CN106345308A - Preparation method for polyesteramide compound nanofiltration membrane with strong chlorine resistance and pollution resistance - Google Patents
Preparation method for polyesteramide compound nanofiltration membrane with strong chlorine resistance and pollution resistance Download PDFInfo
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- 239000012528 membrane Substances 0.000 title claims abstract description 78
- 238000001728 nano-filtration Methods 0.000 title claims abstract description 43
- 229920006149 polyester-amide block copolymer Polymers 0.000 title claims abstract description 33
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 229910052801 chlorine Inorganic materials 0.000 title claims abstract description 22
- 239000000460 chlorine Substances 0.000 title claims abstract description 22
- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- 150000001875 compounds Chemical class 0.000 title 1
- 239000002131 composite material Substances 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- VHYFNPMBLIVWCW-UHFFFAOYSA-N 4-Dimethylaminopyridine Chemical compound CN(C)C1=CC=NC=C1 VHYFNPMBLIVWCW-UHFFFAOYSA-N 0.000 claims abstract description 20
- KJJPLEZQSCZCKE-UHFFFAOYSA-N 2-aminopropane-1,3-diol Chemical compound OCC(N)CO KJJPLEZQSCZCKE-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 4
- 239000003960 organic solvent Substances 0.000 claims description 23
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims description 18
- 239000008346 aqueous phase Substances 0.000 claims description 18
- 239000012074 organic phase Substances 0.000 claims description 12
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 7
- 238000000108 ultra-filtration Methods 0.000 claims description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 6
- 239000004695 Polyether sulfone Substances 0.000 claims description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical group CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 6
- 229920006393 polyether sulfone Polymers 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- 238000005406 washing Methods 0.000 claims description 5
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 4
- 229920002492 poly(sulfone) Polymers 0.000 claims description 4
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 13
- 230000010933 acylation Effects 0.000 abstract description 7
- 238000005917 acylation reaction Methods 0.000 abstract description 7
- 239000003054 catalyst Substances 0.000 abstract description 7
- 150000001805 chlorine compounds Chemical class 0.000 abstract description 7
- 239000000178 monomer Substances 0.000 abstract description 7
- 238000012695 Interfacial polymerization Methods 0.000 abstract description 6
- 238000006555 catalytic reaction Methods 0.000 abstract description 2
- 238000009776 industrial production Methods 0.000 abstract description 2
- 239000003444 phase transfer catalyst Substances 0.000 abstract description 2
- 239000012071 phase Substances 0.000 description 7
- 239000004952 Polyamide Substances 0.000 description 5
- 229920002647 polyamide Polymers 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- 238000010612 desalination reaction Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
- 238000012876 topography Methods 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 229920000768 polyamine Polymers 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000004566 IR spectroscopy Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000003373 anti-fouling effect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000009285 membrane fouling Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- 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
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
- B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
-
- 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
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本发明公开了一种耐氯性强且抗污染的聚酯酰胺复合纳滤膜的制备方法,所述方法以丝氨醇为水相反应单体,同时将4‑二甲氨基吡啶加入水相作为相转移催化剂和酰化催化剂,通过丝氨醇与多元酰氯在多孔支撑层上的界面聚合反应制备新型聚酯酰胺复合纳滤膜。本发明通过丝氨醇与多元酰氯在4‑二甲氨基吡啶的催化作用下于多孔支撑层上进行界面聚合反应,从而获得一种新型的聚酯酰胺复合纳滤膜,该纳滤膜具有耐氯性好、亲水性强、抗污染能力强和溶质截留能力强的特点,且制备工艺简便温和,适于工业化生产。The invention discloses a preparation method of a polyester amide composite nanofiltration membrane with strong chlorine resistance and pollution resistance. In the method, serinol is used as a reaction monomer in the water phase, and 4-dimethylaminopyridine is added into the water phase at the same time As a phase transfer catalyst and acylation catalyst, a novel polyester amide composite nanofiltration membrane was prepared by interfacial polymerization of serinol and polyacyl chlorides on a porous support layer. In the present invention, a novel polyester amide composite nanofiltration membrane is obtained through interfacial polymerization reaction of serinol and polyacyl chlorides on a porous support layer under the catalysis of 4-dimethylaminopyridine. It has the characteristics of good chlorine, strong hydrophilicity, strong anti-pollution ability and strong solute interception ability, and the preparation process is simple and mild, which is suitable for industrial production.
