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CN109759021B - A kind of preparation method of cyclodextrin-based Cu2O blend membrane for treating ppcps in regenerated water - Google Patents

A kind of preparation method of cyclodextrin-based Cu2O blend membrane for treating ppcps in regenerated water Download PDF

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CN109759021B
CN109759021B CN201910107680.XA CN201910107680A CN109759021B CN 109759021 B CN109759021 B CN 109759021B CN 201910107680 A CN201910107680 A CN 201910107680A CN 109759021 B CN109759021 B CN 109759021B
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cyclodextrin
ppcps
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CN109759021A (en
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张军
汪慧静
田禹
尹琳琳
左薇
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Harbin Institute of Technology Shenzhen
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Abstract

The invention discloses cyclodextrin-Cu for treating ppcps in reclaimed water2A preparation method of an O blend membrane belongs to the field of environmental pollution treatment, and specifically comprises the following steps: 1) preparation of ultra-fine Cu2O powder; 2) preparation of ultrafine Cyclodextrin-based-Cu by coupling agent2An O composite material; 3) preparation of cyclodextrin-Cu by blending method2O blend the film. The invention realizes the high-efficiency removal of PPCPs through the adsorption, photocatalytic degradation and membrane interception functions, and simultaneously realizes the excellent separation and recovery of the adsorbent through the membrane fixation function; meanwhile, the photocatalytic efficiency of the photocatalyst is greatly improved; and the life cycle of the membrane is increased, thereby reducing economic losses.

Description

一种用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备 方法Preparation of a cyclodextrin-based Cu2O blend membrane for treating ppcps in regenerated water method

技术领域technical field

本发明涉及一种用于处理ppcps的环糊精基-Cu2O共混膜及其制备方法,具体属于环境污染治理领域。The invention relates to a cyclodextrin-Cu 2 O blended film used for treating ppcps and a preparation method thereof, and particularly belongs to the field of environmental pollution control.

背景技术Background technique

药品和个人护理品(PPCPs)是一类新型微污染物,具有环境稳定性、难降解性以及生物累积性等特点,长期接触会对人体健康和生态环境造成不可逆的潜在危害。目前已经在地表水、地下水、饮用水与再生水中广泛检测到该类污染物存在(浓度一般在10ng/L-500mg/L水平),城市水系统80%以上的PPCPs污染来自再生水。因此,开展再生回用水中PPCPs的去除技术对我国城市污水回用事业的持续发展具有重要的理论和现实意义。Pharmaceuticals and personal care products (PPCPs) are a new type of micro-pollutants with the characteristics of environmental stability, refractory degradation and bioaccumulation. Long-term exposure will cause irreversible potential harm to human health and the ecological environment. At present, such pollutants have been widely detected in surface water, groundwater, drinking water and reclaimed water (the concentration is generally at the level of 10ng/L-500mg/L). More than 80% of PPCPs pollution in urban water systems comes from reclaimed water. Therefore, it is of great theoretical and practical significance to carry out the removal technology of PPCPs in recycled water for the sustainable development of urban sewage reuse in my country.

由于城市污水处理厂传统的生物处理技术对PPCPs去除效果有限,近年来国内外围绕高级氧化、膜过滤、活性炭吸附及组合工艺方法开展相关研究。高级氧化技术(AOPs)通过自由基(OH·为主)的强氧化性实现PPCPs的完全降解或提高其生化性,其中光催化剂技术得到广泛应用,该技术对微量污染物去除效果较好,但超细光催化剂在溶液中的团聚现象是影响光催化效果的重要因素。膜过滤技术通过膜的分子截留作用实现微污染物截留去除,去除率可高达99%以上,但工艺能耗非常高。吸附是一种高效可行的PPCPs脱除技术,成本低、易操作、无副产物生成且去除效率较高,但是吸附剂的有效回收是需要解决的问题。Due to the limited effect of the traditional biological treatment technology in urban sewage treatment plants on the removal of PPCPs, related researches have been carried out on advanced oxidation, membrane filtration, activated carbon adsorption and combined process methods at home and abroad in recent years. Advanced oxidation technology (AOPs) achieves complete degradation of PPCPs or improves its biochemical properties through the strong oxidizing properties of free radicals (OH-based). Among them, photocatalyst technology has been widely used. This technology has a good effect on removing trace pollutants, but The agglomeration of ultrafine photocatalysts in solution is an important factor affecting the photocatalytic effect. Membrane filtration technology achieves the interception and removal of micro-pollutants through the molecular interception of membranes, and the removal rate can be as high as 99% or more, but the process energy consumption is very high. Adsorption is an efficient and feasible removal technology for PPCPs, with low cost, easy operation, no by-product formation and high removal efficiency, but the effective recovery of adsorbents is a problem that needs to be solved.

