CN105457506A - Anti-oxidation ultrafiltration membrane and preparation method thereof - Google Patents
Anti-oxidation ultrafiltration membrane and preparation method thereof Download PDFInfo
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- 239000012528 membrane Substances 0.000 title claims abstract description 71
- 238000000108 ultra-filtration Methods 0.000 title claims abstract description 46
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 230000003064 anti-oxidating effect Effects 0.000 title abstract description 11
- 239000002033 PVDF binder Substances 0.000 claims abstract description 32
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims abstract description 32
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 15
- 239000002904 solvent Substances 0.000 claims abstract description 14
- 239000000843 powder Substances 0.000 claims abstract description 12
- 150000003973 alkyl amines Chemical class 0.000 claims abstract description 9
- -1 ester compound Chemical class 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims abstract description 7
- 239000000126 substance Substances 0.000 claims abstract description 6
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims abstract description 4
- 230000003647 oxidation Effects 0.000 claims description 74
- 238000007254 oxidation reaction Methods 0.000 claims description 74
- 239000000178 monomer Substances 0.000 claims description 32
- 230000003078 antioxidant effect Effects 0.000 claims description 13
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 10
- 150000002148 esters Chemical class 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 9
- 230000004907 flux Effects 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 238000005266 casting Methods 0.000 claims description 7
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 5
- 239000002994 raw material Substances 0.000 claims description 5
- AICNZRYBCUSVMO-UHFFFAOYSA-M trimethyl(tridecyl)azanium;bromide Chemical compound [Br-].CCCCCCCCCCCCC[N+](C)(C)C AICNZRYBCUSVMO-UHFFFAOYSA-M 0.000 claims description 5
- 238000004821 distillation Methods 0.000 claims description 4
- 238000004132 cross linking Methods 0.000 claims description 2
- DDXLVDQZPFLQMZ-UHFFFAOYSA-M dodecyl(trimethyl)azanium;chloride Chemical compound [Cl-].CCCCCCCCCCCC[N+](C)(C)C DDXLVDQZPFLQMZ-UHFFFAOYSA-M 0.000 claims description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 2
- 229910052736 halogen Inorganic materials 0.000 claims description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 150000002989 phenols Chemical class 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 241000555268 Dendroides Species 0.000 claims 3
- YWFWDNVOPHGWMX-UHFFFAOYSA-N n,n-dimethyldodecan-1-amine Chemical compound CCCCCCCCCCCCN(C)C YWFWDNVOPHGWMX-UHFFFAOYSA-N 0.000 claims 2
- 240000006927 Foeniculum vulgare Species 0.000 claims 1
- 235000004204 Foeniculum vulgare Nutrition 0.000 claims 1
- AUBSNUSTVUZGCC-UHFFFAOYSA-N [NH4+].[Br-].C(C)[PH3+].[Br-] Chemical compound [NH4+].[Br-].C(C)[PH3+].[Br-] AUBSNUSTVUZGCC-UHFFFAOYSA-N 0.000 claims 1
- GCKVRHFRDJAIGL-UHFFFAOYSA-M [NH4+].[Br-].C(CCCCCCCCCCC)[P+](CC)(C)C.[Br-] Chemical compound [NH4+].[Br-].C(CCCCCCCCCCC)[P+](CC)(C)C.[Br-] GCKVRHFRDJAIGL-UHFFFAOYSA-M 0.000 claims 1
- 125000001309 chloro group Chemical group Cl* 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 230000006837 decompression Effects 0.000 claims 1
- PLMFYJJFUUUCRZ-UHFFFAOYSA-M decyltrimethylammonium bromide Chemical compound [Br-].CCCCCCCCCC[N+](C)(C)C PLMFYJJFUUUCRZ-UHFFFAOYSA-M 0.000 claims 1
- 150000005205 dihydroxybenzenes Chemical class 0.000 claims 1
- XWBDWHCCBGMXKG-UHFFFAOYSA-N ethanamine;hydron;chloride Chemical compound Cl.CCN XWBDWHCCBGMXKG-UHFFFAOYSA-N 0.000 claims 1
- 125000005843 halogen group Chemical group 0.000 claims 1
- WFKAJVHLWXSISD-UHFFFAOYSA-N isobutyramide Chemical compound CC(C)C(N)=O WFKAJVHLWXSISD-UHFFFAOYSA-N 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 238000006116 polymerization reaction Methods 0.000 claims 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 claims 1
