CN105749981B - A kind of CNT/zinc oxide PTFE film and preparation method thereof - Google Patents
A kind of CNT/zinc oxide PTFE film and preparation method thereof Download PDFInfo
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- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 title claims abstract description 104
- 239000011787 zinc oxide Substances 0.000 title claims abstract description 53
- 229920001343 polytetrafluoroethylene Polymers 0.000 title claims abstract description 45
- 239000004810 polytetrafluoroethylene Substances 0.000 title claims abstract description 45
- 238000002360 preparation method Methods 0.000 title claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 58
- 239000002041 carbon nanotube Substances 0.000 claims abstract description 58
- 229910021393 carbon nanotube Inorganic materials 0.000 claims abstract description 58
- 239000012528 membrane Substances 0.000 claims abstract description 32
- 230000001699 photocatalysis Effects 0.000 claims abstract description 21
- 239000002131 composite material Substances 0.000 claims abstract description 16
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 12
- 239000011701 zinc Substances 0.000 claims abstract description 8
- 238000005245 sintering Methods 0.000 claims abstract description 4
- 238000006243 chemical reaction Methods 0.000 claims abstract description 3
- 238000001035 drying Methods 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 238000003756 stirring Methods 0.000 claims description 9
- 239000002253 acid Substances 0.000 claims description 8
- -1 polytetrafluoroethylene Polymers 0.000 claims description 7
- 239000011941 photocatalyst Substances 0.000 claims description 6
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 4
- 239000003960 organic solvent Substances 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 3
- 238000010907 mechanical stirring Methods 0.000 claims description 3
- 125000000896 monocarboxylic acid group Chemical group 0.000 claims description 3
- 229910017604 nitric acid Inorganic materials 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000011259 mixed solution Substances 0.000 claims description 2
- 238000013033 photocatalytic degradation reaction Methods 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 3
- 239000002957 persistent organic pollutant Substances 0.000 abstract description 3
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 description 13
- 230000000694 effects Effects 0.000 description 7
- 238000000926 separation method Methods 0.000 description 6
- 238000004065 wastewater treatment Methods 0.000 description 6
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 5
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 229910010413 TiO 2 Inorganic materials 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000000575 pesticide Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- ZOIORXHNWRGPMV-UHFFFAOYSA-N acetic acid;zinc Chemical compound [Zn].CC(O)=O.CC(O)=O ZOIORXHNWRGPMV-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000003760 magnetic stirring Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 238000001782 photodegradation Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004246 zinc acetate Substances 0.000 description 1
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
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- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/39—Photocatalytic properties
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- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/58—Fabrics or filaments
- B01J35/59—Membranes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/10—Photocatalysts
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Abstract
本发明公开一种碳纳米管/氧化锌PTFE光催化膜的制备方法,先将酸化的碳纳米管与Zn(CH3COO)2充分混合,调节pH为碱性后,经过高温反应、过滤、洗涤、烘干得到碳纳米管/氧化锌复合材料,然后将碳纳米管/氧化锌复合材料与PTFE置于模具中,经冷压成型、高温烧结,得到碳纳米管/氧化锌PTFE光催化膜。本发明制得的碳纳米管/氧化锌PTFE光催化膜不仅延长了PTFE膜的使用寿命,而且增强了ZnO的光催化降解有机污染物的性能。本发明工艺设备简单,易于规模生产,有很大的市场前景。
The invention discloses a method for preparing a carbon nanotube/zinc oxide PTFE photocatalytic film. Firstly, fully mix acidified carbon nanotubes and Zn(CH 3 COO) 2 , adjust the pH to be alkaline, and then undergo high-temperature reaction, filtration, Washing and drying to obtain the carbon nanotube/zinc oxide composite material, then put the carbon nanotube/zinc oxide composite material and PTFE into the mold, cold press forming, high temperature sintering, and obtain the carbon nanotube/zinc oxide PTFE photocatalytic film . The carbon nanotube/zinc oxide PTFE photocatalytic membrane prepared by the invention not only prolongs the service life of the PTFE membrane, but also enhances the performance of ZnO photocatalytic degradation of organic pollutants. The process equipment of the invention is simple, easy for large-scale production, and has great market prospect.
Description
技术领域technical field
本发明涉及一种碳纳米管/氧化锌PTFE光催化膜及其制备方法,属于复合材料技术领域。The invention relates to a carbon nanotube/zinc oxide PTFE photocatalytic film and a preparation method thereof, belonging to the technical field of composite materials.