Description
技术领域technical field
本发明属于膜分离技术领域,涉及一种耐氯性强、抗污染能力强的聚酯酰胺复合纳滤膜的制备方法。The invention belongs to the technical field of membrane separation, and relates to a preparation method of a polyester amide composite nanofiltration membrane with strong chlorine resistance and strong pollution resistance.
背景技术Background technique
随着经济的发展、人口的增加和水污染的加剧,世界多国均面临着水资源短缺的问题。因此,在额外清洁水资源无法补充的情况下,对现有的水资源进行净化处理是应对水资源危机的重要举措。纳滤膜(NF)是介于超滤膜和反渗透膜之间的一种特殊膜材料,它能够截留小分子有机物,具有部分脱盐能力,同时具有通量高、能耗低的特点,目前已经应用于水的软化、苦咸水脱盐、污水深度处理、药物与生物提纯和食品加工等众多领域。With the development of economy, the increase of population and the aggravation of water pollution, many countries in the world are facing the problem of water shortage. Therefore, when additional clean water resources cannot be replenished, the purification of existing water resources is an important measure to deal with the water resource crisis. Nanofiltration membrane (NF) is a special membrane material between ultrafiltration membrane and reverse osmosis membrane. It can intercept small molecular organic matter, has partial desalination ability, and has the characteristics of high flux and low energy consumption. At present, It has been used in many fields such as water softening, brackish water desalination, advanced sewage treatment, pharmaceutical and biological purification, and food processing.
通过多元胺和多元酰氯在支撑层上通过界面聚合反应制备的聚酰胺复合纳滤膜目前已经在纳滤膜的市场份额中占据了主导地位。然而,较为严重的膜污染问题和耐氯性差是限制其进一步推广应用的主要障碍。因此,开发具有抗污染能力且耐氯性强的新型纳滤膜是众多研究者的工作重点。现有的研究表明,由多元胺和多元酰氯制备的聚酰胺复合纳滤膜通常具有较高的污染物去除能力和脱盐能力,但其抗污染能力和耐氯性较差;而由多元酚或多元醇与多元酰氯或多元酸制备的聚酯复合纳滤膜通常具有更强的抗污染能力和耐氯性,但其膜孔较大,污染物截留能力和脱盐率较低。如何将聚酰胺纳滤膜和聚酯纳滤膜的优点相结合,从而制备一种抗污染能力强、耐氯性强和污染物去除能力强的复合纳滤膜是我们的研究目标。Polyamide composite nanofiltration membranes prepared by interfacial polymerization of polyamines and polyacyl chlorides on the support layer have occupied a dominant position in the market share of nanofiltration membranes. However, the serious membrane fouling problem and poor chlorine resistance are the main obstacles limiting its further application. Therefore, the development of new nanofiltration membranes with anti-pollution ability and strong chlorine resistance is the focus of many researchers. Existing studies have shown that polyamide composite nanofiltration membranes prepared from polyamines and polyacyl chlorides usually have high pollutant removal and desalination capabilities, but their anti-pollution and chlorine resistance are poor; Polyester composite nanofiltration membranes prepared by polyols and polyacyl chlorides or polyacids usually have stronger anti-fouling ability and chlorine resistance, but their membrane pores are larger, and the pollutant retention capacity and desalination rate are lower. How to combine the advantages of polyamide nanofiltration membrane and polyester nanofiltration membrane to prepare a composite nanofiltration membrane with strong anti-pollution ability, strong chlorine resistance and strong pollutant removal ability is our research goal.
