CN108246122B - Method for synthesizing NaA molecular sieve membrane - Google Patents
Method for synthesizing NaA molecular sieve membrane Download PDFInfo
- Publication number
- CN108246122B CN108246122B CN201810178837.3A CN201810178837A CN108246122B CN 108246122 B CN108246122 B CN 108246122B CN 201810178837 A CN201810178837 A CN 201810178837A CN 108246122 B CN108246122 B CN 108246122B
- Authority
- CN
- China
- Prior art keywords
- molecular sieve
- naa molecular
- seed
- source
- naa
- 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.)
- Active
Links
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 110
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 110
- 239000012528 membrane Substances 0.000 title claims abstract description 67
- 238000000034 method Methods 0.000 title claims abstract description 29
- 230000002194 synthesizing effect Effects 0.000 title abstract 2
- 239000013078 crystal Substances 0.000 claims abstract description 65
- 239000007788 liquid Substances 0.000 claims abstract description 41
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 39
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000001548 drop coating Methods 0.000 claims abstract description 22
- 230000012010 growth Effects 0.000 claims abstract description 21
- 238000002360 preparation method Methods 0.000 claims abstract description 18
- 230000008025 crystallization Effects 0.000 claims abstract description 8
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 6
- 238000005216 hydrothermal crystallization Methods 0.000 claims abstract description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 81
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 49
- 239000011734 sodium Substances 0.000 claims description 35
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 30
- 238000006243 chemical reaction Methods 0.000 claims description 30
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 22
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 18
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 17
- 229910052708 sodium Inorganic materials 0.000 claims description 17
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 16
- 238000010189 synthetic method Methods 0.000 claims description 16
- 239000002245 particle Substances 0.000 claims description 13
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 11
- 229910052710 silicon Inorganic materials 0.000 claims description 11
- 239000010703 silicon Substances 0.000 claims description 11
- 239000003513 alkali Substances 0.000 claims description 10
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 10
- 229910052782 aluminium Inorganic materials 0.000 claims description 10
- 230000007935 neutral effect Effects 0.000 claims description 10
- 238000002425 crystallisation Methods 0.000 claims description 7
- 238000009826 distribution Methods 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 7
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 3
- 238000001308 synthesis method Methods 0.000 claims description 3
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims 1
- 235000012239 silicon dioxide Nutrition 0.000 claims 1
- 238000000926 separation method Methods 0.000 abstract description 14
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000008367 deionised water Substances 0.000 description 28
- 229910021641 deionized water Inorganic materials 0.000 description 28
- 238000003756 stirring Methods 0.000 description 25
- 238000000576 coating method Methods 0.000 description 11
- 239000011248 coating agent Substances 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 8
- 238000001000 micrograph Methods 0.000 description 7
- -1 polytetrafluoroethylene Polymers 0.000 description 7
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 7
- 239000004810 polytetrafluoroethylene Substances 0.000 description 7
- 239000000843 powder Substances 0.000 description 7
- 229910001220 stainless steel Inorganic materials 0.000 description 7
- 239000010935 stainless steel Substances 0.000 description 7
- 239000008399 tap water Substances 0.000 description 7
- 235000020679 tap water Nutrition 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000001878 scanning electron micrograph Methods 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- 238000007598 dipping method Methods 0.000 description 3
- 238000011065 in-situ storage Methods 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- 230000034655 secondary growth Effects 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 244000137852 Petrea volubilis Species 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical group [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 238000009827 uniform distribution Methods 0.000 description 2
- 239000004115 Sodium Silicate Substances 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 230000003698 anagen phase Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010335 hydrothermal treatment Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000005373 pervaporation Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 238000001338 self-assembly Methods 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000001771 vacuum deposition Methods 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000011041 water permeability test Methods 0.000 description 1
Images
Classifications
-
- 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
- B01D71/02—Inorganic material
- B01D71/028—Molecular sieves
-
- 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
- B01D67/0039—Inorganic membrane manufacture
-
- 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
- B01D2325/00—Details relating to properties of membranes
- B01D2325/36—Hydrophilic membranes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
本发明公开了一种NaA分子筛膜的合成方法,具体步骤为:1)支撑体表面的预处理;2)支撑体表面晶种层的制备;将NaA分子筛晶种分散在乙醇中,得晶种液,采用滴涂的方法将晶种液涂覆在预处理好的支撑体表面,烘干得表面附着晶种层的支撑体;3)NaA分子筛膜的制备:置于NaA分子筛膜生长液中,加热进行水热反应进行晶化制得NaA分子筛膜。本发明涉及的制备方法简单可行,适合于批量生产;采用滴涂的方法,能够在亲水性不是很好的氧化铝支撑体上生成致密性、平整度好的NaA分子筛膜,其可重复性高,分离性能好,适合推广应用。The invention discloses a method for synthesizing a NaA molecular sieve membrane. The specific steps are: 1) pretreatment on the surface of a support body; 2) preparation of a seed layer on the surface of the support body; dispersing the NaA molecular sieve crystal seeds in ethanol to obtain the crystal seeds 3) Preparation of NaA molecular sieve film: placed in NaA molecular sieve film growth liquid , heating for hydrothermal reaction and crystallization to obtain NaA molecular sieve membrane. The preparation method involved in the invention is simple and feasible, and is suitable for mass production; by adopting the drop coating method, a NaA molecular sieve membrane with good compactness and good flatness can be formed on the alumina support body with poor hydrophilicity, and the repeatability is High, good separation performance, suitable for popularization and application.
Description
技术领域technical field
本发明属于分子筛膜制备技术领域,具体涉及一种NaA分子筛膜的合成方法。The invention belongs to the technical field of molecular sieve membrane preparation, in particular to a synthesis method of NaA molecular sieve membrane.
背景技术Background technique
据统计,工业上的能源消耗约占总能源消耗的32%,而这些能量大部分应用在了物质分离方向。现有的分离技术包括精馏、萃取、吸附、重结晶等,其中应用最广泛的是精馏,此过程中,需要不断地重复汽化和冷凝,这需要大量的能源消耗,并且精馏在其他能量利用方面存在很多低效率情况。而膜分离技术与这些传统分离技术相比,具有能量消耗低、污染少、易于实现连续分离、易于与其他分离过程耦合、使用条件温和、易于放大等优点,在很多工业领域的应用越来越广泛。According to statistics, industrial energy consumption accounts for about 32% of the total energy consumption, and most of this energy is used in the direction of material separation. Existing separation technologies include rectification, extraction, adsorption, recrystallization, etc. Among them, rectification is the most widely used. In this process, repeated vaporization and condensation are required, which requires a lot of energy consumption, and rectification is used in other There are many inefficiencies in energy utilization. Compared with these traditional separation technologies, membrane separation technology has the advantages of low energy consumption, less pollution, easy to achieve continuous separation, easy coupling with other separation processes, mild conditions of use, and easy amplification. widely.