发明内容SUMMARY OF THE INVENTION

为解决上述问题,本发明的目的是提供一种不仅能高效处理再生水中ppcps,同时兼顾回收吸附剂以及抑制膜污染的环糊精基-Cu2O 共混膜材料的制备方法。In order to solve the above problems, the purpose of the present invention is to provide a preparation method of cyclodextrin-Cu 2 O blended membrane material which can not only efficiently treat ppcps in regenerated water, but also take into account the recovery of adsorbent and the inhibition of membrane fouling.

本发明提供的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法包括以下步骤:The preparation method of the cyclodextrin-Cu 2 O blend membrane for treating ppcps in regenerated water provided by the present invention comprises the following steps:

1)制备超细Cu2O粉末;1) Preparation of ultrafine Cu 2 O powder;

2)通过偶联剂制备超细环糊精基-Cu2O复合材料;2) Preparation of ultrafine cyclodextrin-Cu 2 O composite material by coupling agent;

3)共混法制备环糊精基-Cu2O共混膜。3) The cyclodextrin-Cu 2 O blend film was prepared by blending method.

步骤1)具体为:取NaOH溶液和CuSO4溶液加入反应釜中,磁力搅拌均匀后,加入葡萄糖溶液,加热反应,将反应釜冷却至室温,分离提纯固体产物制得超细氧化亚铜粉末。所述CuSO4,NaOH,葡萄糖的摩尔比为1:15:3。所述NaOH溶液的浓度为5mol/L,CuSO4溶液的浓度为1mol/L,葡萄糖溶液的浓度为1.5mol/L。所述加热反应,反应温度为230-380℃,反应时间为4-8h。所述分离提纯,具体为:抽滤取滤渣,用无水乙醇清洗3-5次,最后置于真空干燥箱内真空烘干。所述真空烘干,真空度为1200-4800pa,烘干温度为55-60℃,烘干时间为2-20h。Step 1) is specifically as follows: add NaOH solution and CuSO 4 solution into the reaction kettle, after magnetic stirring uniformly, add glucose solution, heat the reaction, cool the reaction kettle to room temperature, separate and purify the solid product to obtain ultrafine cuprous oxide powder. The molar ratio of CuSO 4 , NaOH and glucose is 1:15:3. The concentration of the NaOH solution is 5 mol/L, the concentration of the CuSO 4 solution is 1 mol/L, and the concentration of the glucose solution is 1.5 mol/L. In the heating reaction, the reaction temperature is 230-380° C., and the reaction time is 4-8 h. The separation and purification are specifically as follows: extracting the filter residue by suction filtration, washing with absolute ethanol for 3-5 times, and finally placing it in a vacuum drying box for vacuum drying. In the vacuum drying, the vacuum degree is 1200-4800pa, the drying temperature is 55-60°C, and the drying time is 2-20h.