背景技术Background technique
在水资源日益匮乏的今天,对污水的处理引起了人们广泛的重视。膜分离技术是20世纪初出现,在20世纪60年代后快速发展为一门新的水处理技术。由于其兼有分离、浓缩和纯化等功能,又具备高效、节能、环保过滤及过滤过程简单、易于控制等特征,膜分离技术已在生物、环保等领域得到了广泛的应用,成为分离科学中最重要的手段之一。PTFE膜以聚四氟乙烯为原材料,透气不透水、通气量大、耐高温、抗强酸、无毒,在膜分离技术中扮演着重要的角色。但是单独将PTFE膜应用于农药废水处理过程中,只能对农药废水进行物理分离 ,并没有有效地去除废水中的污染物质,而且PTFE膜在长时间运行中会受到污染,从而降低了分离的效果。因此,找到一种将有机废水无害化的方法变得尤为重要。In today's increasingly scarce water resources, the treatment of sewage has aroused widespread attention. Membrane separation technology appeared in the early 20th century, and developed rapidly into a new water treatment technology after the 1960s. Due to its functions of separation, concentration and purification, as well as high efficiency, energy saving, environmental protection and filtration, and the filtration process is simple and easy to control, membrane separation technology has been widely used in the fields of biology and environmental protection, and has become an important part of separation science. One of the most important means. PTFE membrane is made of polytetrafluoroethylene, which is breathable, impermeable, large air flow, high temperature resistance, strong acid resistance, non-toxic, and plays an important role in membrane separation technology. However, the application of PTFE membrane alone in the process of pesticide wastewater treatment can only physically separate the pesticide wastewater, and does not effectively remove the pollutants in the wastewater, and the PTFE membrane will be polluted during long-term operation, thereby reducing the separation efficiency. Effect. Therefore, it is particularly important to find a method to make organic wastewater harmless.
纳米光催化技术是一种高级氧化技术,目前被广泛应用于废水处理过程中。纳米光催化剂在光的照射作用下产生具有强氧化作用的羟基自由基,将废水中的有害物质降解,生成水和无害气体,并且不会产生二次污染。目前研究的最为成熟的纳米光催化剂是TiO2,但是TiO2只能利用紫外光进行催化作用,限制了其在废水处理中的广泛运用。ZnO作为光催化剂,具有价格低廉、无毒、高光催化性能等特点,成为人们研究的热点。为了进一步提高ZnO的光降解活性,纳米级ZnO应运而生。但是,纳米ZnO在使用过程中,会发生严重的光腐蚀现象,限制了ZnO的应用。近几年,碳纳米管管壁官能团迅速发展,并且碳纳米管具有优良的电子传导性、对反应物和反应产物的吸附和脱附性能、碳与金属催化剂的金属-载体强相互作用和量子效应能特点,使其越来越多地用作催化剂载体。碳纳米管与纳米ZnO的复合材料,可减少ZnO的光腐蚀,提高ZnO对有机废水的光催化降解效果。Nanophotocatalytic technology is an advanced oxidation technology, which is widely used in wastewater treatment process. The nano-photocatalyst generates hydroxyl radicals with strong oxidation effect under the irradiation of light, degrades harmful substances in wastewater, generates water and harmless gases, and does not produce secondary pollution. The most mature nano-photocatalyst studied at present is TiO 2 , but TiO 2 can only be catalyzed by ultraviolet light, which limits its wide application in wastewater treatment. As a photocatalyst, ZnO has the characteristics of low price, non-toxicity, and high photocatalytic performance, and has become a research hotspot. In order to further improve the photodegradation activity of ZnO, nanoscale ZnO came into being. However, during the use of nano-ZnO, serious photocorrosion phenomenon will occur, which limits the application of ZnO. In recent years, carbon nanotube wall functional groups have developed rapidly, and carbon nanotubes have excellent electronic conductivity, adsorption and desorption properties for reactants and reaction products, strong metal-support interaction between carbon and metal catalysts, and quantum The effect and energy characteristics make it more and more used as a catalyst carrier. The composite material of carbon nanotubes and nano-ZnO can reduce the photocorrosion of ZnO and improve the photocatalytic degradation effect of ZnO on organic wastewater.
