WO2017121169A1 - 一种蒽醌功能化的聚偏氟乙烯膜的制备方法 - Google Patents
一种蒽醌功能化的聚偏氟乙烯膜的制备方法 Download PDFInfo
- Publication number
- WO2017121169A1 WO2017121169A1 PCT/CN2016/103560 CN2016103560W WO2017121169A1 WO 2017121169 A1 WO2017121169 A1 WO 2017121169A1 CN 2016103560 W CN2016103560 W CN 2016103560W WO 2017121169 A1 WO2017121169 A1 WO 2017121169A1
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- WO
- WIPO (PCT)
- Prior art keywords
- polyvinylidene fluoride
- tetramethoxynaphthalene
- reaction
- hydroxy
- butene
- Prior art date
Links
- 229920002981 polyvinylidene fluoride Polymers 0.000 title claims abstract description 46
- 239000012528 membrane Substances 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 28
- -1 poly(vinylidene fluoride) Polymers 0.000 title abstract description 11
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims abstract description 54
- 229920001577 copolymer Polymers 0.000 claims abstract description 25
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 21
- 230000003197 catalytic effect Effects 0.000 claims abstract description 13
- 229920000642 polymer Polymers 0.000 claims abstract description 8
- 229910021591 Copper(I) chloride Inorganic materials 0.000 claims abstract description 7
- 238000005266 casting Methods 0.000 claims abstract description 7
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 claims abstract description 7
- 229940045803 cuprous chloride Drugs 0.000 claims abstract description 7
- VMGSQCIDWAUGLQ-UHFFFAOYSA-N n',n'-bis[2-(dimethylamino)ethyl]-n,n-dimethylethane-1,2-diamine Chemical compound CN(C)CCN(CCN(C)C)CCN(C)C VMGSQCIDWAUGLQ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000010526 radical polymerization reaction Methods 0.000 claims abstract description 4
- 239000000178 monomer Substances 0.000 claims abstract description 3
- 239000002904 solvent Substances 0.000 claims abstract description 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 66
- 239000000243 solution Substances 0.000 claims description 51
- 238000006243 chemical reaction Methods 0.000 claims description 49
- 239000002033 PVDF binder Substances 0.000 claims description 43
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 35
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 32
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 30
- 239000005457 ice water Substances 0.000 claims description 29
- 238000003786 synthesis reaction Methods 0.000 claims description 29
- 230000015572 biosynthetic process Effects 0.000 claims description 28
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 27
- 229920000131 polyvinylidene Polymers 0.000 claims description 22
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- IJOOHPMOJXWVHK-UHFFFAOYSA-N chlorotrimethylsilane Chemical compound C[Si](C)(C)Cl IJOOHPMOJXWVHK-UHFFFAOYSA-N 0.000 claims description 18
- 238000003756 stirring Methods 0.000 claims description 18
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 claims description 17
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims description 17
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 16
- 235000019439 ethyl acetate Nutrition 0.000 claims description 15
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 15
- FBYIJIHPWCXRHH-UHFFFAOYSA-N 1,4,5,8-tetramethoxynaphthalene-2-carbaldehyde Chemical compound O=CC1=CC(OC)=C2C(OC)=CC=C(OC)C2=C1OC FBYIJIHPWCXRHH-UHFFFAOYSA-N 0.000 claims description 14
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- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims description 11
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- 229910052707 ruthenium Inorganic materials 0.000 claims description 11
- 229910021556 Chromium(III) chloride Inorganic materials 0.000 claims description 10
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 10
- 229930192627 Naphthoquinone Natural products 0.000 claims description 10
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 10
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- QSWDMMVNRMROPK-UHFFFAOYSA-K chromium(3+) trichloride Chemical compound [Cl-].[Cl-].[Cl-].[Cr+3] QSWDMMVNRMROPK-UHFFFAOYSA-K 0.000 claims description 10
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- SWNROPPWBFHVCS-UHFFFAOYSA-N 1,4,5,8-tetramethoxynaphthalene Chemical compound C1=CC(OC)=C2C(OC)=CC=C(OC)C2=C1OC SWNROPPWBFHVCS-UHFFFAOYSA-N 0.000 claims description 9
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- XMPZTFVPEKAKFH-UHFFFAOYSA-P ceric ammonium nitrate Chemical compound [NH4+].[NH4+].[Ce+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O XMPZTFVPEKAKFH-UHFFFAOYSA-P 0.000 claims description 5
- VAYGXNSJCAHWJZ-UHFFFAOYSA-N dimethyl sulfate Chemical compound COS(=O)(=O)OC VAYGXNSJCAHWJZ-UHFFFAOYSA-N 0.000 claims description 5
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- 239000002808 molecular sieve Substances 0.000 claims description 5
- 238000010992 reflux Methods 0.000 claims description 5