发明内容Contents of the invention
本发明的目的是提供一种新型耐氯性强且抗污染的聚酯酰胺复合纳滤膜的制备方法,将聚酰胺纳滤膜和聚酯纳滤膜的优点相结合,解决了现有商用纳滤膜易污染、耐氯性差的问题。The purpose of the present invention is to provide a preparation method of a novel polyester amide composite nanofiltration membrane with strong chlorine resistance and anti-pollution, which combines the advantages of polyamide nanofiltration membrane and polyester nanofiltration membrane to solve the existing commercial problems. Nanofiltration membranes are prone to fouling and poor chlorine resistance.
本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
一种耐氯性强且抗污染的聚酯酰胺复合纳滤膜的制备方法,以丝氨醇为水相反应单体,同时将4-二甲氨基吡啶加入水相作为相转移催化剂和酰化催化剂,通过丝氨醇与多元酰氯在多孔支撑层上的界面聚合反应制备新型聚酯酰胺复合纳滤膜,具体步骤如下:A preparation method of a polyester amide composite nanofiltration membrane with strong chlorine resistance and anti-pollution, using serinol as a reaction monomer in the water phase, and simultaneously adding 4-dimethylaminopyridine to the water phase as a phase transfer catalyst and acylation Catalyst, through the interfacial polymerization reaction of serinol and polyacyl chloride on the porous support layer to prepare a new type of polyester amide composite nanofiltration membrane, the specific steps are as follows:
一、配制水相溶液:向纯水中加入0.5~5%(w/v)的丝氨醇,同时加入0.05~0.5%(w/v)的4-二甲氨基吡啶作为相转移和酰化催化剂,充分搅拌并溶解后采用三乙胺将溶液的pH值调至11.3~12.0;1. Preparation of aqueous phase solution: add 0.5~5% (w/v) serinol to pure water, and add 0.05~0.5% (w/v) 4-dimethylaminopyridine at the same time for phase transfer and acylation Catalyst, after fully stirring and dissolving, use triethylamine to adjust the pH value of the solution to 11.3~12.0;
二、配制有机相溶液:以正己烷、环己烷、甲苯、正庚烷或正辛烷中的一种或多种为有机溶剂,向有机溶剂中加入0.01~0.5%(w/v)的多元酰氯;2. Prepare the organic phase solution: use one or more of n-hexane, cyclohexane, toluene, n-heptane or n-octane as the organic solvent, and add 0.01~0.5% (w/v) of Polyacid chlorides;
三、以聚砜、聚醚砜、磺化聚醚砜或聚丙烯多孔超滤膜为支承层,首先将水相溶液倒向支撑层表面并浸泡1~10 分钟,然后倒掉水相溶液并除去膜面多余水分,接着将有机相溶液倒向膜面,并反应10~120 秒,反应结束后采用有机溶剂对膜面进行充分冲洗以去除未反应单体;3. With polysulfone, polyethersulfone, sulfonated polyethersulfone or polypropylene porous ultrafiltration membrane as the supporting layer, first pour the aqueous phase solution onto the surface of the supporting layer and soak for 1 to 10 minutes, then pour off the aqueous phase solution and dry it. Remove excess moisture from the membrane surface, then pour the organic phase solution onto the membrane surface, and react for 10-120 seconds. After the reaction, fully rinse the membrane surface with an organic solvent to remove unreacted monomers;
四、将有机溶剂冲洗过后的膜放在20~80℃下热处理5~20分钟;4. Heat-treat the film after washing with organic solvent at 20-80°C for 5-20 minutes;
五、最后用纯水对膜进行充分清洗,由此获得聚酯酰胺复合纳滤膜。5. Finally, the membrane is fully washed with pure water to obtain a polyester amide composite nanofiltration membrane.
本发明通过丝氨醇与多元酰氯在4-二甲氨基吡啶的催化作用下于多孔支撑层上进行界面聚合反应,从而获得一种新型的聚酯酰胺复合纳滤膜,该纳滤膜具有耐氯性好、亲水性强、抗污染能力强和溶质截留能力强的特点,且制备工艺简便温和,适于工业化生产。In the present invention, a novel polyester amide composite nanofiltration membrane is obtained through the interfacial polymerization reaction of serinol and polyacyl chlorides on the porous support layer under the catalysis of 4-dimethylaminopyridine. It has the characteristics of good chlorine, strong hydrophilicity, strong anti-pollution ability and strong solute interception ability, and the preparation process is simple and mild, which is suitable for industrial production.