发明内容Contents of the invention
本发明的目的提供一种碳纳米管/氧化锌PTFE光催化膜及其制备方法,根据PTFE膜和碳纳米管/氧化锌各自的优缺点,向PTFE膜中添加碳纳米管/氧化锌复合材料,不但解决了PTFE膜易受污染的问题,还使PTFE膜具备了氧化锌的光催化性能,对污染水体有净化作用。The object of the present invention provides a kind of carbon nanotube/zinc oxide PTFE photocatalyst membrane and preparation method thereof, according to the respective advantages and disadvantages of PTFE membrane and carbon nanotube/zinc oxide, add carbon nanotube/zinc oxide composite material in PTFE membrane , not only solves the problem of PTFE membrane being easily polluted, but also makes PTFE membrane have the photocatalytic performance of zinc oxide, which can purify polluted water.
本发明的技术方案如下:Technical scheme of the present invention is as follows:
本发明所述的一种碳纳米管/氧化锌PTFE光催化膜的制备方法,包括以下步骤:A kind of preparation method of carbon nanotube/zinc oxide PTFE photocatalytic film of the present invention, comprises the following steps:
1)取碳纳米管,加入混酸,在80~90℃水浴条件下持续搅拌,然后将碳纳米管与混酸的混合物抽滤、洗涤、烘干得到酸化处理的碳纳米管;1) Take carbon nanotubes, add mixed acid, and continue to stir in a water bath at 80-90°C, then filter, wash, and dry the mixture of carbon nanotubes and mixed acid to obtain acidified carbon nanotubes;
2) 取步骤1)中酸化处理过的碳纳米管与Zn(CH2COOH)2按一定的比例混合,加入氨水使pH变为弱碱性,继续搅拌,再经100~150℃高温反应、过滤、洗涤、烘干,得到碳纳米管/氧化锌复合材料;2) Mix the acidified carbon nanotubes and Zn(CH 2 COOH) 2 in a certain proportion in step 1), add ammonia water to make the pH become weakly alkaline, continue to stir, and then react at a high temperature of 100~150°C, Filtrating, washing and drying to obtain the carbon nanotube/zinc oxide composite material;
3)将步骤2)得到的碳纳米管/氧化锌复合材料与聚四氟乙烯粉末按一定的质量比加入到有机溶剂中,用超声波和高速机械搅拌2~3小时至变成粘稠混合液;3) Add the carbon nanotube/zinc oxide composite material and polytetrafluoroethylene powder obtained in step 2) into the organic solvent according to a certain mass ratio, and stir with ultrasonic waves and high-speed machinery for 2 to 3 hours until it becomes a viscous mixture ;
4) 将步骤3)中的混合液加热后,置于模具中冷压成型,经高温烧结后得到碳纳米管/氧化锌PTFE膜。4) After heating the mixed solution in step 3), place it in a mold for cold pressing, and sinter at high temperature to obtain a carbon nanotube/zinc oxide PTFE film.
上述步骤1)中加入的混酸为浓硫酸与浓硝酸以体积比1~3:1混合而成。The mixed acid added in the above step 1) is a mixture of concentrated sulfuric acid and concentrated nitric acid at a volume ratio of 1-3:1.
上述步骤2)中碳纳米管与Zn(CH2COOH)2的比例关系由最终获得的碳纳米管/氧化锌复合材料中碳纳米管和氧化锌的质量比所决定,一般碳纳米管和氧化锌的质量配比为1:25~50。The proportion relationship between carbon nanotubes and Zn(CH 2 COOH) 2 in the above step 2) is determined by the mass ratio of carbon nanotubes and zinc oxide in the finally obtained carbon nanotube/zinc oxide composite material. Generally, carbon nanotubes and zinc oxide The mass ratio of zinc is 1:25~50.
上述步骤3)中碳纳米管/氧化锌复合材料与聚四氟乙烯粉末的质量比为1:6~20;有机溶剂为N-甲基吡咯烷酮;高速机械搅拌转速为300~400r/min。The mass ratio of the carbon nanotube/zinc oxide composite material to the polytetrafluoroethylene powder in the above step 3) is 1:6~20; the organic solvent is N-methylpyrrolidone; the speed of high-speed mechanical stirring is 300~400r/min.
上述步骤4)中高温烧结温度在300~400℃。The medium-high temperature sintering temperature in the above step 4) is 300-400°C.