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 5
- JRMUNVKIHCOMHV-UHFFFAOYSA-M tetrabutylammonium bromide Chemical compound [Br-].CCCC[N+](CCCC)(CCCC)CCCC JRMUNVKIHCOMHV-UHFFFAOYSA-M 0.000 claims description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 4
- ITVPBBDAZKBMRP-UHFFFAOYSA-N chloro-dioxido-oxo-$l^{5}-phosphane;hydron Chemical compound OP(O)(Cl)=O ITVPBBDAZKBMRP-UHFFFAOYSA-N 0.000 claims description 3
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical class [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 2
- 239000003999 initiator Substances 0.000 claims description 2
- ZEGDFCCYTFPECB-UHFFFAOYSA-N 2,3-dimethoxynaphthalene-1,4-dione Chemical compound C1=CC=C2C(=O)C(OC)=C(OC)C(=O)C2=C1 ZEGDFCCYTFPECB-UHFFFAOYSA-N 0.000 claims 1
- 239000005046 Chlorosilane Substances 0.000 claims 1
- KOPOQZFJUQMUML-UHFFFAOYSA-N chlorosilane Chemical compound Cl[SiH3] KOPOQZFJUQMUML-UHFFFAOYSA-N 0.000 claims 1
- 238000013375 chromatographic separation Methods 0.000 claims 1
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 abstract 2
- SKUSCEYATDFRHZ-UHFFFAOYSA-N 1-(1,4,5,8-tetramethoxynaphthalen-2-yl)but-3-en-1-ol Chemical compound C=CCC(O)C1=CC(OC)=C2C(OC)=CC=C(OC)C2=C1OC SKUSCEYATDFRHZ-UHFFFAOYSA-N 0.000 abstract 2
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- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 9
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- 101710141544 Allatotropin-related peptide Proteins 0.000 description 3
- 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 description 3
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- C08F12/14—Monomers containing only one unsaturated aliphatic radical containing one ring substituted by hetero atoms or groups containing heteroatoms
- C08F12/22—Oxygen
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Definitions
- the invention belongs to the field of preparation of a polyvinylidene fluoride ultrafiltration membrane, and in particular relates to a preparation method of a hydrazine functionalized polyvinylidene fluoride ultrafiltration membrane.
- the biological method is the most common method to solve the above-mentioned problem of water pollution, but due to the limitation of the electron transport rate in the biological denitrification process, the biological treatment effect is unstable and the treatment efficiency is low. It has been found that the redox mediator can accelerate the electron transport rate in the biological denitrification process and improve the biological process efficiency. Terpenoids are one of the redox mediators. There have been a lot of reports to prove that terpenoids can effectively promote the degradation of nitrogenous wastewater.
- reaction solution is extracted with chloroform, washed with saturated brine, dried over anhydrous magnesium sulfate, filtered, and then evaporated to chloroform, and then purified by column chromatography to obtain 1,4,5,8-tetramethoxynaphthalene-2-carbaldehyde;
- step 2 the volume ratio of N,N-2-methylacetamide, phosphorus oxychloride, and 1,4,5,8-tetramethoxynaphthalene in chloroform is 2-3:2-5. :10-25.
- the eluents used in the column chromatography in Step 1, Step 2, and Step 3 were mixed solvents of petroleum ether and acetone in a volume ratio of 4:1.
- the step (2) is specifically: adding a solution of polyvinylidene fluoride and N,N-dimethylformamide in a double-layer glass reactor (as shown in FIG. 3), stirring until the solution is uniform, and adding Me6TREN and 2- (1-hydroxy-3-butene)-1,4,5,8-tetramethoxynaphthalene, deoxygenated with argon for 30 min, added cuprous chloride, deoxygenated for 1 h, sealed, double-layer glass reactor The mixture was placed in an ice water bath and subjected to ultraviolet irradiation under magnetic stirring for a predetermined time.
- the outer layer of the double-layer glass reactor in the step 2) is provided with a water inlet and a water outlet, and is connected with the constant temperature circulating water bath to keep the reaction temperature constant; the inner layer is provided with an air inlet, a vacuum port and a feed.
- the reaction was carried out under a nitrogen atmosphere; the top was covered with quartz glass to reduce the absorption of ultraviolet light by the glass during ultraviolet irradiation; the wavelength of the ultraviolet lamp used was 365 nm and the power was 1000 W.
- the mass ratio of the N,N-dimethylformamide to the polymer of the step (3) is 15-20:80-85.
- Figure 3 is a double glass reactor
- Fig. 5 is a recycling effect diagram of a fluorene-functionalized polyvinylidene fluoride ultrafiltration membrane; as can be seen from the figure, the ultrafiltration membrane of the present invention has stable performance and can be recycled and used multiple times.
- N,N-2-methylacetamide was added to two reaction bottles, and the two reaction bottles were placed in an ice water bath, which was slowly dropped.