- 230000007704 transition Effects 0.000 claims 1
- 229920002873 Polyethylenimine Polymers 0.000 abstract description 26
- 239000000463 material Substances 0.000 abstract description 10
- 238000000354 decomposition reaction Methods 0.000 abstract description 3
- 238000007259 addition reaction Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 16
- 235000006708 antioxidants Nutrition 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- 238000011426 transformation method Methods 0.000 description 7
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 6
- 229910052801 chlorine Inorganic materials 0.000 description 6
- 239000000460 chlorine Substances 0.000 description 6
- 230000003247 decreasing effect Effects 0.000 description 6
- 230000001590 oxidative effect Effects 0.000 description 6
- BGNXCDMCOKJUMV-UHFFFAOYSA-N Tert-Butylhydroquinone Chemical compound CC(C)(C)C1=CC(O)=CC=C1O BGNXCDMCOKJUMV-UHFFFAOYSA-N 0.000 description 5
- 230000032683 aging Effects 0.000 description 5
- XJWSAJYUBXQQDR-UHFFFAOYSA-M dodecyltrimethylammonium bromide Chemical compound [Br-].CCCCCCCCCCCC[N+](C)(C)C XJWSAJYUBXQQDR-UHFFFAOYSA-M 0.000 description 5
- 239000004250 tert-Butylhydroquinone Substances 0.000 description 5
- 235000019281 tert-butylhydroquinone Nutrition 0.000 description 5
- ZDAHQDGJYAANRH-UHFFFAOYSA-M ethyl-dimethyl-tetradecylazanium;bromide Chemical compound [Br-].CCCCCCCCCCCCCC[N+](C)(C)CC ZDAHQDGJYAANRH-UHFFFAOYSA-M 0.000 description 4
- 239000000499 gel Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000007800 oxidant agent Substances 0.000 description 4
- FFGSPQDSOUPWGY-UHFFFAOYSA-M dodecyl-ethyl-dimethylazanium;bromide Chemical compound [Br-].CCCCCCCCCCCC[N+](C)(C)CC FFGSPQDSOUPWGY-UHFFFAOYSA-M 0.000 description 3
- VIPWBDNNTAIYFL-UHFFFAOYSA-M ethyl-dimethyl-tetradecylazanium;chloride Chemical compound [Cl-].CCCCCCCCCCCCCC[N+](C)(C)CC VIPWBDNNTAIYFL-UHFFFAOYSA-M 0.000 description 3
- 239000003292 glue Substances 0.000 description 3
- 238000007790 scraping Methods 0.000 description 3
- 238000005292 vacuum distillation Methods 0.000 description 3
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229920000110 poly(aryl ether sulfone) Polymers 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- CZBZUDVBLSSABA-UHFFFAOYSA-N butylated hydroxyanisole Chemical compound COC1=CC=C(O)C(C(C)(C)C)=C1.COC1=CC=C(O)C=C1C(C)(C)C CZBZUDVBLSSABA-UHFFFAOYSA-N 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 239000000412 dendrimer Substances 0.000 description 1
- 229920000736 dendritic polymer Polymers 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- PHAFDKCRJVKSSR-UHFFFAOYSA-N ethene hydrofluoride Chemical group F.C=C PHAFDKCRJVKSSR-UHFFFAOYSA-N 0.000 description 1
- 230000005281 excited state Effects 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 150000002367 halogens Chemical group 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- IJAPPYDYQCXOEF-UHFFFAOYSA-N phthalazin-1(2H)-one Chemical group C1=CC=C2C(=O)NN=CC2=C1 IJAPPYDYQCXOEF-UHFFFAOYSA-N 0.000 description 1
- 229920006260 polyaryletherketone Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
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
- B01D71/06—Organic material
- B01D71/30—Polyalkenyl halides
- B01D71/32—Polyalkenyl halides containing fluorine atoms
- B01D71/34—Polyvinylidene fluoride
-
- 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
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0013—Casting processes
-
- 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
- B01D2325/00—Details relating to properties of membranes
- B01D2325/30—Chemical resistance
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本发明属于材料制备领域,更具体地说,涉及一种耐氧化超滤膜及其制备方法。The invention belongs to the field of material preparation, and more specifically relates to an oxidation-resistant ultrafiltration membrane and a preparation method thereof.