步骤2)具体为:取步骤1)制备的超细Cu2O粉末与甲苯搅拌成糊状,滴加偶联剂,加热回流反应,冷却至室温后加入环糊精基材料,在氮气保护下加热搅拌反应,冷却至室温后静置,分离提纯固体产物得环糊精基-Cu2O复合材料。所述Cu2O粉末在甲苯中的浓度为1 g/mL,所述Cu2O粉末与偶联剂的质量/体积比为(5-10):(14-18) g/mL。所述Cu2O粉末与环糊精基材料的质量比为(5-10):(8-16)。所述回流反应,温度为130℃-140℃,回流时间为4h。所述加热搅拌反应,反应温度为128℃,反应时间为2h。所述所述静置,静置时间为18-30h,分离提纯具体为:过滤取滤渣,依次用丙酮、乙醚、甲醇、蒸馏水分别洗涤3-5次,真空干燥。所述真空干燥,真空度为 1200-4800pa,温度为55-60℃,干燥时间为2-20h。所述环糊精基材料为α-环糊精,β-环糊精,γ-环糊精交联聚合物中的一种。所述偶联剂为硅烷类偶联剂,包括氨丙基三乙氧基硅烷(KH550),乙烯基三乙氧基硅烷(A151),乙烯基三乙氧基硅烷(A171),巯丙基三甲(乙)氧基硅烷 (KH580,KH590)中的一种或几种。Step 2) is specifically: taking the ultrafine Cu 2 O powder prepared in step 1) and stirring it with toluene into a paste, adding a coupling agent dropwise, heating and refluxing for reaction, cooling to room temperature, adding a cyclodextrin-based material, and under nitrogen protection The reaction is heated and stirred, cooled to room temperature and then left to stand, and the solid product is separated and purified to obtain a cyclodextrin-Cu 2 O composite material. The concentration of the Cu 2 O powder in toluene is 1 g/mL, and the mass/volume ratio of the Cu 2 O powder to the coupling agent is (5-10):(14-18) g/mL. The mass ratio of the Cu 2 O powder to the cyclodextrin-based material is (5-10):(8-16). In the reflux reaction, the temperature is 130°C-140°C, and the reflux time is 4h. For the heating and stirring reaction, the reaction temperature was 128° C. and the reaction time was 2 h. The said standing, the standing time is 18-30h, and the separation and purification are as follows: filtering and collecting the filter residue, washing with acetone, ether, methanol and distilled water for 3-5 times respectively, and vacuum drying. In the vacuum drying, the vacuum degree is 1200-4800pa, the temperature is 55-60°C, and the drying time is 2-20h. The cyclodextrin-based material is one of α-cyclodextrin, β-cyclodextrin and γ-cyclodextrin cross-linked polymer. The coupling agent is a silane coupling agent, including aminopropyltriethoxysilane (KH550), vinyltriethoxysilane (A151), vinyltriethoxysilane (A171), mercaptopropyl One or more of trimethyl(eth)oxysilane (KH580, KH590).

步骤3)具体为:将PVDF粉末和有机溶剂加入圆底烧瓶中,搅拌得到均一透明的膜材料液后,在搅拌状态下添加PVP粉末和步骤2) 制备的环糊精基-Cu2O复合材料,充分混合后超声分散得到悬浮铸膜液,所述铸膜液静置自然脱泡,倾倒在玻璃板上凝胶定型后刮膜,经烘干后得到环糊精基-Cu2O共混膜。所述PVDF粉末在所述有机溶剂中的浓度为0.25g/mL,所述PVP粉末在所述有机溶剂中的浓度为 1:10-1:15g/mL,所述环糊精基-Cu2O复合材料与PVDF粉末的质量比为1:5-1:12。所述有机溶剂为N,N-二甲基乙酰胺,N,N-二甲基甲酰胺、N-甲基吡咯烷酮、二甲基亚砜中的一种。所述烘干,温度为 55-60℃,烘干时间为2-20h。Step 3) is specifically as follows: adding PVDF powder and organic solvent into a round-bottomed flask, stirring to obtain a uniform and transparent membrane material solution, adding PVP powder and the cyclodextrin-Cu 2 O composite prepared in step 2) under stirring The materials are fully mixed and ultrasonically dispersed to obtain a suspension casting liquid. The casting liquid is left to stand for natural defoaming, poured onto a glass plate for gel setting, scraped, and dried to obtain a cyclodextrin-Cu 2 O co-polymer. mixed film. The concentration of the PVDF powder in the organic solvent is 0.25g/mL, the concentration of the PVP powder in the organic solvent is 1:10-1:15g/mL, and the cyclodextrin-Cu 2 The mass ratio of O composite to PVDF powder is 1:5-1:12. The organic solvent is one of N,N-dimethylacetamide, N,N-dimethylformamide, N-methylpyrrolidone and dimethyl sulfoxide. For the drying, the temperature is 55-60° C., and the drying time is 2-20h.