所述方法制备得到的碳纳米管/氧化锌PTFE光催化膜,不仅延长了PTFE膜的使用寿命,而且增强了ZnO的光催化降解有机污染物的性能,在污水处理中有较佳的效果,苯酚和COD去除率均可达到95%以上,膜经蒸馏水超声清洗5~6小时,膜的通量可以恢复到90%以上,易于清洗。The carbon nanotube/zinc oxide PTFE photocatalytic film prepared by the method not only prolongs the service life of the PTFE film, but also enhances the performance of ZnO photocatalytic degradation of organic pollutants, and has a better effect in sewage treatment. Both the removal rate of phenol and COD can reach more than 95%. After the membrane is ultrasonically cleaned with distilled water for 5-6 hours, the flux of the membrane can be restored to more than 90%, which is easy to clean.
有益效果:Beneficial effect:
根据PTFE膜和碳纳米管/氧化锌各自的优缺点,向PTFE膜中添加碳纳米管/氧化锌复合材料,制备得到碳纳米管/氧化锌PTFE光催化膜,碳纳米管/氧化锌PTFE光催化膜不仅延长了PTFE膜的使用寿命,而且增强了ZnO的光催化降解有机污染物的性能。本发明工艺设备简单,易于规模生产,有很大的市场前景。解决了PTFE膜易受污染的问题,对污染水体有净化作用,可有效降解有机废水,市场前景广阔。According to the advantages and disadvantages of PTFE film and carbon nanotube/zinc oxide, add carbon nanotube/zinc oxide composite material to PTFE film to prepare carbon nanotube/zinc oxide PTFE photocatalytic film, carbon nanotube/zinc oxide PTFE photocatalytic film The catalytic membrane not only prolongs the service life of the PTFE membrane, but also enhances the photocatalytic degradation of organic pollutants of ZnO. The process equipment of the invention is simple, easy for large-scale production, and has great market prospect. It solves the problem that the PTFE membrane is easily polluted, has a purifying effect on polluted water, can effectively degrade organic wastewater, and has a broad market prospect.
附图说明Description of drawings
图1碳纳米管/氧化锌-PTFE光催化膜废水处理装置示意图;Fig. 1 schematic diagram of carbon nanotube/zinc oxide-PTFE photocatalytic membrane wastewater treatment device;
其中:1-废水池,2-进水泵,3-加热器,4-膜蒸馏器,5-碳纳米管/氧化锌PTFE光催化膜,6-石英冷阱,7-光源,8-循环水泵,9-循环水池,10-集水池。Among them: 1-Wastewater pool, 2-Inlet pump, 3-Heater, 4-Membrane distiller, 5-Carbon nanotube/zinc oxide PTFE photocatalytic membrane, 6-Quartz cold trap, 7-Light source, 8-Circulating water pump , 9-circulating pool, 10-collecting pool.
具体实施方式Detailed ways
以下是本发明的几个具体实施例,进一步说明本发明,但是本发明不仅限于此。The following are several specific embodiments of the present invention to further illustrate the present invention, but the present invention is not limited thereto.
实施例1Example 1
取500mg碳纳米管加入有磁力搅拌的100mL单颈平底烧瓶,加入40mL混酸(浓硫酸:浓硝酸=3:1,体积比),先用60HZ超声水浴1h,在90℃水浴条件下搅拌2h,将混合物用去离子水稀释10倍后,用0.22μm混合膜抽滤,并反复用去离子水洗涤抽滤,再将滤物置于真空干燥箱中60℃干燥24h。Take 500mg of carbon nanotubes and put them into a 100mL single-neck flat-bottomed flask with magnetic stirring, add 40mL of mixed acid (concentrated sulfuric acid:concentrated nitric acid=3:1, volume ratio), first use a 60HZ ultrasonic water bath for 1h, then stir in a 90°C water bath for 2h, After the mixture was diluted 10 times with deionized water, it was suction-filtered with a 0.22 μm mixed membrane, washed with deionized water repeatedly and then dried in a vacuum oven at 60°C for 24 hours.