膜分离技术的关键在于膜组件,主要分为有机膜、无机膜和生物膜。无机膜较有机膜相比,具有机械强度高、耐化学腐蚀强、耐高温、不容易老化等优点,得到了广泛的应用。而NaA分子筛膜作为无机膜的一种,除具备了无机膜的优点外,同时由于其有效孔径为0.41nm,硅铝比为1等特点,使其成为目前人工合成的最具亲水性的分子筛,并且它在有机溶剂脱水,尤其是在醇水共沸物体系等的脱水领域具有优异的分离效果。近年来能源短缺,燃料乙醇拥有了很大的发展前景,无水乙醇的制备一般采用精馏的方法,但是当水含量较少时,产生恒沸物,很难得到100%乙醇,若把NaA分子筛膜应用到渗透蒸发分离技术中,将会推动燃料乙醇的应用。The key to membrane separation technology lies in membrane components, which are mainly divided into organic membranes, inorganic membranes and biological membranes. Compared with organic films, inorganic films have the advantages of high mechanical strength, strong chemical corrosion resistance, high temperature resistance, and not easy to age, and have been widely used. As a kind of inorganic membrane, NaA molecular sieve membrane not only has the advantages of inorganic membrane, but also has the characteristics of effective pore size of 0.41nm and silicon-aluminum ratio of 1, making it the most hydrophilic synthetic membrane at present. Molecular sieve, and it has excellent separation effect in the dehydration of organic solvents, especially in the field of dehydration of alcohol-water azeotrope systems. In recent years, there is a shortage of energy, and fuel ethanol has great development prospects. The preparation of anhydrous ethanol generally adopts the method of rectification, but when the water content is small, azeotropes are generated, and it is difficult to obtain 100% ethanol. The application of molecular sieve membrane to pervaporation separation technology will promote the application of fuel ethanol.
目前NaA分子筛膜的合成方法主要包括原位合成法、二次生长法、微波加热合成法、蒸汽相转化法等。原位水热合成法简单易于操作,但是这种制膜方法对膜的厚度,晶粒的大小都不容易控制,且膜表面容易凹凸不平、出现裂纹等问题,对膜的分离性能和通量都产生较大的影响。目前应用最广泛的是二次生长法,这种方法把晶体的生长期和成核期分开,首先在支撑体表面涂覆一层晶种,用来作为原位水热合成过程中的晶核,当在合成液体系中进行水热反应时,作为生长中心,这样缩短了膜的晶化时间,对于膜的厚度,杂晶的生成,都起到了一定的控制作用;其中,支撑体表面的涂晶步骤对所得NaA分子筛膜的质量具有重要的影响。At present, the synthesis methods of NaA molecular sieve membranes mainly include in-situ synthesis, secondary growth, microwave heating synthesis, and vapor phase inversion. The in-situ hydrothermal synthesis method is simple and easy to operate, but this method of membrane production is not easy to control the thickness of the membrane and the size of the grains, and the membrane surface is prone to unevenness and cracks. have a greater impact. At present, the most widely used method is the secondary growth method. This method separates the growth phase and the nucleation phase of the crystal. First, a layer of seed crystals is coated on the surface of the support, which is used as the crystal nucleus in the in-situ hydrothermal synthesis process. , when the hydrothermal reaction is carried out in the synthesis liquid system, it acts as the growth center, which shortens the crystallization time of the film, and plays a certain role in controlling the thickness of the film and the formation of miscellaneous crystals; The coating step has an important influence on the quality of the obtained NaA molecular sieve membrane.
目前,涂晶的方法有很多,如热浸渍法、真空涂晶法、擦涂法等。其中应用最广泛的热浸渍法,通过把支撑体进行热处理后内部形成热空气,在浸入晶种液时急剧冷却形成负压,在压差的推动下,使晶种吸附在支撑体的表面形成晶种层;在此过程涂覆时间短,晶种分布不够均匀,即使多次重复涂晶也不能完全覆盖载体表面。其他几种涂覆方法也都很难实现晶种在支撑体上均匀分布。晶种涂覆的好坏,对NaA分子筛膜的厚度,均匀度,还有致密性等具有较大的影响,从而影响膜的性能。At present, there are many methods of coating crystal, such as hot dipping method, vacuum coating method, wipe coating method, etc. Among them, the most widely used hot dipping method is to form hot air inside the support body after heat treatment, and rapidly cool to form a negative pressure when immersed in the seed liquid. Seed layer: In this process, the coating time is short, the distribution of the seeds is not uniform enough, and the surface of the carrier cannot be completely covered even if the coating is repeated for many times. Several other coating methods are also difficult to achieve uniform distribution of seeds on the support. The quality of seed coating has a great influence on the thickness, uniformity and compactness of NaA molecular sieve membrane, thus affecting the performance of the membrane.
发明内容SUMMARY OF THE INVENTION
本发明要解决的技术问题是针对现有NaA分子筛膜二次生长法制备过程中存在的晶种分布不均匀和致密性低等问题,提供一种通过滴涂法,将晶种均匀、致密的涂覆于亲水性不是很好的支撑体上,并通过水热反应制备致密、平整的分子筛膜的合成工艺,所得分子筛膜分离性能高、渗透通量大,且涉及的制备工艺简单便捷,重复性高,适合推广应用。The technical problem to be solved by the present invention is to solve the problems of uneven distribution of crystal seeds and low compactness existing in the preparation process of the existing NaA molecular sieve film secondary growth method, and to provide a method for uniform and dense seed crystals through a drop coating method. The synthetic process of coating on a support body with poor hydrophilicity and preparing a dense and smooth molecular sieve membrane through hydrothermal reaction, the obtained molecular sieve membrane has high separation performance and large permeation flux, and the involved preparation process is simple and convenient, High repeatability, suitable for promotion and application.
为实现上述目的,本发明采用的技术方案为:To achieve the above object, the technical scheme adopted in the present invention is:
一种NaA分子筛膜的合成方法,其特征在于,包括以下步骤:A kind of synthetic method of NaA molecular sieve membrane, is characterized in that, comprises the following steps:
1)支撑体表面的预处理;对氧化铝板进行打磨,置于水中进行超声震荡清洗,然后依次浸泡于盐酸溶液和氢氧化钠溶液中,再超声震荡水洗至中性,干燥,取出备用;1) Pretreatment of the surface of the support body; the alumina plate is polished, placed in water for ultrasonic vibration cleaning, then immersed in hydrochloric acid solution and sodium hydroxide solution in turn, then ultrasonically washed with water to neutrality, dried, and taken out for use;
2)支撑体表面晶种层的制备;将硅源、铝源、碱源和水混合搅拌均匀,置于反应釜中进行晶化处理,然后进行抽滤、干燥,制得NaA分子筛晶种;将NaA分子筛晶种溶于乙醇溶液中,制得晶种液,采用滴涂法,将晶种液涂覆于经步骤1)预处理的氧化铝板的表面,烘干得表面覆盖晶种层的支撑体;2) Preparation of the crystal seed layer on the surface of the support; the silicon source, the aluminum source, the alkali source and the water are mixed and stirred uniformly, placed in the reaction kettle for crystallization, and then suction filtered and dried to obtain the NaA molecular sieve crystal seed; The NaA molecular sieve crystal seeds are dissolved in the ethanol solution to prepare the seed crystal liquid, and the drop coating method is used to coat the seed crystal liquid on the surface of the alumina plate pretreated in step 1), and dry to obtain a surface covered with the seed crystal layer. support body;
3)NaA分子筛膜的制备;将硅源、铝源、碱源和水混合搅拌均匀,得NaA分子筛膜生长液;将步骤2)所得表面覆盖晶种层的支撑体浸渍于装有NaA分子筛膜生长液的反应釜中进行水热晶化,反应结束后急速冷却,进行水洗、烘干,即在氧化铝板上制得NaA分子筛膜。3) Preparation of NaA molecular sieve membrane; the silicon source, aluminum source, alkali source and water are mixed and stirred evenly to obtain a NaA molecular sieve membrane growth solution; the support body covered with the seed layer on the surface obtained in step 2) is immersed in a NaA molecular sieve membrane The hydrothermal crystallization is carried out in the reaction kettle of the growth liquid, and after the reaction is completed, it is rapidly cooled, washed with water, and dried to obtain a NaA molecular sieve film on the alumina plate.