- the aromatic ether copolymer is vacuum dried for use; the ratio of raw materials is: 2-(1-hydroxy-3-butene)-1,4,5,8-tetramethoxynaphthalene, polyvinylidene fluoride, N,N - dimethylformamide, the mass ratio of the catalytic system is: 45:7:500:0.5;
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Abstract
一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法,包括:(1)2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成;(2)聚偏氟乙烯-芳香醚类共聚物的合成:选用聚偏氟乙烯为引发剂,2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘为单体,N,N-二甲基甲酰胺为溶剂,氯化亚铜/Me6TREN为催化体系,经过原子自由基聚合法合成聚偏氟乙烯-芳香醚类共聚物;(3)利用脱甲基氧化法将聚偏氟乙烯-芳香醚类共聚物还原成醌;(4)将步骤(3)的聚合物和N,N-二甲基甲酰胺制成铸膜液,刮制成膜。
Description
本发明属于聚偏氟乙烯超滤膜的制备领域,具体涉及一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法。
聚偏氟乙烯高分子材料具有机械强度高,化学稳定性良好、耐紫外辐照、室温下不被酸、碱、强氧化剂和卤素腐蚀等优点,以聚偏氟乙烯为原料制备的膜材料在环境工程领域应用广泛。但是聚偏氟乙烯表面疏水性较强,表面能比较低等缺点将影响膜的寿命。为进一步优化聚偏氟乙烯膜的性能,研究人员进行了一系列改性研究。申请号为2010102559483的中国专利申请公开了一种聚偏氟乙烯改性膜的制备方法,通过在铸膜液中添加致孔剂和聚丙烯腈来共混改性聚偏氟乙烯膜;申请号为2011100222338的中国专利申请利用水相原子转移自由基聚合的方法在聚偏氟乙烯膜表面上接枝有功能性聚合物,使聚偏氟乙烯膜表功能化,所得的膜具有良好的亲水性和抗污能力;申请号为2014106980874的中国专利申请通过静电纺丝的方法制备了聚偏氟乙烯/改性蒙脱土复合纤维膜材料,所制备的膜材料具有优良疏水吸油性能,可用于海上或水面溢油的处理、含油废水的处理。上述改性研究对优化膜性能、增加膜的使用寿命有一定意义,但是其应用原理仍然是基于物理分离,即将污染物质转移和富集,并未实现污染物质的降解,仍有危害环境的可能。研究开发一种既能够净化污水,又能够降解污染物质的膜具有重要的意义。
高浓度含氮的生活污水、工业废水和农田地表水径流汇入湖泊、水库、河流和海湾水域,造成水体中的某些藻类过度繁殖,严重恶化水质,破坏水体生态平衡。生物法是解决上述水体污染问题的最常用方法,但是受生物反硝化过程中电子传输速率的限制,生物法处理效果不稳定、处理效率低。经研究发现氧化还原介体可加快生物反硝化过程中的电子传输速率,提高生物法的处理效率。蒽醌类化合物是氧化还原介体中的一种,目前已有大量报道证实蒽醌类化合物能有效促进含氮废水的降解。已有的报道中多将蒽醌类化合物直接投入使用,这将造成氧化还原介体的流失,引发二次污染。为解决上述问题,研究人员对蒽醌类化合物的固定进行了一系列的研究。文献《固定化氧化还原介体强化酸性红B生物脱色作用研究》采用海藻酸钙固定1,5-二氯蒽,并应用于偶氮染料酸性红B的脱色中,发现固定化的1,5-二氯蒽能促进偶氮染料酸性红B的脱色,但是1,5-二氯蒽只是通过物理作用力束缚在载体上,容易从载体上解析下来。文献《固定化氧化还原介体加速亚硝酸盐生物反硝化作用》利用循环伏
安法固定蒽醌磺酸钠(AQS/PPy/ACF),结果表明固定后的蒽醌磺酸钠能够明显加速亚硝酸盐生物反硝化过程,但是采用循环伏安法固定蒽醌磺酸钠的前提是制备聚吡咯膜,其制备过程受很多参数控制,非常复杂。如果将氧化还原介体固定于膜上,能有效解决氧化还原介体固定的问题,提高高浓度含氮污水的处理效率。
发明内容
本发明的目的在于针对现有技术的不足,提供一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法。该发明以化学合成和化学改性的方法将氧化还原介体固定于聚偏氟乙烯上,解决了现有的物理固定方法中出现的醌类物质易从载体上脱落流失,造成水体二次污染等问题;所制得的蒽醌功能化聚偏氟乙烯超滤膜在含氮污水处理领域具有良好的应用前景。
为实现上述目的,本发明采用如下技术方案:
一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法,包括以下步骤:
(1)2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成;
(2)聚偏氟乙烯-芳香醚类共聚物的合成:选用聚偏氟乙烯为引发剂,2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘为单体,N,N-二甲基甲酰胺为溶剂,氯化亚铜/Me6TREN为催化体系,经原子自由基聚合法合成聚偏氟乙烯-芳香醚类共聚物;
(3)利用脱甲基氧化法将聚偏氟乙烯-芳香醚类共聚物脱甲氧基还原成醌;
(4)将步骤(3)的聚合物和N,N-二甲基甲酰胺制成铸膜液,刮制成膜。
步骤(1)中2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成包括以下步骤:
①1,4,5,8-四甲氧基萘的合成:将萘茜、催化量四丁基溴化铵、四氢呋喃加入到圆底烧瓶中,搅拌至溶解,然后添加连二亚硫酸钠水溶液和硫酸二甲酯溶液,搅拌至溶液均匀;将圆底烧瓶移至冰水浴中,反应1h,缓慢滴加NaOH水溶液,滴加完毕后移除冰水浴,在室温下反应30min,匀速搅拌18h至反应完全,反应液经乙酸乙酯萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收乙酸乙酯,柱层析分离得1,4,5,8-四甲氧基萘;
②1,4,5,8-四甲氧基萘-2-甲醛的合成:在两口反应瓶中加入N,N-2-甲基乙酰胺,将两口反应瓶置于冰水浴中,依次缓慢滴加三氯氧磷溶液和0.063mol/L 1,4,5,8-四甲氧基萘的三氯甲烷溶液,滴加完毕后移除冰水浴,加热回流反应5h;然后加冰水停止反应,反应液经氯仿萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收氯仿,柱层析分离得1,4,5,8-四甲氧基萘-2-甲醛;
③2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成:氩气保护下,在干燥的两口反应瓶中依次加入分子筛、无水四氢呋喃、无水三氯化铬和锰粉,搅拌至颜色变成黑色后加入烯丙基
溴,加入1,4,5,8-四甲氧基萘-2-甲醛和三甲基氯硅烷,反应3h,加饱和碳酸氢钠淬灭反应,反应液经硅藻土、乙醚洗涤,乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压回收浓缩残留物,用四氢呋喃溶解,加10%盐酸水解,在室温下搅拌10min,用乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压浓缩,柱层析得2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘。
步骤①中萘茜、四氢呋喃、连二亚硫酸钠、硫酸二甲酯、氢氧化钠的质量配比为:1.2-2:70-80:50-60:100-120:100-150。
步骤②中N,N-2-甲基乙酰胺、三氯氧磷、1,4,5,8-四甲氧基萘的三氯甲烷溶液的体积配比为:2-3:2-5:10-25。
步骤③中无水四氢呋喃、无水三氯化铬、1,4,5,8-四甲氧基萘-2-甲醛、三甲基氯硅烷、烯丙基溴、锰粉的质量配比为:10-30:10-30:30-60:30-80:30-80:600-800。
步骤①、步骤②、步骤③中柱层析时所用的洗脱剂均为体积比为4:1的石油醚和丙酮混合溶剂。
步骤(2)具体为:在双层玻璃反应器(如图3所示)中依次添加聚偏氟乙烯、N,N-二甲基甲酰胺溶液,搅拌至溶液均匀后,添加Me6TREN和2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘,通氩气除氧30min,添加氯化亚铜,除氧1h,密封,将双层玻璃反应器置于冰水浴中,磁力搅拌下紫外辐照反应至预定的时间,待反应结束后用1:1的乙醇/水溶液沉析过滤,用氯仿重复多次抽提,得聚偏氟乙烯-芳香醚类共聚物,真空干燥备用;原料配比为:2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘、聚偏氟乙烯、N,N-二甲基甲酰胺、催化体系的质量配比为:30-60:5-12:400-550:0.1-1。
步骤2)中所述双层玻璃反应器的外层上设有进水口和出水口,与恒温循环水浴槽相连,以保持反应温度恒定;内层设有进气口、抽真空口及进料口,使反应在氮气氛围下进行;顶端采用石英玻璃加盖,以减少紫外辐照过程中玻璃对紫外光的吸收;所用紫外灯的波长为365nm,功率为1000W。
步骤(3)具体为:在两口反应瓶中滴加聚偏氟乙烯-芳香醚类共聚物的乙氰溶液,室温搅拌下滴加硝酸铈铵的水溶液,反应1h,减压回收乙氰,用氯仿萃取,水洗,饱和食盐水洗,无水硫酸镁干燥1.5h,减压回收氯仿,硅胶柱层析分离得2-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌和6-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌的混合物,真空干燥后备用;所述的硅胶柱层析时所用的洗脱剂为体积比为3:1的石油醚和丙酮混合溶剂。
步骤(4)中:N,N-二甲基甲酰胺和步骤(3)的聚合物的质量配比为:15-20:80-85。
上述制备过程主要分为四步:①本发明利用NHK反应在萘茜上引入双键侧链,利
于高分子材料与蒽醌类物质的ATRP聚合反应的发生;②利用ATRP法合成接枝PVDF-芳香醚类共聚物,使聚偏氟乙烯功能化;③利用脱甲基氧化法制备醌,使聚偏氟乙烯蒽醌功能化;④利用相转化法,将制备的蒽醌功能化聚偏氟乙烯材料刮制成膜。
本发明的有益效果在于:
(1)单纯的蒽醌类化合物无法进行原子自由基聚合,本发明利用NHK反应在萘茜上引入双键侧链,利于高分子材料与蒽醌类物质的ATRP聚合反应的发生;在聚偏氟乙烯膜上所固定的蒽醌分子牢固、不会脱落;
(2)应用膜作为氧化还原介体的固定载体,可以适应各种膜处理设备,利于本发明的推广和应用;
(3)本发明能有效促进高浓度含氮废水的降解,特别是印染废水的降解。
图1为2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成路线图;
图2为聚偏氟乙烯-芳香醚类共聚物的合成路线图;
图3为双层玻璃反应器;
图4为所制膜片的红外光谱图;
图5为蒽醌功能化聚偏氟乙烯超滤膜的循环使用效果图;从图中可以看出,本发明的超滤膜性能稳定,可循环多次使用。
本发明用下列实施例来进一步说明本发明,但本发明的保护范围并不限于下列实施例。
实施例1
一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法,包括以下步骤:
(1)2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成:
①1,4,5,8-四甲氧基萘的合成:将萘茜、催化量四丁基溴化铵、四氢呋喃加入到圆底烧瓶中,搅拌至溶解,然后添加连二亚硫酸钠水溶液和硫酸二甲酯溶液,搅拌至溶液均匀;将圆底烧瓶移至冰水浴中,反应1h,缓慢滴加NaOH水溶液,滴加完毕后移除冰水浴,在室温下反应30min,匀速搅拌18h至反应完全,反应液经乙酸乙酯萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收乙酸乙酯,柱层析分离得1,4,5,8-四甲氧基萘;1H NMR(400MHz,DMSO):δ6.44(d,4H),3.37(s,12H,CH3)。
萘茜、四氢呋喃、连二亚硫酸钠、硫酸二甲酯、氢氧化钠的质量配比为:1.5:75:55:
110:125;
②1,4,5,8-四甲氧基萘-2-甲醛的合成:在两口反应瓶中加入N,N-2-甲基乙酰胺,将两口反应瓶置于冰水浴中,依次缓慢滴加三氯氧磷和0.063mol/L1,4,5,8-四甲氧基萘的三氯甲烷溶液,滴加完毕后移除冰水浴,加热回流反应5h;然后加冰水停止反应,反应液经氯仿萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收氯仿,柱层析分离得1,4,5,8-四甲氧基萘-2-甲醛;1H NMR(400MHz,DMSO):δ6.49-6.51(m,3H),3.40(s,9H,CH3),3.43(s,3H,CH3),10.11(s,1H,CHO)。
N,N-2-甲基乙酰胺、三氯氧磷、1,4,5,8-四甲氧基萘的三氯甲烷溶液的体积配比为:2.5:3:15;
③2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成:氩气保护下,在干燥的两口反应瓶中依次加入分子筛、无水四氢呋喃、无水三氯化铬和锰粉,搅拌至颜色变成黑色后加入烯丙基溴,加入1,4,5,8-四甲氧基萘-2-甲醛和三甲基氯硅烷,反应3h,加饱和碳酸氢钠淬灭反应,反应液经硅藻土、乙醚洗涤,乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压回收浓缩残留物,用四氢呋喃溶解,加10%盐酸水解,在室温下搅拌10min,用乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压浓缩,柱层析得2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘;1H NMR(400MHz,DMSO):δ6.47-6.51(m,3H),3.37(s,9H,CH3),3.43(s,3H,CH3),8.45(s,1H,OH),4.83(t,1H,CH),2.39(m,2H,CH2),4.92(d,2H,CH2),5.76(m,1H,CH)。
无水四氢呋喃、无水三氯化铬、1,4,5,8-四甲氧基萘-2-甲醛、三甲基氯硅烷、烯丙基溴、锰粉的质量配比为:20:20:50:60:50:700。
(2)聚偏氟乙烯-芳香醚类共聚物的合成:在双层玻璃反应器中依次添加聚偏氟乙烯、N,N-二甲基甲酰胺溶液,搅拌至溶液均匀后,添加Me6TREN和2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘,通氩气除氧30min,添加氯化亚铜,除氧1h,密封,将双层玻璃反应器置于冰水浴中,磁力搅拌下紫外辐照反应至预定的时间,待反应结束后用1:1的乙醇/水溶液沉析过滤,用氯仿重复多次抽提,得聚偏氟乙烯-芳香醚类共聚物,真空干燥备用;原料配比为:2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘、聚偏氟乙烯、N,N-二甲基甲酰胺、催化体系的质量配比为:45:7:500:0.5;
(3)利用脱甲基氧化法将聚偏氟乙烯-芳香醚类共聚物制成醌:
在两口反应瓶中滴加聚偏氟乙烯-芳香醚类共聚物的乙氰溶液,室温搅拌下滴加硝酸铈铵的水溶液,反应1h,减压回收乙氰,用氯仿萃取,水洗,饱和食盐水洗,无水硫酸镁干燥1.5
h,减压回收氯仿,硅胶柱层析分离得2-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌和6-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌的混合物,真空干燥后备用;所述的硅胶柱层析时所用的洗脱剂为体积比为3:1的石油醚和丙酮混合溶剂;
(4)将步骤(3)的聚合物和N,N-二甲基甲酰胺按质量配比17:82制成铸膜液,刮制成膜。
实施例2
一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法,包括以下步骤:
(1)2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成:
①1,4,5,8-四甲氧基萘的合成:将萘茜、催化量四丁基溴化铵、四氢呋喃加入到圆底烧瓶中,搅拌至溶解,然后添加连二亚硫酸钠水溶液和硫酸二甲酯溶液,搅拌至溶液均匀;将圆底烧瓶移至冰水浴中,反应1h,缓慢滴加NaOH水溶液,滴加完毕后移除冰水浴,在室温下反应30min,匀速搅拌18h至反应完全,反应液经乙酸乙酯萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收乙酸乙酯,柱层析分离得1,4,5,8-四甲氧基萘;萘茜、四氢呋喃、连二亚硫酸钠、硫酸二甲酯、氢氧化钠的质量配比为:1.2:80:50:120:150;