将20mg上述处理的碳纳米管超声分散于150mL无水乙醇和水的混合液(体积比1:1)中,加入30mL浓度为0.2mol/L的乙酸锌溶液,充分搅拌,加入氨水调节pH为碱性(pH值为8~9),充分搅拌后过滤,固相分散在去离子水中,调节pH为中性。将以上反应物置于反应釜中,120℃条件下反应5h,然后快速冷却至室温,产物经过滤、洗涤,在60~80℃下干燥,得到4%碳纳米管/氧化锌复合材料。Ultrasonic disperse 20 mg of the above-mentioned carbon nanotubes into 150 mL of a mixture of absolute ethanol and water (volume ratio 1:1), add 30 mL of zinc acetate solution with a concentration of 0.2 mol/L, stir well, and add ammonia water to adjust the pH to Alkaline (pH 8~9), stir well and filter, disperse the solid phase in deionized water, and adjust the pH to be neutral. The above reactants were placed in a reaction kettle and reacted at 120°C for 5 hours, then rapidly cooled to room temperature, and the product was filtered, washed, and dried at 60-80°C to obtain a 4% carbon nanotube/zinc oxide composite material.
将上述碳纳米管/氧化锌复合材料按质量分数为10%添加到聚四氟乙烯中,加入N-甲基吡咯烷酮,用超声波和高速机械搅拌器充分混合,高速机械搅拌转速为300~400r/min,加热混合物使N-甲基吡咯烷酮完全挥发 ,再将碳纳米管/氧化锌和聚四氟乙烯混合物置于模具(规格为6mm×20mm×20mm)中冷压成型,再经300~400℃烧结,得到10%碳纳米管/氧化锌-PTFE光催化膜。Add the above-mentioned carbon nanotube/zinc oxide composite material to polytetrafluoroethylene at a mass fraction of 10%, add N-methylpyrrolidone, and fully mix with ultrasonic waves and a high-speed mechanical stirrer. The high-speed mechanical stirring speed is 300~400r/ min, heat the mixture to completely volatilize N-methylpyrrolidone, then put the mixture of carbon nanotubes/zinc oxide and polytetrafluoroethylene into a mold (6mm×20mm×20mm) for cold pressing, and then heat it at 300~400℃ Sintering to obtain a 10% carbon nanotube/zinc oxide-PTFE photocatalytic film.
实施例2Example 2
以实施例1制备得到的10%碳纳米管/氧化锌-PTFE光催化膜进行废水处理,以浓度为40mg/L的苯酚废水为待处理废水,通过如图1所示的废水处理装置,将苯酚废水加入到废水池1中,通过进水泵2的牵引废水进入膜蒸馏器4热侧,热侧的温度设置为65℃,冷侧温度为室温,水力停留时间设为3h,热测温度由加热器3控制,碳纳米管/氧化锌PTFE光催化膜5在500W可见光照射条件下处理废水,热测废水中水蒸气透过碳纳米管/氧化锌PTFE膜5进入膜蒸馏器4冷侧并液化成水,以膜两侧的蒸汽压差作为驱动力;打开带有液位控制器的进水泵2,循环水泵8,使膜蒸馏器冷热侧水循环流动,循环水池9中的水通过循环泵8进入光催化膜冷侧,将液化的水带入循环水池9,最终膜蒸馏的产水会进入集水池10。每隔0.5h取一次样,并测量集水池10中苯酚浓度和COD值,发现苯酚和COD去除率均可达到95%。将实验用完的膜经蒸馏水超声清洗5~6小时,膜的通量可以恢复到90%以上。The 10% carbon nanotube/zinc oxide-PTFE photocatalyst membrane that prepares with embodiment 1 carries out waste water treatment, is the phenol waste water of 40mg/L with concentration as waste water to be treated, by the waste water treatment device as shown in Figure 1, will The phenol waste water is added to the waste water tank 1, and the waste water is drawn into the hot side of the membrane still 4 through the suction pump 2. The temperature of the hot side is set at 65°C, the temperature of the cold side is at room temperature, and the hydraulic retention time is set at 3h. The thermal measurement temperature is determined by The heater 3 controls the carbon nanotube/zinc oxide PTFE photocatalytic membrane 5 to treat the wastewater under the condition of 500W visible light irradiation. Liquefied into water, the vapor pressure difference on both sides of the membrane is used as the driving force; the water inlet pump 2 and the circulating water pump 8 with a liquid level controller are turned on to circulate the hot and cold side water of the membrane distiller, and the water in the circulating pool 9 passes through the circulation The pump 8 enters the cold side of the photocatalytic membrane and brings the liquefied water into the circulating pool 9 , and finally the produced water from the membrane distillation enters the sump 10 . Take a sample every 0.5h, and measure the concentration of phenol and the COD value in the sump 10, and find that the removal rate of phenol and COD can reach 95%. After the membrane used up in the experiment is ultrasonically cleaned with distilled water for 5-6 hours, the flux of the membrane can be restored to more than 90%.
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