上述方案中,步骤1)中所述打磨步骤采用砂纸进行打磨,砂纸型号优选为800#和1200#。In the above scheme, the grinding step described in step 1) is carried out with sandpaper, and the sandpaper model is preferably 800# and 1200#.
上述方案中,步骤1)中所述盐酸和氢氧化钠浓度为0.5-4mol/L。In the above scheme, the concentration of hydrochloric acid and sodium hydroxide described in step 1) is 0.5-4mol/L.
上述方案中,步骤1)中所述干燥温度为50-80℃,干燥时间为10-24h。In the above scheme, the drying temperature in step 1) is 50-80° C., and the drying time is 10-24 h.
上述方案中,所述步骤2)和步骤3)中所述铝源为氯化铝、氢氧化铝、偏铝酸钠中的一种;硅源为水玻璃、硅酸钠、硅溶胶、二氧化硅中的一种;碱源为氢氧化钠。In the above scheme, the aluminum source described in the step 2) and the step 3) is one of aluminum chloride, aluminum hydroxide, and sodium metaaluminate; the silicon source is water glass, sodium silicate, silica sol, two A kind of silicon oxide; the alkali source is sodium hydroxide.
上述方案中,步骤2)和步骤3)中所述碱源、硅源和铝源的添加量分别以其引入的Na2O、SiO2和Al2O3为准,碱源、硅源、铝源和水的摩尔比按Al2O3:Na2O:SiO2:H2O计为1:(0.5~3):(1~3):(100~200)。In the above scheme, the addition amounts of the alkali source, silicon source and aluminum source described in step 2) and step 3) are respectively the Na 2 O, SiO 2 and Al 2 O 3 introduced by them, and the alkali source, silicon source, The molar ratio of the aluminum source and water is calculated as Al 2 O 3 :Na 2 O:SiO 2 :H 2 O as 1:(0.5-3):(1-3):(100-200).
上述方案中,步骤2)所的NaA分子筛晶种的平均粒径为1~5μm。In the above scheme, the average particle size of the NaA molecular sieve seeds in step 2) is 1-5 μm.
上述方案中,所述晶种液中NaA分子筛晶种的浓度为2~5g/L。In the above scheme, the concentration of NaA molecular sieve seeds in the seed liquid is 2-5 g/L.
优选的,所述晶种液中NaA分子筛晶种的浓度为3~4g/L。Preferably, the concentration of NaA molecular sieve seeds in the seed solution is 3-4 g/L.
上述方案中,所述滴涂法将晶种液逐滴滴加至支撑体表面直至晶种液完全覆盖支撑体,滴加速度为30~60滴/min。In the above solution, in the drop coating method, the seed liquid is added dropwise to the surface of the support until the seed liquid completely covers the support, and the dropping rate is 30-60 drops/min.
优选的,所述滴涂高度为0.5~10cm;注射器直径为0.2~1cm。Preferably, the drop coating height is 0.5-10 cm; the diameter of the syringe is 0.2-1 cm.
优选的,支撑体表面对应的滴涂量为0.5~1ml/cm2。Preferably, the drop coating amount corresponding to the surface of the support is 0.5-1 ml/cm 2 .
更优选的,每一个滴涂点(注射器滴入位置)对应的支撑体表面滴涂面积为1cm2以下。More preferably, the drop-coating area on the surface of the support corresponding to each drop-coating point (drop-in position of the syringe) is 1 cm 2 or less.
上述方案中,所述支撑体把没有覆盖晶种层的一面采用不影响晶化反应的材料(优选为聚四氟乙烯胶纸)进行包裹保护,再置于NaA分子筛膜生长液中进行水热合成晶化处理。In the above-mentioned scheme, the support body uses the material (preferably polytetrafluoroethylene tape) that does not affect the crystallization reaction to wrap and protect the side that does not cover the seed layer, and then is placed in the NaA molecular sieve film growth solution for hydrothermal treatment. Synthetic crystallization treatment.
上述方案中,步骤2)中所述烘干温度为50~100℃。In the above scheme, the drying temperature in step 2) is 50-100°C.
优选的,步骤2)中所述烘干时间为2~3h。Preferably, the drying time in step 2) is 2-3h.
上述方案中,步骤2)和步骤3)中所述混合搅拌的搅拌速度为60~500r/min,搅拌时间3~5h,搅拌温度为室温条件。In the above scheme, the stirring speed of the mixing and stirring described in step 2) and step 3) is 60~500r/min, the stirring time is 3~5h, and the stirring temperature is room temperature.
上述方案中,所述水热晶化温度为60~120℃,时间为1~6h。In the above scheme, the hydrothermal crystallization temperature is 60-120° C., and the time is 1-6 h.
上述方案中,所述氧化铝板由氧化铝颗粒压制而成,氧化铝颗粒的尺寸范围为10~30μm,颗粒之间形成的孔径分布范围为0.5-1μm。In the above solution, the alumina plate is formed by pressing alumina particles, the size of the alumina particles is in the range of 10-30 μm, and the pore size distribution formed between the particles is in the range of 0.5-1 μm.
优选的,采用的氧化铝板表面的等效直径为1~10cm。Preferably, the equivalent diameter of the surface of the alumina plate used is 1-10 cm.
本发明的原理为:采用滴涂的方法,将NaA晶种液滴到支撑体上,当液滴遇到支撑体时,液体有铺展的趋势,随着不断地滴涂,晶种液将支撑体完全覆盖,形成一层溶液层;在适宜的温度下(滴涂后的烘干温度),NaA颗粒在乙醇中发生自组装过程,自发形成有序结构,并平整地排列在一起,随着乙醇的蒸发,最终形成均匀的晶种层。The principle of the present invention is as follows: using the method of drip coating, drop the NaA seed crystal on the support body, when the droplet encounters the support body, the liquid has a tendency to spread, and with the continuous drip coating, the seed crystal liquid will support The body is completely covered to form a layer of solution; at a suitable temperature (drying temperature after drop coating), the NaA particles undergo a self-assembly process in ethanol, spontaneously form an ordered structure, and are evenly arranged together. The evaporation of ethanol eventually forms a uniform seed layer.
本发明的有益效果为:The beneficial effects of the present invention are:
1)本发明首次提出采用滴涂法,通过支撑体表面的预处理、调控晶种液和烘干条件,在亲水性不是很好的支撑体上得到均匀、致密的NaA分子筛晶种层,并进行进一步晶化制备得到NaA分子筛膜;该方法简单便捷、易于操作,重复性好,弥补了其他涂晶方法受亲水性限制的问题,适合推广应用。1) The present invention proposes for the first time that a drop coating method is adopted to obtain a uniform and dense NaA molecular sieve seed layer on a support whose hydrophilicity is not very good through pretreatment of the surface of the support, regulation of the seed liquid and drying conditions, The NaA molecular sieve membrane is prepared by further crystallization; the method is simple, convenient, easy to operate, and has good repeatability, which makes up for the problem that other coating methods are limited by hydrophilicity, and is suitable for popularization and application.
