symmetrical polyamide membranes in a solvent-free environment. According to a certain molar ratio, amine compounds and acid chloride compounds are respectively taken as raw materials, and the The amine compounds and the acid chloride compounds are respectively placed in a temperature environment of 40~100°C for gas-phase treatment. During the gas-phase treatment, the gas-phase amine compounds and gas-phase acid chloride compounds generated in real time are respectively transported to the internal clamping There is a closed membrane with a symmetrical porous base membrane, and the gas phase amine compound and the gas phase acid chloride compound are respectively located on one side of the symmetrical porous base membrane in the closed membrane, and the gas phase amine compound and the gas phase acid chloride compound will be in the symmetrical porous Polymerization is carried out on the basement membrane at a temperature of 40-100°C for 30-180 minutes to obtain a finished symmetrical polyamide membrane.
优选的,所述的胺类化合物为邻苯二胺、间苯二胺、对苯二胺、乙二胺、二亚乙基三胺、三亚乙基四胺和哌嗪中的任意一种。Preferably, the amine compound is any one of o-phenylenediamine, m-phenylenediamine, p-phenylenediamine, ethylenediamine, diethylenetriamine, triethylenetetramine and piperazine.
优选的,所述的酰氯类化合物为均苯三甲酰氯、邻苯二甲酰氯、间苯二甲酰氯和对苯二甲酰氯中的任意一种。Preferably, the acid chloride compound is any one of trimesoyl chloride, phthaloyl chloride, isophthaloyl chloride and terephthaloyl chloride.
优选的,所述对称多孔基底膜的孔径为1~400nm。Preferably, the pore diameter of the symmetrical porous basement membrane is 1-400 nm.
优选的,所述的对称多孔基底膜以对称聚丙烯腈、对称聚偏氟乙烯、对称尼龙、对称聚醚砜、对称混合纤维素或对称聚氯乙烯为基底。Preferably, the symmetrical porous base membrane is based on symmetrical polyacrylonitrile, symmetrical polyvinylidene fluoride, symmetrical nylon, symmetrical polyethersulfone, symmetrical mixed cellulose or symmetrical polyvinyl chloride.
优选的,所述原料中胺类化合物和酰氯类化合物的摩尔比为1:1至1:3。Preferably, the molar ratio of the amine compound and the acid chloride compound in the raw material is 1:1 to 1:3.
一种无溶剂环境制备对称聚酰胺膜的方法,具体包括以下步骤:A method for preparing symmetrical polyamide membranes in a solvent-free environment, specifically comprising the following steps:
步骤一、取对称多孔基底膜竖直夹持在密闭膜具中,在密闭模具的左右两侧分别通过一根连接导管与胺类化合物储存瓶和酰氯类化合物储存瓶的内部连通,制成一个聚合反应装置,备用;Step 1. Take the symmetrical porous basement membrane and clamp it vertically in the airtight membrane tool. On the left and right sides of the airtight mold, connect with the inside of the amine compound storage bottle and the acyl chloride compound storage bottle through a connecting conduit respectively to form a Polymerization reaction device, standby;
步骤二、先称取0.1~3g胺类化合物置于胺类化合物储存瓶中,再称取一定量酰氯类化合物置于酰氯类化合物储存瓶中,保证称取的酰氯类化合物的摩尔数为胺类化合物摩尔数的1~3倍,备用;
步骤三、将步骤一制成的聚合反应装置放入温度为40~100℃的烘箱中进行聚合反应30~180min,胺类化合物储存瓶内产生的气相胺类化合物和酰氯类化合物储存瓶内产生的气相酰氯类化合物将经由连接导管进入密闭膜具中,在对称多孔基底膜的表面发生聚合反应,最终制得成品对称聚酰胺膜。
优选的,在步骤一中,所述的对称多孔基底膜夹持在密闭膜具的内部中心处,连接导管连接于密闭模具左右两侧的中部。Preferably, in Step 1, the symmetrical porous base membrane is clamped at the inner center of the closed mold, and the connecting conduit is connected to the middle of the left and right sides of the closed mold.
有益效果:Beneficial effect:
1、本发明的制备方法采用气相聚合的方式,在不使用任何溶剂的条件下,即可快速、高效地制备出了结构稳固,膜层结合度高,不易剥离,且具有完全对称结构的聚酰胺膜。制备得到的聚酰胺膜,结构疏松、均一,避免了传统界面聚合制备的聚酰胺膜结构致密、且聚合过程剧烈放热造成膜结构不均匀的现象,因此,表现出了比传统界面聚合制备的聚酰胺膜更好的分离性能。1. The preparation method of the present invention adopts the method of gas phase polymerization, and without using any solvent, it can quickly and efficiently prepare a polymer with a stable structure, a high degree of film bonding, not easy to peel off, and a completely symmetrical structure. Amide film. The prepared polyamide membrane has a loose and uniform structure, which avoids the dense structure of the polyamide membrane prepared by traditional interfacial polymerization and the phenomenon of uneven membrane structure caused by the intense heat release during the polymerization process. Polyamide membrane for better separation performance.