背景技术Background technique
目前采用最多的超滤膜为PVDF材质。传统膜材料行业提升的是膜的亲水性和高通量,但是随着水质要求和回用水比例日益提高,氧化等物化预处理手段也在不断加强,导致对超滤膜的耐氧化性要求也越来越高。Currently, the most widely used ultrafiltration membrane is made of PVDF. The traditional membrane material industry is improving the hydrophilicity and high flux of the membrane. However, with the increasing water quality requirements and the proportion of reused water, physical and chemical pretreatment methods such as oxidation are also continuously strengthened, resulting in the requirement for oxidation resistance of ultrafiltration membranes. Also getting higher and higher.
目前,已有文献和专利报道通过向PVDF材质中加入耐氧化材料,从而达到提高膜耐氧化性能的目的。例如,中国专利申请号为CN201310097069,申请公开日为2013年03月25日的专利申请文件公开了一种掺杂聚乙烯醇缩甲醛层和聚联丙烯邻苯二甲酸酯层提升膜材料耐氧化剂性能。中国专利申请号为CN200910220545,申请公开日为2009年12月01日的专利申请文件(公开号CN101721927B)公开了一种掺杂二氮杂萘酮结构共聚芳醚砜提升膜材料耐氧化剂性能。中国专利申请号为CN200510011473,申请公开日为2005年03月25日的专利申请文件(公开号CN1695778B)公开了一种掺杂聚芳醚砜或聚芳醚酮提升膜材料耐氧化剂性能。At present, there are existing literature and patent reports that the purpose of improving the oxidation resistance of the membrane is achieved by adding oxidation-resistant materials to the PVDF material. For example, the Chinese patent application number is CN201310097069, and the patent application document with the application publication date of March 25, 2013 discloses a doped polyvinyl formal layer and polypropylene phthalate layer to improve the resistance of the film material. Oxidizing properties. The Chinese patent application number is CN200910220545, and the patent application document (publication number CN101721927B) with the application publication date of December 1, 2009 discloses a doped phthalazinone structure copolymerized polyarylethersulfone to improve the oxidation resistance of the membrane material. The Chinese patent application number is CN200510011473, and the patent application document (publication number CN1695778B) with the application publication date of March 25, 2005 discloses a doped polyarylethersulfone or polyaryletherketone to improve the oxidation resistance of the membrane material.
但是在PVDF中掺杂树枝状聚乙烯亚胺、长链烷基胺类物质和酚类或酯类化合物的复配耐氧化剂,制备耐氧化超滤膜的方法还未见报道。However, the method of preparing oxidation-resistant ultrafiltration membranes by doping dendritic polyethyleneimine, long-chain alkylamines, and phenols or esters in PVDF has not been reported.
发明内容Contents of the invention
1.要解决的问题1. The problem to be solved
针对现有超滤膜在高氧化性水体使用过程中易氧化的问题,本发明提供一种耐氧化超滤膜及其制备方法。Aiming at the problem that the existing ultrafiltration membrane is easily oxidized during use in highly oxidative water bodies, the invention provides an oxidation-resistant ultrafiltration membrane and a preparation method thereof.
2.技术方案2. Technical solution
为了解决现有技术中的问题,本发明所制备的超滤膜的原料的主要组分包括PVDF粉体、溶剂和耐氧化剂,具体地,本发明的技术方案如下:In order to solve the problems in the prior art, the main components of the raw material of the ultrafiltration membrane prepared by the present invention include PVDF powder, solvent and anti-oxidant, specifically, the technical scheme of the present invention is as follows:
一种耐氧化超滤膜,制备该耐氧化超滤膜的原料的主要组分及各主要组分的重量份数为:PVDF粉体:100份;溶剂:40-60份;耐氧化剂:0.5-1份。An oxidation-resistant ultrafiltration membrane, the main components of the raw materials for preparing the oxidation-resistant ultrafiltration membrane and the parts by weight of each main component are: PVDF powder: 100 parts; solvent: 40-60 parts; oxidation resistance: 0.5 -1 copy.
优选地,所述的溶剂是二甲基乙酰胺、二甲基甲酰胺、二甲基亚砜或N-甲基吡咯烷酮中的一种或多种。Preferably, the solvent is one or more of dimethylacetamide, dimethylformamide, dimethylsulfoxide or N-methylpyrrolidone.