2)本发明采用的晶种分散剂是乙醇,乙醇的蒸发速度、乙醇极性与NaA颗粒之间的相互作用,是促进晶种层平整、均匀分布的重要因素。2) The crystal seed dispersant used in the present invention is ethanol, and the interaction between the evaporation speed of ethanol, the polarity of ethanol and the NaA particles is an important factor for promoting the smooth and uniform distribution of the seed crystal layer.
3)本发明所得NaA分子筛膜平整紧密,具有较高的渗透性能和分离性能,具有较高的工业应用价值。3) The NaA molecular sieve membrane obtained by the present invention is flat and compact, has high permeability and separation performance, and has high industrial application value.
附图说明Description of drawings
图1为本发明实施例1所得NaA分子筛晶种层的扫描电镜图。1 is a scanning electron microscope image of the NaA molecular sieve seed layer obtained in Example 1 of the present invention.
图2为本发明实施例2所得NaA分子筛膜的扫描电镜图。2 is a scanning electron microscope image of the NaA molecular sieve membrane obtained in Example 2 of the present invention.
图3为本发明实施例2所得NaA分子筛膜和X射线衍射图Fig. 3 is the NaA molecular sieve membrane and X-ray diffractogram obtained in Example 2 of the present invention
图4为本发明实施例3所得NaA分子筛膜的扫描电镜图。4 is a scanning electron microscope image of the NaA molecular sieve membrane obtained in Example 3 of the present invention.
图5为本发明实施例4所得NaA分子筛膜的扫描电镜图。5 is a scanning electron microscope image of the NaA molecular sieve membrane obtained in Example 4 of the present invention.
图6为对比例1所得NaA分子筛膜的扫描电镜图。6 is a scanning electron microscope image of the NaA molecular sieve membrane obtained in Comparative Example 1.
图7为对比例2所得NaA分子筛晶种层的扫描电镜图。7 is a scanning electron microscope image of the NaA molecular sieve seed layer obtained in Comparative Example 2.
图8为对比例3所得NaA分子筛晶种层的扫描电镜图。8 is a scanning electron microscope image of the NaA molecular sieve seed layer obtained in Comparative Example 3.
具体实施方式Detailed ways
为了更好的理解本发明,下面结合具体实施例和附图进一步阐明本发明的内容,但本发明的内容不仅仅局限于下面的实施例。In order to better understand the present invention, the content of the present invention is further explained below with reference to specific embodiments and accompanying drawings, but the content of the present invention is not limited to the following embodiments.
以下实施例中,所述氧化铝板(α-Al2O3板)为由大颗粒氧化铝(10~30μm)压制形成的圆形支撑体,颗粒之间形成的孔径分布范围为0.5-1μm;氧化铝板的直径为1~3cm。In the following examples, the alumina plate (α-Al 2 O 3 plate) is a circular support formed by pressing large-particle alumina (10-30 μm), and the pore size distribution between the particles is 0.5-1 μm; The diameter of the alumina plate is 1 to 3 cm.
实施例1Example 1
一种NaA分子筛膜的合成方法,其制备方法包括如下步骤:A kind of synthetic method of NaA molecular sieve membrane, its preparation method comprises the steps:
1)依次用800#和1200#的砂纸对α-Al2O3板(直径1cm)进行打磨,置于水中进行超声震荡洗掉残留的粉末,依次在2mol/L的盐酸和氢氧化钠溶液分别浸泡24h,再超声震荡15min用去离子水洗至中性,并置于60℃烘箱中干燥12h,取出备用;1) Use 800# and 1200# sandpaper in turn to polish the α-Al 2 O 3 plate (diameter 1cm), place it in water and carry out ultrasonic vibration to wash off the residual powder, and then add 2mol/L hydrochloric acid and sodium hydroxide solution in turn. Soak for 24 hours, then ultrasonically shake for 15 minutes, wash with deionized water until neutral, and place them in a 60°C oven to dry for 12 hours, then take them out for use;
2)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温混合搅拌3h(搅拌速率300r/min),装入不锈钢反应釜中,在100℃条件下反应4h,抽滤,烘干(80℃),制得NaA分子筛晶种;将所得NaA分子筛晶种溶于乙醇中搅拌均匀,配制3g/L晶种液,用直径为0.3cm的注射器取配制好的晶种液,以距离α-Al2O3板表面圆心1cm高处为滴涂中心,以大约1滴/秒的速度将晶种液滴涂在氧化铝板上(支撑体表面对应的滴涂量为0.5~1ml/cm2),使晶种液完全覆盖在支撑体表面,80℃条件下烘2.5h,得表面覆盖晶种层的支撑体,备用;2) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, mixed and stirred at room temperature for 3h (stirring rate 300r/min), put into a stainless steel reaction kettle, reacted at 100°C for 4h, suction filtered, and dried (80°C) to obtain NaA molecular sieve seeds Dissolve the gained NaA molecular sieve crystal seeds in ethanol and stir evenly, prepare 3g/L seed crystal liquid, take the prepared seed crystal liquid with a syringe with a diameter of 0.3cm, and take the distance α-Al 2 O 3 plate surface circle center 1cm high At the center of the drop coating, apply the seed crystal droplet on the alumina plate at a speed of about 1 drop/second (the drop coating amount corresponding to the surface of the support body is 0.5-1ml/cm 2 ), so that the seed crystal solution completely covers the support. The surface of the body was baked at 80°C for 2.5 hours to obtain a support body covered with a seed layer, which was used for later use;
3)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温搅拌3h(搅拌速率300r/min),制得分子筛膜生长液,将所得表面覆盖晶种层的支撑体用聚四氟乙烯胶纸包裹背面(无晶种层的一面),放入盛有分子筛膜生长液的反应釜中,在100℃条件下反应3h,反应结束后用自来水冲洗急速冷却,将支撑体取出,用去离子水洗涤至中性并烘干,得到NaA分子筛膜。3) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, stirred at room temperature for 3h (stirring rate 300r/min) to obtain a molecular sieve film growth solution, and the back surface of the support whose surface was covered with the seed layer was wrapped with polytetrafluoroethylene tape (without the seed layer) one side), put it into the reaction kettle filled with molecular sieve film growth liquid, react at 100 ° C for 3 hours, rinse with tap water and rapidly cool after the reaction, take out the support, wash with deionized water to neutrality and dry, A NaA molecular sieve membrane was obtained.
图1为本实施例所得NaA分子筛晶种层不同放大倍数下的SEM,可以看出,NaA晶种在支撑体的表面分布均匀、平整;平均粒径约为1.5~2μm。Fig. 1 is the SEM under different magnifications of the NaA molecular sieve seed layer obtained in the present embodiment. It can be seen that the NaA seeds are distributed evenly and flat on the surface of the support body; the average particle size is about 1.5-2 μm.