②1,4,5,8-四甲氧基萘-2-甲醛的合成:在两口反应瓶中加入N,N-2-甲基乙酰胺,将两口反应瓶置于冰水浴中,依次缓慢滴加三氯氧磷和0.063mol/L 1,4,5,8-四甲氧基萘的三氯甲烷溶液,滴加完毕后移除冰水浴,加热回流反应5h;然后加冰水停止反应,反应液经氯仿萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收氯仿,柱层析分离得1,4,5,8-四甲氧基萘-2-甲醛;N,N-2-甲基乙酰胺、三氯氧磷、1,4,5,8-四甲氧基萘的三氯甲烷溶液的体积配比为:2:5:10;
③2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成:氩气保护下,在干燥的两口反应瓶中依次加入分子筛、无水四氢呋喃、无水三氯化铬和锰粉,搅拌至颜色变成黑色后加入烯丙基溴,加入1,4,5,8-四甲氧基萘-2-甲醛和三甲基氯硅烷,反应3h,加饱和碳酸氢钠淬灭反应,反应液经硅藻土、乙醚洗涤,乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压回收浓缩残留物,用四氢呋喃溶解,加10%盐酸水解,在室温下搅拌10min,用乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压浓缩,柱层析得2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘;无水四氢呋喃、无水三氯化铬、1,4,5,8-四甲氧基萘-2-甲醛、三甲基氯硅烷、烯丙基溴、锰粉的质量配比为:10:30:30:80:30:800。
(2)聚偏氟乙烯-芳香醚类共聚物的合成:在双层玻璃反应器中依次添加聚偏氟乙烯、N,N-二甲基甲酰胺溶液,搅拌至溶液均匀后,添加Me6TREN和2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘,通氩气除氧30min,添加氯化亚铜,除氧1h,密封,将双层玻璃反应器置于冰水
浴中,磁力搅拌下紫外辐照反应至预定的时间,待反应结束后用1:1的乙醇/水溶液沉析过滤,用氯仿重复多次抽提,得聚偏氟乙烯-芳香醚类共聚物,真空干燥备用;原料配比为:2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘、聚偏氟乙烯、N,N-二甲基甲酰胺、催化体系的质量配比为:30:12:400:1;
(3)利用脱甲基氧化法将聚偏氟乙烯-芳香醚类共聚物制成醌:
在两口反应瓶中滴加聚偏氟乙烯-芳香醚类共聚物的乙氰溶液,室温搅拌下滴加硝酸铈铵的水溶液,反应1h,减压回收乙氰,用氯仿萃取,水洗,饱和食盐水洗,无水硫酸镁干燥1.5h,减压回收氯仿,硅胶柱层析分离得2-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌和6-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌的混合物,真空干燥后备用;所述的硅胶柱层析时所用的洗脱剂为体积比为3:1的石油醚和丙酮混合溶剂;
(4)将步骤(3)的聚合物和N,N-二甲基甲酰胺按质量配比15:85制成铸膜液,刮制成膜。
实施例3
一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法,包括以下步骤:
(1)2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成:
①1,4,5,8-四甲氧基萘的合成:将萘茜、催化量四丁基溴化铵、四氢呋喃加入到圆底烧瓶中,搅拌至溶解,然后添加连二亚硫酸钠水溶液和硫酸二甲酯溶液,搅拌至溶液均匀;将圆底烧瓶移至冰水浴中,反应1h,缓慢滴加NaOH水溶液,滴加完毕后移除冰水浴,在室温下反应30min,匀速搅拌18h至反应完全,反应液经乙酸乙酯萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收乙酸乙酯,柱层析分离得1,4,5,8-四甲氧基萘;萘茜、四氢呋喃、连二亚硫酸钠、硫酸二甲酯、氢氧化钠的质量配比为:2:70:60:100:100;
②1,4,5,8-四甲氧基萘-2-甲醛的合成:在两口反应瓶中加入N,N-2-甲基乙酰胺,将两口反应瓶置于冰水浴中,依次缓慢滴加三氯氧磷溶液0.063mol/L1,4,5,8-四甲氧基萘的三氯甲烷溶液,滴加完毕后移除冰水浴,加热回流反应5h;然后加冰水停止反应,反应液经氯仿萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收氯仿,柱层析分离得1,4,5,8-四甲氧基萘-2-甲醛;N,N-2-甲基乙酰胺、三氯氧磷、1,4,5,8-四甲氧基萘的三氯甲烷溶液的体积配比为:3:2:25;
③2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成:氩气保护下,在干燥的两口反应瓶中依次加入分子筛、无水四氢呋喃、无水三氯化铬和锰粉,搅拌至颜色变成黑色,加入1,4,5,8-四甲氧基萘-2-甲醛和三甲基氯硅烷,反应3h,加饱和碳酸氢钠淬灭反应,反应液经硅藻土、乙醚洗涤,乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压回收浓缩残留物,用四氢呋
喃溶解,加10%盐酸水解,在室温下搅拌10min,用乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压浓缩,柱层析得2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘;无水四氢呋喃、无水三氯化铬、1,4,5,8-四甲氧基萘-2-甲醛、三甲基氯硅烷、烯丙基溴、锰粉的质量配比为:30:10:60:30:80:800。