优选地,所述的耐氧化剂由单体A、单体B和单体C交联共聚而成,其中单体A为树枝状聚乙烯亚胺;单体B为长链烷基胺类物质;单体C为酚类或酯类化合物。Preferably, the oxidation resistance is formed by cross-linking and copolymerizing monomer A, monomer B and monomer C, wherein monomer A is dendritic polyethyleneimine; monomer B is a long-chain alkylamine; Monomer C is a phenolic or ester compound.
优选地,所述的树枝状聚乙烯亚胺的结构式为:Preferably, the structural formula of the dendritic polyethyleneimine is:
其中,n为100-1000,树枝状聚乙烯亚胺的分子量为50000-500000。Wherein, n is 100-1000, and the molecular weight of dendritic polyethyleneimine is 50000-500000.
优选地,所述的长链烷基胺类物质的结构式为:Preferably, the structural formula of the long-chain alkylamines is:
式中,m为10-12,R为甲基或乙基,X为卤素元素。In the formula, m is 10-12, R is methyl or ethyl, and X is a halogen element.
优选地,所述的长链烷基胺类物质为十二烷基三甲基氯化铵、十二烷基三甲基溴化铵、十二烷基二甲基乙基溴化铵、十四烷基二甲基乙基溴化铵、十四烷基二甲基乙基氯化铵、十三烷基三甲基溴化铵等中的一种或几种;所述的单体C为丁基羟基茴香酚、四季戊四醇酯和叔丁基对二苯二酚中的一种。Preferably, the long-chain alkylamines are dodecyltrimethylammonium chloride, dodecyltrimethylammonium bromide, dodecyldimethylethylammonium bromide, One or more of tetraalkyldimethylethylammonium bromide, tetradecyldimethylethylammonium chloride, tridecyltrimethylammonium bromide, etc.; the monomer C It is one of butyl hydroxyanisole, tetraerythritol ester and tert-butyl hydroquinone.
上述的一种耐氧化超滤膜的制备方法,具体的制备步骤为:The above-mentioned preparation method of an oxidation-resistant ultrafiltration membrane, the specific preparation steps are:
(1)按比例将单体A、单体B和单体C反应制备耐氧化剂;(1) react monomer A, monomer B and monomer C in proportion to prepare oxidation resistance;
(2)按比例将PVDF粉体溶解于溶剂中,加入耐氧化剂,搅拌均匀,脱泡熟化后,采用传统相转变法将铸膜液静置、凝胶、刮膜,即可合成聚偏氟乙烯超滤膜。(2) Dissolve PVDF powder in a solvent in proportion, add anti-oxidant, stir evenly, after defoaming and curing, use the traditional phase transformation method to stand, gel, and scrape the casting liquid to synthesize polyvinylidene fluoride Ethylene ultrafiltration membrane.
优选地,步骤(1)中耐氧化剂的制备方法为:将单体A、单体B和单体C在反应釜中发生聚合反应,反应温度为40~80℃,反应时间为24~48h;反应结束后减压蒸馏即可得到所述的耐氧化剂。Preferably, the preparation method of oxidant resistance in step (1) is as follows: polymerize monomer A, monomer B and monomer C in a reactor, the reaction temperature is 40-80°C, and the reaction time is 24-48 hours; After the reaction is finished, the oxidation resistance can be obtained by distillation under reduced pressure.
优选地,单体A、单体B和单体C的摩尔比为1:(0.1-0.4):(0.01-0.05)。Preferably, the molar ratio of monomer A, monomer B and monomer C is 1:(0.1-0.4):(0.01-0.05).
聚乙烯亚胺(PEI)是一种高分子有机物,通常具有直线状和树枝状两种形式,是正电荷密度最大的一类高分子有机物之一;同时树枝状结构能够起到交联剂的作用,可以与其它高分子形成高交联空间网状结构,该结构分子量大、性能稳定、不易流失,能够稳定地存在于PVDF中。但是目前,通过将PEI这种树枝状高分子交联剂应用于PVDF超滤膜的制备中尚未见文献报道,本发明独创的将树枝状聚乙烯亚胺和长链烷基胺类物质及酚类或酯类化合物反应制备得到一种空间高交联网状结构的耐氧化剂,并将这种耐氧化剂作为超滤膜的添加剂制备得到一种耐氧化的超滤膜。本发明中合成的改性PVDF超滤膜具有制备过程简单,所需原料种类少,产品合格率高等优点,同时其耐氧化性能明显。Polyethyleneimine (PEI) is a kind of high-molecular organic matter, which usually has two forms: linear and dendritic. , can form a highly cross-linked space network structure with other polymers, the structure has a large molecular weight, stable performance, and is not easy to be lost, and can stably exist in PVDF. However, at present, there is no literature report on the application of PEI, a dendritic polymer crosslinking agent, in the preparation of PVDF ultrafiltration membranes. The oxidation resistance of a space highly cross-linked network structure is prepared by reacting the class or ester compound, and an oxidation resistance ultrafiltration membrane is prepared by using the oxidation resistance as an additive of the ultrafiltration membrane. The modified PVDF ultrafiltration membrane synthesized in the invention has the advantages of simple preparation process, less types of raw materials required, high product qualified rate, etc., and meanwhile, its oxidation resistance is obvious.