实施例2Example 2
一种NaA分子筛膜的合成方法,其制备方法包括如下步骤:A kind of synthetic method of NaA molecular sieve membrane, its preparation method comprises the steps:
1)依次用800#和1200#的砂纸对α-Al2O3板(直径1cm)进行打磨,置于水中进行超声震荡洗掉残留的粉末,依次在2mol/L的盐酸和氢氧化钠溶液分别浸泡24h,再超声震荡15min用去离子水洗至中性,并置于60℃烘箱中干燥12h,取出备用;1) Use 800# and 1200# sandpaper in turn to polish the α-Al 2 O 3 plate (diameter 1cm), place it in water and carry out ultrasonic vibration to wash off the residual powder, and then add 2mol/L hydrochloric acid and sodium hydroxide solution in turn. Soak for 24 hours, then ultrasonically shake for 15 minutes, wash with deionized water until neutral, and place them in a 60°C oven to dry for 12 hours, then take them out for use;
2)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:150计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温混合搅拌3h(搅拌速率500r/min),装入不锈钢反应釜中,在100℃条件下反应4h,抽滤,烘干(80℃),制得NaA分子筛晶种;将所得NaA分子筛晶种溶于乙醇中搅拌均匀,配制3g/L晶种液,用直径为0.3cm的注射器取配制好的晶种液,以距离α-Al2O3板表面圆心1cm高处为滴涂中心,以大约1滴/秒的速度将晶种液滴涂在氧化铝板上(支撑体表面对应的滴涂量为0.5~1ml/cm2),使晶种液完全覆盖在支撑体表面,80℃条件下烘2.5h,得表面覆盖晶种层的支撑体,备用;2) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:150, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, mixed and stirred at room temperature for 3h (stirring rate 500r/min), put into a stainless steel reaction kettle, reacted at 100°C for 4h, suction filtered, and dried (80°C) to obtain NaA molecular sieve seeds Dissolve the gained NaA molecular sieve crystal seeds in ethanol and stir evenly, prepare 3g/L seed crystal liquid, take the prepared seed crystal liquid with a syringe with a diameter of 0.3cm, and take the distance α-Al 2 O 3 plate surface circle center 1cm high At the center of the drop coating, apply the seed crystal droplet on the alumina plate at a speed of about 1 drop/second (the drop coating amount corresponding to the surface of the support body is 0.5-1ml/cm 2 ), so that the seed crystal solution completely covers the support. The surface of the body was baked at 80°C for 2.5 hours to obtain a support body covered with a seed layer, which was used for later use;
3)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:150计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温搅拌3h(搅拌速率500r/min),制得分子筛膜生长液,将所得表面覆盖晶种层的支撑体用聚四氟乙烯胶纸包裹背面(无晶种层的一面),放入盛有分子筛膜生长液的反应釜中,在120℃条件下反应3h,反应结束后用自来水冲洗急速冷却,将支撑体取出,用去离子水洗涤至中性并烘干,得到NaA分子筛膜。3) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:150, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, stirred at room temperature for 3h (stirring rate 500r/min) to obtain a molecular sieve film growth solution, and the back surface of the support whose surface was covered with the seed layer was wrapped with polytetrafluoroethylene tape (without the seed layer) one side), put it into the reaction kettle filled with the molecular sieve film growth solution, react at 120 ° C for 3 hours, rinse with tap water and rapidly cool after the reaction, take out the support, wash with deionized water to neutrality and dry, A NaA molecular sieve membrane was obtained.
图2和图3分别为本实施例所得NaA分子筛膜的SEM图和XRD图。从图2中可以看出在氧化铝板上生成了致密、平整的NaA分子筛膜,并且侧面图显示NaA分子筛膜与氧化铝板之间结合紧密,未见脱离处。图3中XRD图谱显示滴涂法已将NaA分子筛晶种成功涂覆于氧化铝板上并生成NaA分子筛膜。FIG. 2 and FIG. 3 are the SEM image and the XRD image of the NaA molecular sieve membrane obtained in this example, respectively. It can be seen from Figure 2 that a dense and flat NaA molecular sieve membrane is formed on the alumina plate, and the side view shows that the NaA molecular sieve membrane and the alumina plate are tightly bound, and there is no separation. The XRD pattern in Figure 3 shows that the NaA molecular sieve seed crystals have been successfully coated on the alumina plate by the drop coating method and a NaA molecular sieve film is formed.
实施例3Example 3
一种NaA分子筛膜的合成方法,其制备方法包括如下步骤:A kind of synthetic method of NaA molecular sieve membrane, its preparation method comprises the steps:
1)依次用800#和1200#的砂纸对α-Al2O3板(直径3cm)进行打磨,置于水中进行超声震荡洗掉残留的粉末,依次在2mol/L的盐酸和氢氧化钠溶液分别浸泡24h,再超声震荡15min用去离子水洗至中性,并置于60℃烘箱中干燥12h,取出备用;1) Use 800# and 1200# sandpapers in turn to polish the α-Al 2 O 3 plate (diameter 3cm), place it in water and carry out ultrasonic vibration to wash off the residual powder, and then add 2mol/L hydrochloric acid and sodium hydroxide solution in turn. Soak for 24 hours, then ultrasonically shake for 15 minutes, wash with deionized water until neutral, and place them in a 60°C oven to dry for 12 hours, then take them out for use;
2)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温混合搅拌3h(搅拌速率300r/min),装入不锈钢反应釜中,在100℃条件下反应4h,抽滤,烘干(80℃),制得NaA分子筛晶种;将所得NaA分子筛晶种溶于乙醇中搅拌均匀,配制3g/L晶种液,用直径为0.3cm的注射器取配制好的晶种液,以距离α-Al2O3板表面圆心2cm高处为滴涂中心,以大约1滴/秒的速度将晶种液滴涂在氧化铝板上(支撑体表面对应的滴涂量为0.5~1ml/cm2),使晶种液完全覆盖在支撑体表面,80℃条件下烘2.5h,得表面覆盖晶种层的支撑体,备用;2) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, mixed and stirred at room temperature for 3h (stirring rate 300r/min), put into a stainless steel reaction kettle, reacted at 100°C for 4h, suction filtered, and dried (80°C) to obtain NaA molecular sieve seeds Dissolve the gained NaA molecular sieve crystal seeds in ethanol and stir evenly, prepare 3g/L seed crystal liquid, take the prepared seed crystal liquid with a syringe with a diameter of 0.3cm, and take a distance of 2cm from the center of the surface of the α-Al 2 O 3 plate. At the center of the drop coating, apply the seed crystal droplet on the alumina plate at a speed of about 1 drop/second (the drop coating amount corresponding to the surface of the support body is 0.5-1ml/cm 2 ), so that the seed crystal solution completely covers the support. The surface of the body was baked at 80°C for 2.5 hours to obtain a support body covered with a seed layer, which was used for later use;
3)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温搅拌3h(搅拌速率300r/min),制得分子筛膜生长液,将所得表面覆盖晶种层的支撑体用聚四氟乙烯胶纸包裹背面(无晶种层的一面),放入盛有分子筛膜生长液的反应釜中,在100℃条件下反应5h,反应结束后用自来水冲洗急速冷却,将支撑体取出,用去离子水洗涤至中性并烘干,得到NaA分子筛膜。3) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, stirred at room temperature for 3h (stirring rate 300r/min) to obtain a molecular sieve film growth solution, and the back surface of the support whose surface was covered with the seed layer was wrapped with polytetrafluoroethylene tape (without the seed layer) one side), put it into the reaction kettle filled with molecular sieve membrane growth liquid, react at 100 ° C for 5 hours, rinse with tap water and rapidly cool after the reaction, take out the support, wash with deionized water to neutrality and dry, A NaA molecular sieve membrane was obtained.
图4为本实施例制得NaA分子筛膜的SEM图,图中可以看出所得分子筛膜表面平整、致密。FIG. 4 is a SEM image of the NaA molecular sieve membrane obtained in this example, and it can be seen from the figure that the surface of the obtained molecular sieve membrane is smooth and dense.