2、本发明的制备工艺工序简单易操作,同时避免了使用有机溶剂造成的环境污染问题,并降低的制备成本。2. The preparation process of the present invention is simple and easy to operate, while avoiding the environmental pollution problem caused by the use of organic solvents, and reducing the preparation cost.
3、本发明的制备工艺可以通过调节温度,控制胺类化合物和酰氯类化合物形成气相的速率以及气相体积密度,进而影响聚合过程,获得结构疏松的对称聚酰胺膜,更有利于分子穿过,即无溶剂聚合法制备的对称聚酰胺膜拥有较大的气体分子渗透量或水通量。同时,气相体积密度的调控,使两种气相发生聚合的过程缓慢,生成的对称膜材料微结构均匀,使对称聚酰胺膜表现出稳定的分离性能。无溶剂聚合法制备的聚酰胺膜为对称膜,聚酰胺结构和基底完美融合,二者不会发生剥离。无溶剂聚合法制备的对称聚酰胺膜过程不使用有毒、易燃的有机溶剂,没有环境污染问题;也不使用价格高的离子液体,制备成本较低。3. The preparation process of the present invention can adjust the temperature to control the rate of formation of the gas phase and the volume density of the gas phase of the amine compound and the acid chloride compound, thereby affecting the polymerization process and obtaining a symmetrical polyamide membrane with a loose structure, which is more conducive to the passage of molecules. That is, the symmetrical polyamide membrane prepared by the solvent-free polymerization method has a large gas molecule permeation or water flux. At the same time, the adjustment of the volume density of the gas phase makes the polymerization process of the two gas phases slow, and the microstructure of the formed symmetrical membrane material is uniform, so that the symmetrical polyamide membrane exhibits stable separation performance. The polyamide membrane prepared by the solvent-free polymerization method is a symmetrical membrane, and the polyamide structure and the substrate are perfectly integrated without peeling off. The symmetric polyamide membrane prepared by the solvent-free polymerization method does not use toxic and flammable organic solvents, so there is no environmental pollution problem; high-priced ionic liquids are not used, and the preparation cost is low.
4、本发明的制备工艺通过调节反应物温度(40~100℃),使胺类化合物和酰氯类化合物成为气相状态,并分别接触对称多孔基底膜的左右两侧。胺类化合物分子和酰氯类化合物分子在对称多孔基底膜中相互渗透并接触,胺类化合物分子的胺基和酰氯类化合物分子的酰氯基团发生缩合反应生成酰胺基团,最终聚酰胺网络结构相互连通并包裹对称多孔基底膜,形成对称聚酰胺膜。两者结合度高,不易分离,且均一性强,使成品聚酰胺膜的分离能力得到显著改善。4. In the preparation process of the present invention, by adjusting the temperature of the reactants (40-100°C), the amine compounds and the acyl chloride compounds are in the gas phase state and contact the left and right sides of the symmetrical porous basement membrane respectively. The amine compound molecules and the acid chloride compound molecules penetrate and contact each other in the symmetrical porous basement membrane, and the amine groups of the amine compound molecules and the acid chloride groups of the acid chloride compound molecules undergo condensation reactions to form amide groups, and finally the polyamide network structure interacts with each other. Connecting and wrapping the symmetrical porous basement membrane to form a symmetrical polyamide membrane. The combination of the two is high, it is not easy to separate, and the uniformity is strong, so that the separation ability of the finished polyamide membrane is significantly improved.
附图说明Description of drawings
图1为本发明所采用聚合反应装置的结构示意图;Fig. 1 is the structural representation of the polymerization reaction device that the present invention adopts;
图2为本发明实施例1所制备对称聚酰胺膜的照片;Fig. 2 is the photo of the symmetrical polyamide membrane prepared by the embodiment of the present invention 1;
图3为本发明实施例1所制备对称聚酰胺膜的FESEM图。Fig. 3 is a FESEM image of the symmetrical polyamide membrane prepared in Example 1 of the present invention.