3.有益效果3. Beneficial effect
(1)本发明合成的耐氧化剂为空间高交联网状结构,能够稳定的存在于PVDF中,不易流失,具有较好的耐氧化性能;(1) The oxidation resistance synthesized by the present invention is a space highly cross-linked network structure, which can be stably present in PVDF, is not easy to be lost, and has good oxidation resistance;
(2)本发明合成的耐氧化剂中长链烷烃胺类物质能够中和及吸附PVDF分解过程中释放的HCl,并与形成的双键进行加成反应,从而提高PVDF材质的抗氧化性能;(2) The oxidant-resistant medium-long-chain alkane amines synthesized by the present invention can neutralize and absorb the HCl released during the decomposition process of PVDF, and perform addition reaction with the formed double bond, thereby improving the oxidation resistance of PVDF material;
(3)本发明合成过程中产生的C=C双键和以及酚类功能基团还可以吸收和屏蔽部分紫外光区的有害能量,捕捉由紫外光激发的活性自由基,猝灭激发态分子,分解紫外光产生的过氧化物,因此,本发明的耐氧化曝气软管具有抗氧化能力强、使用寿命长等优点;(3) The C=C double bonds and phenolic functional groups produced in the synthesis process of the present invention can also absorb and shield part of the harmful energy in the ultraviolet region, capture active free radicals excited by ultraviolet light, and quench excited state molecules , to decompose peroxides produced by ultraviolet light, therefore, the oxidation-resistant aeration hose of the present invention has the advantages of strong oxidation resistance and long service life;
(4)本发明所制备的耐氧化超滤膜合成工艺简单,原料价廉易得,成品率高,性能优良、环保。(4) The oxidation-resistant ultrafiltration membrane prepared by the present invention has simple synthesis process, cheap and easy-to-obtain raw materials, high yield, excellent performance and environmental protection.
具体实施方式detailed description
下面结合具体实施例对本发明进一步进行描述。The present invention will be further described below in conjunction with specific embodiments.
实施例1Example 1
一种耐氧化超滤膜的制备方法为:A preparation method of an oxidation-resistant ultrafiltration membrane is as follows:
步骤(1):按摩尔比例为1:0.1:0.01取分子量为50000-100000范围的PEI(称量后配制成水溶液,以下简称PEI溶液)、十二烷基三甲基溴化铵和丁基羟基茴香酚,将十二烷基三甲基溴化铵和丁基羟基茴香酚置于反应釜,向其中缓慢滴加PEI溶液,加热至80℃混合反应24h,反应结束后通过减压蒸馏得到耐氧化剂;Step (1): Take PEI with a molecular weight of 50,000-100,000 in the molar ratio of 1:0.1:0.01 (weighed to prepare an aqueous solution, hereinafter referred to as PEI solution), dodecyltrimethylammonium bromide and butyl Hydroxyanishol, put dodecyltrimethylammonium bromide and butylhydroxyanishol in a reaction kettle, slowly add PEI solution dropwise to it, heat to 80°C and mix for 24 hours, after the reaction is completed, it can be obtained by vacuum distillation Oxidant resistance;
步骤(2):取PVDF粉体:100份;溶剂二甲基乙酰胺:40份;耐氧化剂:0.5份,搅拌均匀,脱泡熟化后,采用传统相转变法将铸膜液静置、凝胶、刮膜,即可合成耐氧化聚偏氟乙烯超滤膜。Step (2): Take PVDF powder: 100 parts; solvent dimethylacetamide: 40 parts; anti-oxidant: 0.5 parts, stir evenly, after defoaming and aging, use the traditional phase transformation method to let the casting liquid stand still and coagulate Glue and scraping membrane can be used to synthesize oxidation-resistant polyvinylidene fluoride ultrafiltration membrane.