实施例4Example 4
一种NaA分子筛膜的合成方法,其制备方法包括如下步骤:A kind of synthetic method of NaA molecular sieve membrane, its preparation method comprises the steps:
1)依次用800#和1200#的砂纸对α-Al2O3板(直径3cm)进行打磨,置于水中进行超声震荡洗掉残留的粉末,依次在2mol/L的盐酸和氢氧化钠溶液分别浸泡24h,再超声震荡15min用去离子水洗至中性,并置于60℃烘箱中干燥12h,取出备用;1) Use 800# and 1200# sandpapers in turn to polish the α-Al 2 O 3 plate (diameter 3cm), place it in water and carry out ultrasonic vibration to wash off the residual powder, and then add 2mol/L hydrochloric acid and sodium hydroxide solution in turn. Soak for 24 hours, then ultrasonically shake for 15 minutes, wash with deionized water until neutral, and place them in a 60°C oven to dry for 12 hours, then take them out for use;
2)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温混合搅拌3h(搅拌速率400r/min),装入不锈钢反应釜中,在100℃条件下反应4h,抽滤,烘干(80℃),制得NaA分子筛晶种;将所得NaA分子筛晶种溶于乙醇中搅拌均匀,配制3g/L晶种液,用直径为0.3cm的注射器取配制好的晶种液,以距离α-Al2O3板表面圆心2cm高处为滴涂中心,以大约1滴/秒的速度将晶种液滴涂在氧化铝板上(支撑体表面对应的滴涂量为0.5~1ml/cm2),使晶种液完全覆盖在支撑体表面,80℃条件下烘2.5h,得表面覆盖晶种层的支撑体,备用;2) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, mixed and stirred at room temperature for 3h (stirring rate 400r/min), put into a stainless steel reaction kettle, reacted at 100°C for 4h, suction filtered, and dried (80°C) to obtain NaA molecular sieve seeds Dissolve the gained NaA molecular sieve crystal seeds in ethanol and stir evenly, prepare 3g/L seed crystal liquid, take the prepared seed crystal liquid with a syringe with a diameter of 0.3cm, and take a distance of 2cm from the center of the surface of the α-Al 2 O 3 plate. At the center of the drop coating, apply the seed crystal droplet on the alumina plate at a speed of about 1 drop/second (the drop coating amount corresponding to the surface of the support body is 0.5-1ml/cm 2 ), so that the seed crystal solution completely covers the support. The surface of the body was baked at 80°C for 2.5 hours to obtain a support body covered with a seed layer, which was used for later use;
3)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温搅拌4.5h(搅拌速率400r/min),制得分子筛膜生长液,将所得表面覆盖晶种层的支撑体用聚四氟乙烯胶纸包裹背面(无晶种层的一面),放入盛有分子筛膜生长液的反应釜中,在100℃条件下反应3h,反应结束后用自来水冲洗急速冷却,将支撑体取出,用去离子水洗涤至中性并烘干,得到NaA分子筛膜。3) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8 g of deionized water, stirred at room temperature for 4.5 h (stirring rate 400 r/min) to obtain a molecular sieve membrane growth liquid, and the back surface of the support whose surface was covered with the seed layer was wrapped with polytetrafluoroethylene tape (without the seed layer). side), put it into the reaction kettle filled with molecular sieve film growth liquid, react at 100 ° C for 3 hours, rinse with tap water and rapidly cool after the reaction, take out the support, wash with deionized water to neutrality and dry , to obtain a NaA molecular sieve membrane.
图5为本实施例制得NaA分子筛膜的SEM图,图中可以看出所得分子筛膜表面平整、致密。FIG. 5 is a SEM image of the NaA molecular sieve membrane obtained in this example, and it can be seen from the figure that the surface of the obtained molecular sieve membrane is smooth and dense.
对比例1Comparative Example 1
一种NaA分子筛膜的合成方法,其制备方法包括如下步骤:A kind of synthetic method of NaA molecular sieve membrane, its preparation method comprises the steps:
1)依次用800#和1200#的砂纸对α-Al2O3板(直径1cm)进行打磨,置于水中进行超声震荡洗掉残留的粉末,依次在2mol/L的盐酸和氢氧化钠溶液分别浸泡24h,再超声震荡15min用去离子水洗至中性,并置于60℃烘箱中干燥12h,取出备用;1) Use 800# and 1200# sandpaper in turn to polish the α-Al 2 O 3 plate (diameter 1cm), place it in water and carry out ultrasonic vibration to wash off the residual powder, and then add 2mol/L hydrochloric acid and sodium hydroxide solution in turn. Soak for 24 hours, then ultrasonically shake for 15 minutes, wash with deionized water until neutral, and place them in a 60°C oven to dry for 12 hours, then take them out for use;
2)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温混合搅拌3h(搅拌速率300r/min),装入不锈钢反应釜中,在100℃条件下反应4h,抽滤,烘干(80℃),制得NaA分子筛晶种;将所得NaA分子筛晶种溶于乙醇中搅拌均匀,配制3g/L晶种液,用聚四氟乙烯胶纸包裹氧化铝板一侧,采用热浸渍法使氧化铝板覆有晶种,80℃条件下烘干,得表面覆盖晶种层的支撑体,备用;2) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, mixed and stirred at room temperature for 3h (stirring rate 300r/min), put into a stainless steel reaction kettle, reacted at 100°C for 4h, suction filtered, and dried (80°C) to obtain NaA molecular sieve seeds ; Dissolve the obtained NaA molecular sieve crystal seeds in ethanol and stir evenly, prepare 3 g/L crystal seed solution, wrap one side of the alumina plate with polytetrafluoroethylene tape, and use the hot dipping method to make the alumina plate covered with crystal seeds, 80 ℃ condition Dry down to obtain the support body covered with the seed crystal layer, which is for later use;
3)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温搅拌4.5h(搅拌速率300r/min),制得分子筛膜生长液,将所得表面覆盖晶种层的支撑体放入盛有分子筛膜生长液的反应釜中,在100℃条件下反应3h,反应结束后用自来水冲洗急速冷却,将支撑体取出,用去离子水洗涤至中性并烘干,得到NaA分子筛膜。3) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, stirred at room temperature for 4.5h (stirring rate 300r/min) to obtain a molecular sieve film growth liquid, put the support of the obtained surface covering the seed layer into the reaction kettle filled with the molecular sieve film growth liquid, in the The reaction was carried out at 100° C. for 3 hours. After the reaction was completed, it was rinsed with tap water and rapidly cooled. The support was taken out, washed with deionized water until neutral, and dried to obtain a NaA molecular sieve membrane.
图6为本对比例所得NaA分子筛膜的SEM图,图中可以看出所得分子筛膜并不呈现紧密的状态,部分区域还漏有氧化铝板,这主要是因为热浸法无法使氧化铝板获得均匀紧致的晶种层所致。Fig. 6 is the SEM image of the NaA molecular sieve film obtained by the comparative example. It can be seen from the figure that the obtained molecular sieve film is not in a tight state, and there are alumina plates leaking in some areas. This is mainly because the hot dip method cannot make the alumina plates uniform. due to a compact seed layer.