(2)聚偏氟乙烯-芳香醚类共聚物的合成:在双层玻璃反应器中依次添加聚偏氟乙烯、N,N-二甲基甲酰胺溶液,搅拌至溶液均匀后,添加Me6TREN和2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘,通氩气除氧30min,添加氯化亚铜,除氧1h,密封,将双层玻璃反应器置于冰水浴中,磁力搅拌下紫外辐照反应至预定的时间,待反应结束后用1:1的乙醇/水溶液沉析过滤,用氯仿重复多次抽提,得聚偏氟乙烯-芳香醚类共聚物,真空干燥备用;原料配比为:2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘、聚偏氟乙烯、N,N-二甲基甲酰胺、催化体系的质量配比为:60:5:550:0.1;
(3)利用脱甲基氧化法将聚偏氟乙烯-芳香醚类共聚物制成醌:
在两口反应瓶中滴加聚偏氟乙烯-芳香醚类共聚物的乙氰溶液,室温搅拌下滴加硝酸铈铵的水溶液,反应1h,减压回收乙氰,用氯仿萃取,水洗,饱和食盐水洗,无水硫酸镁干燥1.5h,减压回收氯仿,硅胶柱层析分离得2-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌和6-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌的混合物,真空干燥后备用;所述的硅胶柱层析时所用的洗脱剂为体积比为3:1的石油醚和丙酮混合溶剂;
(4)将步骤(3)的聚合物和N,N-二甲基甲酰胺按质量配比20:80制成铸膜液,刮制成膜。
应用实施例1
表1在含氮废水降解中的应用数据
以上所述仅为本发明的较佳实施例,凡依本发明申请专利范围所做的均等变化与修饰,皆应属本发明的涵盖范围。
Claims (10)
- 一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:包括以下步骤:(1)2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成;(2)聚偏氟乙烯-芳香醚类共聚物的合成:选用聚偏氟乙烯为引发剂,2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘为单体,N,N-二甲基甲酰胺为溶剂,氯化亚铜/Me6TREN为催化体系,经原子自由基聚合法合成聚偏氟乙烯-芳香醚类共聚物;(3)利用脱甲基氧化法将聚偏氟乙烯-芳香醚类共聚物脱甲氧基还原成醌;(4)将步骤(3)的聚合物和N,N-二甲基甲酰胺制成铸膜液,刮制成膜。
- 根据权利要求1所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:步骤(1)中2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成包括以下步骤:①1,4,5,8-四甲氧基萘的合成:将萘茜、催化量四丁基溴化铵、四氢呋喃加入到圆底烧瓶中,搅拌至溶解,然后添加连二亚硫酸钠水溶液和硫酸二甲酯溶液,搅拌至溶液均匀;将圆底烧瓶移至冰水浴中,反应1h,缓慢滴加NaOH水溶液,滴加完毕后移除冰水浴,在室温下反应30min,匀速搅拌18h至反应完全,反应液经乙酸乙酯萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收乙酸乙酯,柱层析分离得1,4,5,8-四甲氧基萘;②1,4,5,8-四甲氧基萘-2-甲醛的合成:在两口反应瓶中加入N,N-2-甲基乙酰胺,将两口反应瓶置于冰水浴中,依次缓慢滴加三氯氧磷和0.063mol/L1,4,5,8-四甲氧基萘的三氯甲烷溶液,滴加完毕后移除冰水浴,加热回流反应5h;然后加冰水停止反应,反应液经氯仿萃取、饱和食盐水洗涤、无水硫酸镁干燥,过滤,减压回收氯仿,柱层析分离得1,4,5,8-四甲氧基萘-2-甲醛;③2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘的合成:氩气保护下,在干燥的两口反应瓶中依次加入分子筛、无水四氢呋喃、无水三氯化铬和锰粉,搅拌至颜色变成黑色后加入烯丙基溴,搅拌至颜色变成黑色,加入1,4,5,8-四甲氧基萘-2-甲醛和三甲基氯硅烷,反应3h,加饱和碳酸氢钠淬灭反应,反应液经硅藻土、乙醚洗涤,乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压回收浓缩残留物,用四氢呋喃溶解,加10%盐酸水解,在室温下搅拌10min,用乙醚萃取,饱和食盐水洗涤,无水硫酸镁干燥,减压浓缩,柱层析得2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘。
- 根据权利要求2所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:步骤①中萘茜、四氢呋喃、连二亚硫酸钠、硫酸二甲酯、氢氧化钠的质量配比为:1.2-2:70-80:50-60:100-120:100-150。
- 根据权利要求2所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:步骤② 中N,N-2-甲基乙酰胺、三氯氧磷、1,4,5,8-四甲氧基萘的三氯甲烷溶液的体积配比为:2-3:2-5:10-25。
- 根据权利要求2所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:步骤③中无水四氢呋喃、无水三氯化铬、1,4,5,8-四甲氧基萘-2-甲醛、三甲基氯硅烷、烯丙基溴、锰粉的质量配比为:10-30:10-30:30-60:30-80:30-80:600-800。