附图说明Description of drawings
图1为丝氨醇分子结构式;Fig. 1 is serinol molecular structural formula;
图2为新型聚酯酰胺复合纳滤膜原子力显微镜形貌;Figure 2 is the atomic force microscope morphology of the novel polyester amide composite nanofiltration membrane;
图3为新型聚酯酰胺复合纳滤膜扫描电镜形貌;Figure 3 is the scanning electron microscope morphology of the novel polyester amide composite nanofiltration membrane;
图4为新型聚酯酰胺复合纳滤膜红外光谱。Figure 4 is the infrared spectrum of the novel polyester amide composite nanofiltration membrane.
具体实施方式detailed description
下面结合附图对本发明的技术方案作进一步的说明,但并不局限于此,凡是对本发明技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,均应涵盖在本发明的保护范围中。The technical solution of the present invention will be further described below in conjunction with the accompanying drawings, but it is not limited thereto. Any modification or equivalent replacement of the technical solution of the present invention without departing from the spirit and scope of the technical solution of the present invention should be covered by the present invention. within the scope of protection.
具体实施方式一:本实施方式提供了一种耐氯性强且抗污染的聚酯酰胺复合纳滤膜的制备方法,具体步骤如下:Embodiment 1: This embodiment provides a method for preparing a polyester amide composite nanofiltration membrane with strong chlorine resistance and anti-pollution, and the specific steps are as follows:
一、配制水相溶液:向纯水中加入2%(w/v)的丝氨醇(其结构式如图1所示),同时加入0.2%(w/v)的4-二甲氨基吡啶作为相转移和酰化催化剂,充分搅拌并溶解后采用三乙胺将溶液的pH值调至11.5;1. Preparation of aqueous phase solution: add 2% (w/v) serinol (its structural formula is shown in Figure 1) to pure water, and add 0.2% (w/v) 4-dimethylaminopyridine at the same time as Phase transfer and acylation catalyst, after fully stirring and dissolving, use triethylamine to adjust the pH value of the solution to 11.5;
二、配制有机相溶液:以正己烷为有机溶剂,向有机溶剂中加入0.1%(w/v)的多元酰氯;2. Prepare the organic phase solution: use n-hexane as the organic solvent, and add 0.1% (w/v) polyacyl chloride to the organic solvent;
三、以聚醚砜多孔超滤膜为支承层,首先将水相溶液倒向支撑层表面并浸泡2分钟,然后倒掉水相溶液并除去膜面多余水分,接着将有机相溶液倒向膜面,并反应60秒,反应结束后采用有机溶剂对膜面进行充分冲洗以去除未反应单体;3. With the polyethersulfone porous ultrafiltration membrane as the supporting layer, first pour the aqueous phase solution onto the surface of the supporting layer and soak for 2 minutes, then pour off the aqueous phase solution and remove excess water on the membrane surface, and then pour the organic phase solution onto the membrane surface, and react for 60 seconds. After the reaction, use an organic solvent to fully rinse the membrane surface to remove unreacted monomers;
四、将有机溶剂冲洗过后的膜放在50℃下热处理10分钟;4. Heat-treat the film after washing with organic solvent at 50°C for 10 minutes;
五、最后用纯水对膜进行充分清洗,由此获得聚酯酰胺复合纳滤膜。5. Finally, the membrane is fully washed with pure water to obtain a polyester amide composite nanofiltration membrane.
图2A给出了未进行反应的多孔支承层原子力显微镜形貌图,图2B则给出了界面聚合完成后得到的聚酯酰胺复合纳滤膜形貌图,由图2可知,通过以上反应步骤,成功地在较为光滑的支承层上形成了凹凸状的聚酯酰胺活性层。Figure 2A shows the topography of the porous support layer atomic force microscope without reaction, and Figure 2B shows the topography of the polyester amide composite nanofiltration membrane obtained after the interfacial polymerization is completed, as can be seen from Figure 2, through the above reaction steps , successfully formed a concave-convex polyester amide active layer on a relatively smooth support layer.