对比例2Comparative Example 2
一种NaA分子筛膜的合成方法,其制备方法包括如下步骤:A kind of synthetic method of NaA molecular sieve membrane, its preparation method comprises the steps:
1)依次用800#和1200#的砂纸对α-Al2O3板(直径1cm)进行打磨,置于水中进行超声震荡洗掉残留的粉末,依次在2mol/L的盐酸和氢氧化钠溶液分别浸泡24h,再超声震荡15min用去离子水洗至中性,并置于60℃烘箱中干燥12h,取出备用;1) Use 800# and 1200# sandpaper in turn to polish the α-Al 2 O 3 plate (diameter 1cm), place it in water and carry out ultrasonic vibration to wash off the residual powder, and then add 2mol/L hydrochloric acid and sodium hydroxide solution in turn. Soak for 24 hours, then ultrasonically shake for 15 minutes, wash with deionized water until neutral, and place them in a 60°C oven to dry for 12 hours, then take them out for use;
2)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温混合搅拌3h(搅拌速率300r/min),装入不锈钢反应釜中,在100℃条件下反应4h,抽滤,烘干(80℃),制得NaA分子筛晶种;将所得NaA分子筛晶种溶于乙腈中搅拌均匀,配制3g/L晶种液,用直径为0.3cm的注射器取配制好的晶种液,以大约1滴/秒的速度将晶种液滴涂在氧化铝板上,使晶种液完全覆盖在支撑体表面,80℃条件下烘2.5h,得表面覆盖晶种层的支撑体,备用;2) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, mixed and stirred at room temperature for 3h (stirring rate 300r/min), put into a stainless steel reaction kettle, reacted at 100°C for 4h, suction filtered, and dried (80°C) to obtain NaA molecular sieve seeds Dissolve the gained NaA molecular sieve crystal seed in acetonitrile and stir evenly, prepare 3g/L seed crystal liquid, take the prepared seed crystal liquid with a syringe with a diameter of 0.3cm, and drop the crystal seed liquid at a speed of about 1 drop/second. Coat it on an alumina plate so that the seed crystal liquid completely covers the surface of the support, and bake it at 80°C for 2.5 hours to obtain a support with the surface covered with the seed layer, which is ready for use;
3)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温搅拌4.5h(搅拌速率300r/min),制得分子筛膜生长液,将所得表面覆盖晶种层的支撑体放入盛有分子筛膜生长液的反应釜中,在100℃条件下反应3h,反应结束后用自来水冲洗急速冷却,将支撑体取出,用去离子水洗涤至中性并烘干,得到NaA分子筛膜。3) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, stirred at room temperature for 4.5h (stirring rate 300r/min) to obtain a molecular sieve film growth liquid, put the support of the obtained surface covering the seed layer into the reaction kettle filled with the molecular sieve film growth liquid, in the The reaction was carried out at 100° C. for 3 hours. After the reaction was completed, it was rinsed with tap water and rapidly cooled. The support was taken out, washed with deionized water until neutral, and dried to obtain a NaA molecular sieve membrane.
图7为本对比例所得NaA分子筛晶种层的SEM图,图中可以看出所得分子筛晶种分布很不均匀,存在凹凸不平的现象。Fig. 7 is the SEM image of the NaA molecular sieve seed crystal layer obtained by the comparative example, and it can be seen from the figure that the distribution of the obtained molecular sieve seed crystal is very uneven, and there is a phenomenon of unevenness.
对比例3Comparative Example 3
一种NaA分子筛膜的合成方法,其制备方法包括如下步骤:A kind of synthetic method of NaA molecular sieve membrane, its preparation method comprises the steps:
1)依次用800#和1200#的砂纸对α-Al2O3板(直径1cm)进行打磨,置于水中进行超声震荡洗掉残留的粉末,依次在2mol/L的盐酸和氢氧化钠溶液分别浸泡24h,再超声震荡15min用去离子水洗至中性,并置于60℃烘箱中干燥12h,取出备用;1) Use 800# and 1200# sandpaper in turn to polish the α-Al 2 O 3 plate (diameter 1cm), place it in water and carry out ultrasonic vibration to wash off the residual powder, and then add 2mol/L hydrochloric acid and sodium hydroxide solution in turn. Soak for 24 hours, then ultrasonically shake for 15 minutes, wash with deionized water until neutral, and place them in a 60°C oven to dry for 12 hours, then take them out for use;
2)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温混合搅拌3h(搅拌速率300r/min),装入不锈钢反应釜中,在100℃条件下反应4h,抽滤,烘干(80℃),制得NaA分子筛晶种;将所得NaA分子筛晶种溶于乙醇中搅拌均匀,配制6g/L晶种液,用直径为0.3cm的注射器取配制好的晶种液,以距离α-Al2O3板表面圆心1cm高处为滴涂中心,以大约1滴/秒的速度将晶种液滴涂在氧化铝板上,使晶种液完全覆盖在支撑体表面,80℃条件下烘2.5h,得表面覆盖晶种层的支撑体,备用;2) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, mixed and stirred at room temperature for 3h (stirring rate 300r/min), put into a stainless steel reaction kettle, reacted at 100°C for 4h, suction filtered, and dried (80°C) to obtain NaA molecular sieve seeds Dissolve the gained NaA molecular sieve crystal seeds in ethanol and stir evenly, prepare 6g/L seed crystal liquid, take the prepared seed crystal liquid with a syringe with a diameter of 0.3cm, and take a distance of 1cm from the center of the surface of the α-Al 2 O 3 plate. At the drop coating center, apply the seed crystal droplet on the alumina plate at a speed of about 1 drop/second, so that the seed crystal liquid completely covers the surface of the support, and bake it at 80 °C for 2.5 hours to obtain a surface covered with a seed crystal layer. The support body, spare;
3)按照Al2O3:Na2O:SiO2:H2O摩尔比为1:2:2:120计,称取偏铝酸钠1.64g,氢氧化钠0.8g,30%硅溶胶3g,去离子水19.8g,室温搅拌3h(搅拌速率300r/min),制得分子筛膜生长液,将所得表面覆盖晶种层的支撑体用聚四氟乙烯胶纸包裹背面(无晶种层的一面),放入盛有分子筛膜生长液的反应釜中,在100℃条件下反应3h,反应结束后用自来水冲洗急速冷却,将支撑体取出,用去离子水洗涤至中性并烘干,得到NaA分子筛膜。3) According to the molar ratio of Al 2 O 3 : Na 2 O : SiO 2 : H 2 O of 1:2:2:120, weigh 1.64 g of sodium metaaluminate, 0.8 g of sodium hydroxide, and 3 g of 30% silica sol , 19.8g of deionized water, stirred at room temperature for 3h (stirring rate 300r/min) to obtain a molecular sieve film growth solution, and the back surface of the support whose surface was covered with the seed layer was wrapped with polytetrafluoroethylene tape (without the seed layer) one side), put it into the reaction kettle filled with molecular sieve film growth liquid, react at 100 ° C for 3 hours, rinse with tap water and rapidly cool after the reaction, take out the support, wash with deionized water to neutrality and dry, A NaA molecular sieve membrane was obtained.
图8为本实施例所得NaA分子筛晶种层的SEM,可以看出,NaA晶种在支撑体的表面分布很不均匀,存在凹凸不平的现象。FIG. 8 is the SEM of the NaA molecular sieve seed layer obtained in this example, it can be seen that the distribution of NaA seeds on the surface of the support is very uneven, and there are uneven phenomena.
应用例Application example
将实施例1~4所得NaA分子筛膜进行乙醇/水的渗透性测试,结果见表1。The NaA molecular sieve membranes obtained in Examples 1-4 were subjected to the permeability test of ethanol/water, and the results are shown in Table 1.
表1 实施例1~4所得NaA分子筛膜的乙醇/水渗透性测试结果Table 1 Ethanol/water permeability test results of NaA molecular sieve membranes obtained in Examples 1-4
上述结果表明,本发明所得NaA分子筛膜具有较高的渗透性能和分离性能。The above results show that the NaA molecular sieve membrane obtained in the present invention has higher permeability and separation performance.