将本实施例中制备的耐氧化超滤膜用于氧化试验,将耐氧化超滤膜放置于余氯为10000mg/L的回用水中运行90天,膜通量降低1%,表明耐氧化超滤膜的抗氧化性能好。The oxidation-resistant ultrafiltration membrane prepared in this example was used in the oxidation test, and the oxidation-resistant ultrafiltration membrane was placed in the recycled water with residual chlorine of 10000 mg/L to run for 90 days, and the membrane flux decreased by 1%, indicating that the oxidation-resistant ultrafiltration membrane The anti-oxidation performance of the filter membrane is good.
实施例2Example 2
本实例其它条件同实施例1,不同之处在于:Other conditions of this instance are the same as embodiment 1, and the difference is:
步骤(1)中按摩尔比例为1:0.2:0.03取分子量为100000-500000范围的PEI(称量后配制成水溶液,以下简称PEI溶液)、十二烷基三甲基溴化铵和四季戊四醇酯,将十二烷基三甲基溴化铵和四季戊四醇酯置于反应釜中,向其中缓慢滴加PEI溶液,加热至40℃混合反应48h,反应结束后通过减压蒸馏得到耐氧化剂;In the step (1), the molar ratio is 1:0.2:0.03 to take PEI with a molecular weight of 100,000-500,000 range (formed into an aqueous solution after weighing, hereinafter referred to as PEI solution), dodecyltrimethylammonium bromide and tetraerythritol Esters, put dodecyltrimethylammonium bromide and tetraerythritol ester in a reaction kettle, slowly drop PEI solution into it, heat to 40°C and mix and react for 48h, and obtain oxidation resistance by vacuum distillation after the reaction;
步骤(2)取PVDF粉体:100份;溶剂二甲基甲酰胺:60份;耐氧化剂:1份,搅拌均匀,脱泡熟化后,采用传统相转变法将铸膜液静置、凝胶、刮膜,即可合成耐氧化聚偏氟乙烯超滤膜。Step (2) Take PVDF powder: 100 parts; solvent dimethylformamide: 60 parts; anti-oxidant: 1 part, stir evenly, after defoaming and aging, use the traditional phase transformation method to let the casting solution stand still and gel , Scrape the membrane to synthesize an oxidation-resistant polyvinylidene fluoride ultrafiltration membrane.
将本实施例中制备的耐氧化超滤膜用于氧化试验,将耐氧化超滤膜放置于余氯为15000mg/L的回用水中运行70天,膜通量降低0.8%,表明耐氧化超滤膜的抗氧化性能好。The oxidation-resistant ultrafiltration membrane prepared in this example was used in the oxidation test, and the oxidation-resistant ultrafiltration membrane was placed in the recycled water with residual chlorine of 15000 mg/L to run for 70 days, and the membrane flux decreased by 0.8%, indicating that the oxidation-resistant ultrafiltration membrane The anti-oxidation performance of the filter membrane is good.
实施例3Example 3
本实例其它条件同实施例1,不同之处在于:Other conditions of this instance are the same as embodiment 1, and the difference is:
步骤(1)中按摩尔比例为1:0.4:0.05取分子量为300000-500000范围的PEI(称量后配制成水溶液,以下简称PEI溶液)、十二烷基二甲基乙基溴化铵和叔丁基对二苯二酚,将十二烷基二甲基乙基溴化铵和叔丁基对二苯二酚置于反应釜,向其中缓慢滴加PEI溶液,加热至50℃混合反应36h,反应结束后通过减压蒸馏即可得到耐氧化剂;In the step (1), the molar ratio is 1:0.4:0.05 to take PEI (weighed to be prepared as an aqueous solution, hereinafter referred to as PEI solution), dodecyldimethylethylammonium bromide and For tert-butyl hydroquinone, put dodecyldimethylethylammonium bromide and tert-butyl hydroquinone in a reaction kettle, slowly add PEI solution dropwise, heat to 50°C for mixed reaction 36h, the oxidation resistance can be obtained by vacuum distillation after the reaction;
步骤(2)取PVDF粉体:100份;溶剂(二甲基亚砜:N-甲基吡咯烷酮=1:1):60份;耐氧化剂:0.6份,搅拌均匀,脱泡熟化后,采用传统相转变法将铸膜液静置、凝胶、刮膜,即可合成耐氧化聚偏氟乙烯超滤膜。Step (2) Take PVDF powder: 100 parts; solvent (dimethyl sulfoxide: N-methylpyrrolidone = 1:1): 60 parts; anti-oxidant: 0.6 parts, stir evenly, after defoaming and curing, use traditional The phase transformation method puts the cast membrane solution to rest, gels, and scrapes the membrane to synthesize an oxidation-resistant polyvinylidene fluoride ultrafiltration membrane.