附图说明:1、胺类化合物,2、酰氯类化合物,3、胺类化合物储存瓶,4、酰氯类化合物储存瓶,5、气相胺类化合物,6、气相酰氯类化合物,7、连接导管,8、密闭膜具,9、对称多孔基底膜。Description of drawings: 1. Amine compounds, 2. Acid chloride compounds, 3. Amine compound storage bottle, 4. Acid chloride compound storage bottle, 5. Gas phase amine compound, 6. Gas phase acid chloride compound, 7. Connecting conduit , 8, closed membrane tool, 9, symmetrical porous basement membrane.
具体实施方式detailed description
下面结合附图和具体实施例对本发明的技术方案做进一步详细的阐述和说明。The technical solution of the present invention will be further elaborated and described below in conjunction with the accompanying drawings and specific embodiments.
如附图1所示,一种无溶剂环境制备对称聚酰胺膜的方法,其以孔径为1~400纳米的对称多孔基底膜(如对称聚丙烯腈、对称聚偏氟乙烯、对称尼龙、对称聚醚砜、对称混合纤维素、对称聚氯乙烯等)为基底。称取0.1~3g胺类化合物(1)放入胺类化合物储存瓶(3)中,再称取一定量的酰氯类化合物(2)(保证酰氯类化合物的摩尔数为胺类化合物摩尔数的1~3倍)放入酰氯类化合物储存瓶(4)中。对称多孔基底膜(9)夹持在密闭膜具(8)中。将整个聚合反应装置在设定温度(40~100℃)的烘箱中一定时间(30~180min)。此过程中,胺类化合物(1)和酰氯类化合物(2)生成对应气相胺类化合物(5)和气相酰氯类化合物(6)。两种气相经过连接导管(7)分别接触对称多孔基底膜(9),在对称多孔基底膜(9)内和表面聚合最终生成对称聚酰胺膜。As shown in Figure 1, a method for preparing a symmetrical polyamide membrane in a solvent-free environment uses a symmetrical porous substrate membrane (such as symmetrical polyacrylonitrile, symmetrical polyvinylidene fluoride, symmetrical nylon, symmetrical Polyethersulfone, symmetrical mixed cellulose, symmetrical polyvinyl chloride, etc.) as the base. Weigh 0.1~3g of amine compound (1) into the amine compound storage bottle (3), and then weigh a certain amount of acid chloride compound (2) (guarantee that the moles of the acid chloride compound are equal to the moles of the amine compound 1~3 times) into the storage bottle (4) of the acid chloride compound. The symmetrical porous basement membrane (9) is clamped in the airtight membrane tool (8). Place the entire polymerization reaction device in an oven at a set temperature (40-100°C) for a certain period of time (30-180min). During this process, the amine compound (1) and the acid chloride compound (2) generate the corresponding gas phase amine compound (5) and gas phase acid chloride compound (6). The two gas phases respectively contact the symmetrical porous basement membrane (9) through the connecting conduit (7), and polymerize in and on the surface of the symmetrical porous basement membrane (9) to finally form a symmetrical polyamide membrane.
该工艺方法通过调节温度(40~100℃),使胺类化合物(如邻苯二胺、间苯二胺、对苯二胺、乙二胺、二亚乙基三胺、三亚乙基四胺、哌嗪等)和酰氯类化合物(如均苯三甲酰氯、邻苯二甲酰氯、间苯二甲酰氯、对苯二甲酰氯等)成为气相状态,并分别接触对称多孔基底膜两侧。胺类化合物分子和酰氯类化合物分子在对称多孔基底膜中相互渗透并接触,胺类化合物分子的胺基和酰氯类化合物分子的酰氯基团发生缩合反应生成酰胺基团,最终聚酰胺网络结构相互连通并包裹对称多孔基底膜,形成对称聚酰胺膜。该方法避免了传统界面聚合法制备的非对称聚酰胺膜结构致密,易造成环境污染的缺陷,能够改善聚酰胺膜的分离能力。The process adjusts the temperature (40~100°C) to make amine compounds (such as o-phenylenediamine, m-phenylenediamine, p-phenylenediamine, ethylenediamine, diethylenetriamine, triethylenetetramine , piperazine, etc.) and acyl chlorides (such as trimesoyl chloride, phthaloyl chloride, isophthaloyl chloride, terephthaloyl chloride, etc.) become gas phase and contact both sides of the symmetrical porous basement membrane respectively. The amine compound molecules and the acid chloride compound molecules penetrate and contact each other in the symmetrical porous basement membrane, and the amine groups of the amine compound molecules and the acid chloride groups of the acid chloride compound molecules undergo condensation reactions to form amide groups, and finally the polyamide network structure interacts with each other. Connecting and wrapping the symmetrical porous basement membrane to form a symmetrical polyamide membrane. The method avoids the defects that the asymmetric polyamide membrane prepared by the traditional interfacial polymerization method has a compact structure and is likely to cause environmental pollution, and can improve the separation ability of the polyamide membrane.