图3A和B分别为多孔支承层和聚酯酰胺复合纳滤膜的扫描电子显微镜形貌图,二者的对比同样证实了聚酯酰胺活性层的生成。此外,图3B还清楚地表明该聚酯酰胺复合纳滤膜表面具有类似于颗粒堆积的形貌特征,这与传统的聚酰胺复合纳滤膜明显不同。Figure 3A and B are scanning electron microscope topography images of the porous support layer and the polyester amide composite nanofiltration membrane, respectively, and the comparison between the two also confirms the formation of the polyester amide active layer. In addition, Figure 3B also clearly shows that the surface of the polyester amide composite nanofiltration membrane has a morphology similar to particle accumulation, which is obviously different from the traditional polyamide composite nanofiltration membrane.
图4则利用红外光谱从化学键的角度证实了反应后酯键和酰胺键的生成,从而进一步证实了聚酯酰胺活性层的生成。Figure 4 uses infrared spectroscopy to confirm the formation of ester bonds and amide bonds after the reaction from the perspective of chemical bonds, thereby further confirming the formation of the polyester amide active layer.
具体实施方式二:本实施方式提供了一种耐氯性强且抗污染的聚酯酰胺复合纳滤膜的制备方法,具体步骤如下:Specific embodiment two: This embodiment provides a preparation method of a polyester amide composite nanofiltration membrane with strong chlorine resistance and anti-pollution, and the specific steps are as follows:
一、配制水相溶液:向纯水中加入1%(w/v)的丝氨醇(其结构式如图1所示),同时加入0.2%(w/v)的4-二甲氨基吡啶作为相转移和酰化催化剂,充分搅拌并溶解后采用三乙胺将溶液的pH值调至11.5;1. Preparation of aqueous phase solution: add 1% (w/v) serinol (its structural formula is shown in Figure 1) to pure water, and add 0.2% (w/v) 4-dimethylaminopyridine at the same time as Phase transfer and acylation catalyst, after fully stirring and dissolving, use triethylamine to adjust the pH value of the solution to 11.5;
二、配制有机相溶液:以正辛烷为有机溶剂,向有机溶剂中加入0.05%(w/v)的多元酰氯;2. Prepare the organic phase solution: use n-octane as the organic solvent, and add 0.05% (w/v) polyacyl chloride to the organic solvent;
三、以聚砜多孔超滤膜为支承层,首先将水相溶液倒向支撑层表面并浸泡2分钟,然后倒掉水相溶液并除去膜面多余水分,接着将有机相溶液倒向膜面,并反应50秒,反应结束后采用有机溶剂对膜面进行充分冲洗以去除未反应单体;3. With the polysulfone porous ultrafiltration membrane as the supporting layer, first pour the aqueous phase solution on the surface of the supporting layer and soak for 2 minutes, then pour off the aqueous phase solution and remove excess water on the membrane surface, and then pour the organic phase solution on the membrane surface , and react for 50 seconds. After the reaction, use an organic solvent to fully rinse the membrane surface to remove unreacted monomers;
四、将有机溶剂冲洗过后的膜放在60℃下热处理15分钟;4. Heat-treat the film after rinsing with the organic solvent at 60°C for 15 minutes;
五、最后用纯水对膜进行充分清洗,由此获得聚酯酰胺复合纳滤膜。5. Finally, the membrane is fully washed with pure water to obtain a polyester amide composite nanofiltration membrane.