将本实施例中制备的耐氧化超滤膜用于氧化试验,将耐氧化超滤膜放置于余氯为12000mg/L的回用水中运行80天,膜通量降低0.9%,表明耐氧化超滤膜的抗氧化性能好。The oxidation-resistant ultrafiltration membrane prepared in this example was used in the oxidation test, and the oxidation-resistant ultrafiltration membrane was placed in the recycled water with residual chlorine of 12000mg/L to run for 80 days, and the membrane flux decreased by 0.9%, indicating that the oxidation-resistant ultrafiltration membrane The anti-oxidation performance of the filter membrane is good.
实施例4Example 4
本实例其它条件同实施例1,不同之处在于:Other conditions of this instance are the same as embodiment 1, and the difference is:
步骤(1)中按摩尔比例为1:0.2:0.02取分子量为400000-500000范围的PEI(称量后配制成水溶液,以下简称PEI溶液)、十四烷基二甲基乙基叔胺和叔丁基对二苯二酚,将十四烷基二甲基乙基溴化铵和叔丁基对二苯二酚置于反应釜,向其中缓慢滴加PEI溶液,加热至45℃混合反应42h,反应结束后通过减压蒸馏即可得到耐氧化剂;In step (1), the molar ratio is 1:0.2:0.02 to take PEI with a molecular weight of 400,000-500,000 (weighed to prepare an aqueous solution, hereinafter referred to as PEI solution), tetradecyldimethylethyl tertiary amine and tertiary Butyl hydroquinone, place tetradecyl dimethyl ethyl ammonium bromide and tert-butyl hydroquinone in a reaction kettle, slowly add PEI solution dropwise, heat to 45°C and mix for 42 hours , after the reaction, the oxidation resistance can be obtained by distillation under reduced pressure;
步骤(2)取PVDF粉体:100份;溶剂二甲基亚砜:50份;耐氧化剂:0.7份,搅拌均匀,脱泡熟化后,采用传统相转变法将铸膜液静置、凝胶、刮膜,即可合成耐氧化聚偏氟乙烯超滤膜。Step (2) Take PVDF powder: 100 parts; solvent dimethyl sulfoxide: 50 parts; anti-oxidant: 0.7 parts, stir evenly, after defoaming and aging, use the traditional phase transformation method to let the casting solution stand still and gel , Scrape the membrane to synthesize an oxidation-resistant polyvinylidene fluoride ultrafiltration membrane.
将本实施例中制备的耐氧化超滤膜用于氧化试验,将耐氧化超滤膜放置于余氯为11000mg/L的回用水中运行100天,膜通量降低0.6%,表明耐氧化超滤膜的抗氧化性能好。The oxidation-resistant ultrafiltration membrane prepared in this example was used in the oxidation test, and the oxidation-resistant ultrafiltration membrane was placed in the recycled water with residual chlorine of 11000 mg/L to run for 100 days, and the membrane flux decreased by 0.6%, indicating that the oxidation-resistant ultrafiltration membrane The anti-oxidation performance of the filter membrane is good.
实施例5Example 5
本实例其它条件同实施例1,不同之处在于:Other conditions of this instance are the same as embodiment 1, and the difference is:
步骤(1)中按摩尔比例为1:0.1:0.02取分子量为50000-500000范围的PEI(称量后配制成水溶液,以下简称PEI溶液)、十四烷基二甲基乙基氯化铵和四季戊四醇酯,将十四烷基二甲基乙基氯化铵和四季戊四醇酯置于反应釜,向其中缓慢滴加PEI溶液,加热至52℃混合反应28h,反应结束后通过减压蒸馏即可得到耐氧化剂;In the step (1), the molar ratio is 1:0.1:0.02 to take PEI (weighed to be prepared as an aqueous solution, hereinafter referred to as PEI solution), tetradecyldimethylethylammonium chloride and Tetraerythritol ester, tetradecyl dimethyl ethyl ammonium chloride and tetraerythritol ester are placed in a reaction kettle, slowly drop PEI solution into it, heat to 52°C and mix for 28 hours. Oxidant resistance can be obtained;
步骤(2)中取PVDF粉体:100份;溶剂N-甲基吡咯烷酮:60份;耐氧化剂:0.5份,搅拌均匀,脱泡熟化后,采用传统相转变法将铸膜液静置、凝胶、刮膜,即可合成耐氧化聚偏氟乙烯超滤膜。Take PVDF powder in step (2): 100 parts; solvent N-methylpyrrolidone: 60 parts; anti-oxidant: 0.5 parts, stir evenly, after defoaming and aging, use the traditional phase transformation method to let the casting liquid stand still and solidify Glue and scraping membrane can be used to synthesize oxidation-resistant polyvinylidene fluoride ultrafiltration membrane.