- 根据权利要求2-5任一项所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:步骤①、步骤②、步骤③中柱层析时所用的洗脱剂均为体积比为4:1的石油醚和丙酮混合溶剂。
- 根据权利要求1所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:步骤(2)中:2-(1-羟基-3-丁烯)-1,4,5,8-四甲氧基萘、聚偏氟乙烯、N,N-二甲基甲酰胺、催化体系的质量配比为:30-60:5-12:400-550:0.1-1。
- 根据权利要求1所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:步骤(3)具体为:在两口反应瓶中滴加聚偏氟乙烯-芳香醚类共聚物的乙氰溶液,室温搅拌下滴加硝酸铈铵的水溶液,反应1h,减压回收乙氰,用氯仿萃取,水洗,饱和食盐水洗,无水硫酸镁干燥1.5h,减压回收氯仿,硅胶柱层析分离得2-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌和6-(1-羟基-3-丁烯)-5,8-二甲氧基-1,4-萘醌的混合物,真空干燥后备用。
- 根据权利要求8所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:所述的硅胶柱层析时所用的洗脱剂为体积比为3:1的石油醚和丙酮混合溶剂。
- 根据权利要求1所述的蒽醌功能化聚偏氟乙烯超滤膜的制备方法,其特征在于:步骤(4)中:N,N-二甲基甲酰胺和步骤(3)的聚合物的质量配比为:15-20:80-85。
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103394295A (zh) * | 2013-08-14 | 2013-11-20 | 哈尔滨工业大学 | 一种亲水性pvdf复合超滤膜及其制备方法 |
CN103464013A (zh) * | 2013-07-25 | 2013-12-25 | 烟台绿水赋膜材料有限公司 | 一种高性能杂化分离膜及其制备方法 |
CN104289118A (zh) * | 2013-07-15 | 2015-01-21 | 华东理工大学 | 一种原位聚合调控聚偏氟乙烯超滤膜结构的方法 |
CN105642127A (zh) * | 2016-01-13 | 2016-06-08 | 厦门理工学院 | 一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60252441A (ja) * | 1984-05-28 | 1985-12-13 | Otsuka Pharmaceut Factory Inc | ナフタレン及びナフトキノン誘導体 |
JPS63112531A (ja) * | 1986-10-29 | 1988-05-17 | Kyushu Kogyo Univ | 2−(1−ヒドロキシ−4−メチル−4−ペンテニル)−1,4,5,8−テトラメトキシナフタレンおよびその製造法 |
JPS63112530A (ja) * | 1986-10-29 | 1988-05-17 | Kyushu Kogyo Univ | 1,4,5,8−テトラメトキシナフタレンの製造法 |
KR20030069326A (ko) * | 2002-02-20 | 2003-08-27 | 주식회사 엠티티 | 폴리테트라플루오르에틸렌 물질의 화학적 표면개질 방법 |
CN1792879A (zh) * | 2005-10-29 | 2006-06-28 | 大连理工大学 | 一种固定化醌类化合物加速偶氮染料废水生物厌氧脱色方法 |
CN102140181B (zh) * | 2011-01-19 | 2013-04-17 | 天津工业大学 | 聚偏氟乙烯亲水改性膜及其制备方法 |
JP6009579B2 (ja) * | 2011-12-09 | 2016-10-19 | ナンヤン テクノロジカル ユニヴァーシティー | ポリ(フッ化ビニリデン)系ポリマーおよび少なくとも1種の導電性ポリマーのグラフトコポリマーの形成方法 |
CN103724668B (zh) * | 2014-01-07 | 2016-02-03 | 河北科技大学 | 一种蒽醌功能化纤维素膜及其制备方法 |
-
2016
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104289118A (zh) * | 2013-07-15 | 2015-01-21 | 华东理工大学 | 一种原位聚合调控聚偏氟乙烯超滤膜结构的方法 |
CN103464013A (zh) * | 2013-07-25 | 2013-12-25 | 烟台绿水赋膜材料有限公司 | 一种高性能杂化分离膜及其制备方法 |
CN103394295A (zh) * | 2013-08-14 | 2013-11-20 | 哈尔滨工业大学 | 一种亲水性pvdf复合超滤膜及其制备方法 |
CN105642127A (zh) * | 2016-01-13 | 2016-06-08 | 厦门理工学院 | 一种蒽醌功能化聚偏氟乙烯超滤膜的制备方法 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114685920A (zh) * | 2022-05-13 | 2022-07-01 | 安徽康采恩包装材料有限公司 | 一种可降解包装材料及其合成方法 |
CN114685920B (zh) * | 2022-05-13 | 2023-09-26 | 安徽康采恩包装材料有限公司 | 一种可降解包装材料及其合成方法 |
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