具体实施方式三:本实施方式提供了一种耐氯性强且抗污染的聚酯酰胺复合纳滤膜的制备方法,具体步骤如下:Specific embodiment three: This embodiment provides a preparation method of a polyester amide composite nanofiltration membrane with strong chlorine resistance and anti-pollution, and the specific steps are as follows:
一、配制水相溶液:向纯水中加入0.5%(w/v)的丝氨醇(其结构式如图1所示),同时加入0.05%(w/v)的4-二甲氨基吡啶作为相转移和酰化催化剂,充分搅拌并溶解后采用三乙胺将溶液的pH值调至11.5;1. Preparation of aqueous phase solution: add 0.5% (w/v) serinol (its structural formula is shown in Figure 1) to pure water, and add 0.05% (w/v) 4-dimethylaminopyridine at the same time as Phase transfer and acylation catalyst, after fully stirring and dissolving, use triethylamine to adjust the pH value of the solution to 11.5;
二、配制有机相溶液:以甲苯和环己烷为有机溶剂,二者体积比为1:1,向有机溶剂中加入0.05%(w/v)的多元酰氯;2. Prepare the organic phase solution: use toluene and cyclohexane as the organic solvent, the volume ratio of the two is 1:1, and add 0.05% (w/v) polyacyl chloride to the organic solvent;
三、以聚丙烯多孔超滤膜为支承层,首先将水相溶液倒向支撑层表面并浸泡4分钟,然后倒掉水相溶液并除去膜面多余水分,接着将有机相溶液倒向膜面,并反应70秒,反应结束后采用有机溶剂对膜面进行充分冲洗以去除未反应单体;3. With polypropylene porous ultrafiltration membrane as the supporting layer, first pour the aqueous phase solution on the surface of the supporting layer and soak for 4 minutes, then pour off the aqueous phase solution and remove excess water on the membrane surface, and then pour the organic phase solution on the membrane surface , and react for 70 seconds. After the reaction, use an organic solvent to fully rinse the membrane surface to remove unreacted monomers;
四、将有机溶剂冲洗过后的膜放在70℃下热处理15分钟;4. Heat the film after washing with organic solvent at 70°C for 15 minutes;
五、最后用纯水对膜进行充分清洗,由此获得聚酯酰胺复合纳滤膜。5. Finally, the membrane is fully washed with pure water to obtain a polyester amide composite nanofiltration membrane.
具体实施方式四:本实施方式提供了一种耐氯性强且抗污染的聚酯酰胺复合纳滤膜的制备方法,具体步骤如下:Specific embodiment four: This embodiment provides a preparation method of a polyester amide composite nanofiltration membrane with strong chlorine resistance and anti-pollution, and the specific steps are as follows:
一、配制水相溶液:向纯水中加入1.5%(w/v)的丝氨醇(其结构式如图1所示),同时加入0.15%(w/v)的4-二甲氨基吡啶作为相转移和酰化催化剂,充分搅拌并溶解后采用三乙胺将溶液的pH值调至11.5;1. Preparation of aqueous phase solution: add 1.5% (w/v) serinol (its structural formula is shown in Figure 1) to pure water, and add 0.15% (w/v) 4-dimethylaminopyridine at the same time as Phase transfer and acylation catalyst, after fully stirring and dissolving, use triethylamine to adjust the pH value of the solution to 11.5;
二、配制有机相溶液:以正辛烷为有机溶剂,向有机溶剂中加入0.07%(w/v)的多元酰氯;2. Prepare the organic phase solution: use n-octane as the organic solvent, and add 0.07% (w/v) polyacyl chloride to the organic solvent;
三、以磺化聚醚砜多孔超滤膜为支承层,首先将水相溶液倒向支撑层表面并浸泡3分钟,然后倒掉水相溶液并除去膜面多余水分,接着将有机相溶液倒向膜面,并反应60秒,反应结束后采用有机溶剂对膜面进行充分冲洗以去除未反应单体;3. With the sulfonated polyethersulfone porous ultrafiltration membrane as the supporting layer, first pour the aqueous phase solution on the surface of the supporting layer and soak for 3 minutes, then pour off the aqueous phase solution and remove excess water on the membrane surface, and then pour the organic phase solution Facing the membrane surface and reacting for 60 seconds, after the reaction, use an organic solvent to fully rinse the membrane surface to remove unreacted monomers;
四、将有机溶剂冲洗过后的膜放在80℃下热处理15分钟;4. Heat-treat the film after washing with organic solvent at 80°C for 15 minutes;
五、最后用纯水对膜进行充分清洗,由此获得聚酯酰胺复合纳滤膜。5. Finally, the membrane is fully washed with pure water to obtain a polyester amide composite nanofiltration membrane.
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