显然,上述实施例仅仅是为清楚地说明所作的实例,而并非对实施方式的限制。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。而因此所引申的显而易见的变化或变动仍处于本发明创造的保护范围之内。Obviously, the above-mentioned embodiments are only examples for clear illustration, and are not intended to limit the implementation manner. For those of ordinary skill in the art, changes or modifications in other different forms can also be made on the basis of the above description. There is no need and cannot be exhaustive of all implementations here. However, the obvious changes or changes derived therefrom still fall within the protection scope of the present invention.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810178837.3A CN108246122B (en) | 2018-03-05 | 2018-03-05 | Method for synthesizing NaA molecular sieve membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810178837.3A CN108246122B (en) | 2018-03-05 | 2018-03-05 | Method for synthesizing NaA molecular sieve membrane |
Publications (2)
Publication Number | Publication Date |
---|---|
CN108246122A CN108246122A (en) | 2018-07-06 |
CN108246122B true CN108246122B (en) | 2020-12-29 |
Family
ID=62745533
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810178837.3A Active CN108246122B (en) | 2018-03-05 | 2018-03-05 | Method for synthesizing NaA molecular sieve membrane |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108246122B (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109351206A (en) * | 2018-10-23 | 2019-02-19 | 黄山学院 | A kind of preparation method of zeolite molecular sieve membrane for nanofiltration |
CN111013405A (en) * | 2019-12-25 | 2020-04-17 | 江门谦信化工发展有限公司 | Ethanol/water system molecular sieve composite membrane and preparation method and application thereof |
CN111992050B (en) * | 2020-09-10 | 2022-05-17 | 南京惟新环保装备技术研究院有限公司 | Carrier surface modified hydrophilic molecular sieve membrane and preparation method thereof |
CN112371081A (en) * | 2020-10-19 | 2021-02-19 | 西安工程大学 | Preparation method of attapulgite-based NaA molecular sieve membrane support |
CN113198334B (en) * | 2021-05-07 | 2021-11-30 | 宿州中粮生物化学有限公司 | NaA molecular sieve membrane and preparation method and application thereof |
CN114225718A (en) * | 2021-12-24 | 2022-03-25 | 中国科学院上海硅酸盐研究所 | NaA molecular sieve membrane on surface of porous silicon nitride ceramic and preparation method thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101544379A (en) * | 2009-04-30 | 2009-09-30 | 浙江大学 | Method for synthesizing molecular sieve membrane by dip coating-rubbing crystal-coating method |
US10265660B2 (en) * | 2009-05-21 | 2019-04-23 | Battelle Memorial Institute | Thin-sheet zeolite membrane and methods for making the same |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101279207A (en) * | 2008-05-20 | 2008-10-08 | 吉林大学 | Preparation method of SAPO-34 molecular sieve membrane for selective separation of methane gas |
CN103846018A (en) * | 2012-12-06 | 2014-06-11 | 中国科学院成都有机化学有限公司 | Method for synthesizing NaA molecular sieve membrane by spraying crystal seeds |
CN104418340B (en) * | 2013-09-11 | 2017-01-25 | 青岛科技大学 | Preparation method of molecular sieve membrane |
CN103599709B (en) * | 2013-11-12 | 2016-05-18 | 中国海洋石油总公司 | The method of the synthetic NaA zeolite membrane of a kind of high rate of film build |
CN106957062B (en) * | 2017-05-05 | 2019-11-01 | 南京膜材料产业技术研究院有限公司 | A kind of preparation method being orientated SAPO-34 molecular screen membrane |
-
2018
- 2018-03-05 CN CN201810178837.3A patent/CN108246122B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101544379A (en) * | 2009-04-30 | 2009-09-30 | 浙江大学 | Method for synthesizing molecular sieve membrane by dip coating-rubbing crystal-coating method |
US10265660B2 (en) * | 2009-05-21 | 2019-04-23 | Battelle Memorial Institute | Thin-sheet zeolite membrane and methods for making the same |
Also Published As
Publication number | Publication date |
---|---|
CN108246122A (en) | 2018-07-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108246122B (en) | Method for synthesizing NaA molecular sieve membrane | |
CN101544379B (en) | Method for synthesizing molecular sieve membrane by dip coating-rubbing crystal-coating method | |
CN105727757B (en) | A kind of preparation method of orientation LTL molecular sieve membrane for gas separation | |
CN103877865B (en) | A kind of method of synthesizing NaA molecular sieve membrane | |
CN106268933B (en) | Core-shell ZSM-5/SAPO-5 composite molecular sieve membrane and its preparation method and its application in biomass gas purification | |
CN108295672B (en) | A kind of preparation method of metal organic framework ZIF-8 film | |
CN105289323B (en) | A kind of preparation method of high-performance silicalite molecular screen membranes | |
CN103432828A (en) | Preparation method of porous metal film | |
CN101252983A (en) | Zeolitic separation membrane and process for producing the same | |
CN102126731B (en) | Method for synthesizing highly-oriented MFI (Melt Flow Index) molecular sieve membrane through controlled secondary growth of twin crystal | |
CN104200947B (en) | Controllable dilute magnetic semiconductor material of a kind of nanostructured and preparation method thereof and device | |
CN107337472B (en) | Preparation method of FAU type zeolite molecular sieve membrane | |
CN103933871A (en) | Preparation method of high-stability all-silicon MFI type molecular sieve membrane | |
CN105921033A (en) | Method for preparing CHA molecular sieve membrane in clear liquid | |
CN111841333B (en) | Efficient preparation method of supported ZIF-8 membrane | |
CN110975817B (en) | Aluminum foil-based aluminum-fumaric acid MOF adsorbent coating and mixed solvent in-situ synthesis method and application thereof | |
CN112121652B (en) | Preparation method of metal organic framework-ceramic membrane nanofiltration composite membrane | |
CN109970075B (en) | Method for synthesizing A-type molecular sieve membrane at low temperature | |
CN1215351A (en) | improved membrane | |
CN112408411A (en) | A method for synthesizing SAPO-34 molecular sieve membrane based on microwave heating | |
CN103086395B (en) | Preparation method of SAPO series molecular sieve membrane with metal oxide as carrier | |
CN110467479A (en) | A kind of the regulation method and fly ash base ceramic membrane of fly ash base ceramics membrane aperture | |
CN112029104A (en) | Metal organic framework film prepared by vapor-assisted epitaxial growth method and application thereof | |
CN101857522B (en) | Method for separating methanol/methyl methacrylate mixed system | |
CN102583425A (en) | Synthetic method of MFI (Mechanical Fuel Injection) type molecular sieve membrane |
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 | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20230202 Address after: Room 103, Floor 1, Building 1, No. 5, Dayushuo Road, Pukou District, Nanjing, Jiangsu Province, 211806 Patentee after: Jiangsu Fengkeda Technology Co.,Ltd. Address before: 430070 Hubei Province, Wuhan city Hongshan District Luoshi Road No. 122 Patentee before: WUHAN University OF TECHNOLOGY |
|
PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A Synthesis Method of NaA Molecular Sieve Membrane Effective date of registration: 20230607 Granted publication date: 20201229 Pledgee: Nanjing Branch of Jiangsu Bank Co.,Ltd. Pledgor: Jiangsu Fengkeda Technology Co.,Ltd. Registration number: Y2023980042949 |