实施例1:Example 1:
称取1g间苯二胺放入胺类化合物储存瓶中,再称取2.45g均苯三甲酰氯放入酰氯类化合物储存瓶中(间苯二胺和均苯三甲酰氯的摩尔比为1:1)。取对称聚丙烯腈基底膜夹持在膜具中。将聚合反应装置放入70℃的烘箱中90min。此过程中,间苯二胺和均苯三甲酰氯生成对应气相间苯二胺和气相均苯三甲酰氯。两种气相经过连接导管分别接触对称多孔基底膜的左右两侧,在对称聚丙烯腈基底膜内和表面聚合最终生成对称聚酰胺膜。Weigh 1g of m-phenylenediamine into the amine compound storage bottle, then weigh 2.45g of trimesoyl chloride into the acid chloride compound storage bottle (the molar ratio of m-phenylenediamine to trimesoyl chloride is 1:1 ). Take the symmetrical polyacrylonitrile basement membrane and clamp it in the membrane tool. Put the polymerization reaction apparatus into an oven at 70° C. for 90 minutes. During this process, m-phenylenediamine and trimesoyl chloride generate corresponding gas phase m-phenylenediamine and gas phase trimesoyl chloride. The two gas phases respectively contact the left and right sides of the symmetrical porous basement membrane through the connecting conduit, and polymerize in and on the surface of the symmetrical polyacrylonitrile basement membrane to finally form a symmetrical polyamide membrane.
实施例2:Example 2:
本实施例的制备方法同实施例1,仅将其中均苯三甲酰氯的用量调整为3.68g(间苯二胺和均苯三甲酰氯的摩尔比为1:1.5)。The preparation method of this example is the same as that of Example 1, except that the amount of trimesoyl chloride is adjusted to 3.68 g (the molar ratio of m-phenylenediamine to trimesoyl chloride is 1:1.5).
实施例3:Example 3:
本实施例的制备方法同实施例1,仅将其中均苯三甲酰氯的用量调整为7.36g(间苯二胺和均苯三甲酰氯的摩尔比为1:3)。The preparation method of this example is the same as that of Example 1, except that the amount of trimesoyl chloride is adjusted to 7.36 g (the molar ratio of m-phenylenediamine and trimesoyl chloride is 1:3).
实施例4:Example 4:
本实施例的制备方法同实施例1,仅将其中烘箱温度设置为50℃。The preparation method of this embodiment is the same as that of Example 1, except that the temperature of the oven is set at 50°C.
实施例5:Example 5:
本实施例的制备方法同实施例1,仅将其中选用的原料1g间苯二胺替换为1g对苯二胺。The preparation method of this embodiment is the same as that of Example 1, except that 1 g of m-phenylenediamine as a raw material is replaced by 1 g of p-phenylenediamine.
实施例6:Embodiment 6:
本实施例的制备方法同实施例1,仅将其中选用的2.45g均苯三甲酰氯替换为1.88g间苯二甲酰氯。The preparation method of this embodiment is the same as that of Example 1, except that 2.45 g of trimesoyl chloride is replaced by 1.88 g of isophthaloyl chloride.
实施例7:Embodiment 7:
本实施例的制备方法同实施例1,仅将其中烘箱内的聚合反应调整为180min。The preparation method of this embodiment is the same as that of Example 1, only the polymerization reaction in the oven is adjusted to 180min.