将本实施例中制备的耐氧化超滤膜用于氧化试验,将耐氧化超滤膜放置于余氯为16000mg/L的回用水中运行90天,膜通量降低1%,表明耐氧化超滤膜的抗氧化性能好。The oxidation-resistant ultrafiltration membrane prepared in this example was used in the oxidation test, and the oxidation-resistant ultrafiltration membrane was placed in the recycled water with residual chlorine of 16000 mg/L to run for 90 days, and the membrane flux decreased by 1%, indicating that the oxidation-resistant ultrafiltration membrane The anti-oxidation performance of the filter membrane is good.
实施例6Example 6
本实例其它条件同实施例1,不同之处在于:Other conditions of this instance are the same as embodiment 1, and the difference is:
步骤(1)中按摩尔比例为1:0.3:0.04取分子量为400000-500000范围的PEI(称量后配制成水溶液,以下简称PEI溶液)、十四烷基二甲基乙基溴化铵和十三烷基三甲基溴化铵混合物、四季戊四醇酯,将十四烷基二甲基乙基溴化铵和十三烷基三甲基溴化铵混合物、四季戊四醇酯置于反应釜中,向其中缓慢滴加PEI溶液,加热至45℃混合反应42h,其中,十四烷基二甲基乙基溴化铵和十三烷基三甲基溴化铵摩尔比例为1:1,反应结束后通过减压蒸馏即可得到耐氧化剂;In the step (1), the molar ratio is 1:0.3:0.04 to get PEI (weighed to be prepared as an aqueous solution, hereinafter referred to as PEI solution), Tetradecyldimethylethylammonium bromide and Tridecyl trimethyl ammonium bromide mixture, tetraerythritol ester, tetradecyl dimethyl ethyl ammonium bromide and tridecyl trimethyl ammonium bromide mixture, tetraerythritol ester are placed in the reaction kettle , slowly drop the PEI solution therein, heat to 45°C and mix for 42h, wherein the molar ratio of tetradecyldimethylethylammonium bromide and tridecyltrimethylammonium bromide is 1:1, and the reaction After the end, the oxidation resistance can be obtained by distillation under reduced pressure;
步骤(2)中取PVDF粉体:100份;溶剂N-甲基吡咯烷酮:50份;耐氧化剂:0.6份,搅拌均匀,脱泡熟化后,采用传统相转变法将铸膜液静置、凝胶、刮膜,即可合成耐氧化聚偏氟乙烯超滤膜。Take PVDF powder in step (2): 100 parts; solvent N-methylpyrrolidone: 50 parts; oxidation resistance: 0.6 parts, stir evenly, after defoaming and aging, use the traditional phase transformation method to let the casting liquid stand still and solidify Glue and scraping membrane can be used to synthesize oxidation-resistant polyvinylidene fluoride ultrafiltration membrane.
将本实施例中制备的耐氧化超滤膜用于氧化试验,将耐氧化超滤膜放置于余氯为14000mg/L的回用水中运行70天,膜通量降低0.6%,表明耐氧化超滤膜的抗氧化性能好。The oxidation-resistant ultrafiltration membrane prepared in this example was used in the oxidation test, and the oxidation-resistant ultrafiltration membrane was placed in the recycled water with residual chlorine of 14000 mg/L to run for 70 days, and the membrane flux decreased by 0.6%, indicating that the oxidation-resistant ultrafiltration membrane The anti-oxidation performance of the filter membrane is good.
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US20060049102A1 (en) * | 2004-09-03 | 2006-03-09 | Miller Jeffrey T | Ionic polymer membranes |
CN104174299A (en) * | 2014-07-30 | 2014-12-03 | 中国海洋大学 | High-flux positive osmosis membrane based on ultrathin support layer and preparation method thereof |
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