下面对各个实施例制得的对称聚酰胺膜进行使用性能测试如下:The symmetric polyamide membrane prepared by each embodiment is tested for performance as follows:
表1Table 1
由表1可知,由无溶剂聚合法制备的对称聚酰胺膜表现出较好的CO2分离性能。实施例2、3和实施例1对比可知,增加均苯三甲酰氯的用量,提高了CO2/CH4和CO2/N2的分离系数,但CO2渗透量有所降低。实施例4和实施例1对比可知,适当降低聚合温度可以提高对称聚酰胺膜的CO2渗透量。实施例5和实施例1对比可知,采用间苯二胺为胺类化合物来源制备的聚酰胺膜CO2渗透量更大,但CO2/CH4和CO2/N2的分离系数降低。实施例6和实施例1对比可知,采用间苯二甲酰氯为酰氯类化合物来源制备的聚酰胺膜CO2渗透量更大,但CO2/CH4和CO2/N2的分离系数降低,其原因可能为相比均苯三甲酰氯,间苯二甲酰氯分子少一个酰氯基团。实施例7和实施例1对比可知,延长聚合时间,更有利于获得致密的聚酰胺膜。综合以上性能可知,本发明制备的对称聚酰胺膜与现有文献中报道的膜材料相比,具有显著优势。As can be seen from Table 1, the symmetric polyamide membrane prepared by the solvent-free polymerization method exhibited better CO2 separation performance. Comparing Examples 2 and 3 with Example 1, it can be seen that increasing the amount of trimesoyl chloride increases the separation coefficients of CO 2 /CH 4 and CO 2 /N 2 , but the amount of CO 2 permeated decreases. Comparing Example 4 with Example 1, it can be seen that appropriately lowering the polymerization temperature can increase the CO 2 permeation rate of the symmetrical polyamide membrane. Comparing Example 5 with Example 1, it can be seen that the polyamide membrane prepared with m-phenylenediamine as the source of amine compounds has a greater CO 2 permeation capacity, but the separation coefficients of CO 2 /CH 4 and CO 2 /N 2 are reduced. Comparing Example 6 with Example 1, it can be seen that the polyamide membrane prepared with isophthaloyl chloride as the source of acid chlorides has a larger CO permeation capacity, but the separation coefficients of CO 2 / CH 4 and CO 2 /N 2 are reduced, The reason may be that compared with trimesoyl chloride, isophthaloyl chloride molecule has one less acid chloride group. Comparing Example 7 with Example 1, it can be seen that prolonging the polymerization time is more conducive to obtaining a dense polyamide film. Based on the above properties, it can be seen that the symmetrical polyamide membrane prepared by the present invention has significant advantages compared with the membrane materials reported in the existing literature.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211462288.5A CN115608163A (en) | 2022-11-17 | 2022-11-17 | A method for preparing symmetrical polyamide membranes in a solvent-free environment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211462288.5A CN115608163A (en) | 2022-11-17 | 2022-11-17 | A method for preparing symmetrical polyamide membranes in a solvent-free environment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN115608163A true CN115608163A (en) | 2023-01-17 |
Family
ID=84878251
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202211462288.5A Pending CN115608163A (en) | 2022-11-17 | 2022-11-17 | A method for preparing symmetrical polyamide membranes in a solvent-free environment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115608163A (en) |
-
2022
- 2022-11-17 CN CN202211462288.5A patent/CN115608163A/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2014087928A1 (en) | Gas separation membrane, gas separation module, gas separation device, and gas separation method | |
CN109925896B (en) | Hybrid composite membrane, preparation method and application thereof | |
Wu et al. | Facile synthesis of molecular sieve membranes following “like grows like” principle | |
JP2016503448A (en) | Blend polymer membrane for gas separation containing fluorinated ethylene-propylene polymer | |
JP2015073980A (en) | Gas separation membrane and gas separation membrane module | |
JPS60202713A (en) | Membrane from organic polymer containing crystalline carriercompound and manufacture thereof | |
CN113893711B (en) | High-flux reverse osmosis composite membrane and preparation method thereof | |
CN107922610A (en) | The method of reverse osmosis membrane is manufactured for the composition of polyamide interfacial polymerization and using it | |
US20240024827A1 (en) | Preparation method of reverse osmosis composite membrane and reverse osmosis composite membrane prepared thereby | |
JP2009241006A (en) | Composite membrane and its manufacturing method | |
WO2018221684A1 (en) | Gas separation membrane, gas separation membrane element, gas separator, and gas separation method | |
JP7337629B2 (en) | Separation membrane and membrane separation method | |
WO2015033772A1 (en) | Composite gas separation membrane, gas separation module, gas separation apparatus and gas separation method | |
US20180339275A1 (en) | Gas separation membrane, gas separation module, gas separator, and gas separation method | |
CN111589309B (en) | Attapulgite-polydimethylsiloxane composite membrane and preparation method and application thereof | |
CN115608163A (en) | A method for preparing symmetrical polyamide membranes in a solvent-free environment | |
JP6282585B2 (en) | Semipermeable membrane and method for producing the same, concentration difference power generation method using semipermeable membrane | |
US20180085716A1 (en) | Gas separation membrane, gas separation module, gas separation device, gas separation method, and polyimide compound | |
JPH0260370B2 (en) | ||
CN115532086A (en) | Polyamide composite membrane for nanofiltration of organic solvent | |
JPS6311045B2 (en) | ||
JP2016137484A (en) | Gas separation membrane | |
JP2012250494A (en) | Laminated film | |
CN112755809A (en) | Forward osmosis membrane with mica sheet as intermediate layer and preparation method thereof | |
CN118846832B (en) | A method for preparing a reverse osmosis membrane capable of withstanding high temperature water environment |
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 |