步骤1)所得超细Cu2O粉末粒径为50-500nm。The particle size of the ultrafine Cu 2 O powder obtained in step 1) is 50-500 nm.

本方法所得环糊精基-Cu2O共混膜中氧化亚铜、环糊精、膜质量比为1:1.6:20-25,膜孔径大小为小于0.01微米。The mass ratio of cuprous oxide, cyclodextrin and membrane in the cyclodextrin-Cu 2 O blend membrane obtained by the method is 1:1.6:20-25, and the membrane pore size is less than 0.01 micron.

有益效果beneficial effect

本发明将环糊精通过偶联剂键合到纳米Cu2O表面,进一步采用共混法制备得到环糊精基-Cu2O复合材料修饰的膜材料,该光催化- 吸附-膜组合系统通过吸附、光催化降解和膜截留作用实现对PPCPs 的高效去除,同时膜的固定作用实现了吸附剂优异的分离回收;环糊精对光催化剂Cu2O的表面修饰有效抑制光催化剂团聚,大大提高光催化剂的光催化效率;光催化剂对有机物的光催化降解作用以及环糊精对膜亲疏水性能的改性同时抑制膜污染,使膜的使用周期得以增加,从而降低经济损耗。In the present invention, cyclodextrin is bonded to the surface of nanometer Cu 2 O through a coupling agent, and a film material modified by a cyclodextrin-Cu 2 O composite material is prepared by a blending method. The photocatalysis-adsorption-membrane combination system The high - efficiency removal of PPCPs is achieved through adsorption, photocatalytic degradation and membrane retention, and the membrane immobilization effect achieves excellent separation and recovery of the adsorbent. Improve the photocatalytic efficiency of the photocatalyst; the photocatalytic degradation of organic matter by the photocatalyst and the modification of the hydrophilic and hydrophobic properties of the membrane by cyclodextrin simultaneously suppress the membrane fouling, so that the service life of the membrane can be increased, thereby reducing economic losses.

具体为:Specifically:

1)本发明所制备的环糊精基-Cu2O共混膜,实现了光催化-吸附- 膜去除微量有机物的有效组合,该组合系统通过环糊精吸附作用、氧化亚铜光催化氧化作用和膜截留作用实现对PPCPs的高效去除,将 ppcps降解或者转化为可生化性更高的小分子。1) The cyclodextrin base-Cu 2 O blend film prepared by the present invention realizes an effective combination of photocatalysis-adsorption-membrane removal of trace organics. The combined system uses cyclodextrin adsorption, cuprous oxide photocatalytic oxidation The PPCPs can be efficiently removed by the action and membrane entrapment, and the PPCPs can be degraded or converted into small molecules with higher biodegradability.

2)本发明所制备的环糊精基-Cu2O共混膜,膜的固定作用实现了环糊精吸附剂优异的分离回收,避免了吸附剂在溶液中难以回收再利用,造成二次污染的问题。2) In the cyclodextrin-based Cu 2 O blend membrane prepared by the present invention, the immobilization of the membrane realizes the excellent separation and recovery of the cyclodextrin adsorbent, and avoids the difficulty of recovery and reuse of the adsorbent in the solution, resulting in secondary pollution problem.

3)本发明所制备的环糊精基-Cu2O共混膜,环糊精对光催化剂 Cu2O的表面修饰改变了氧化亚铜的表面性质,有效抑制氧化亚铜团聚,大大提高光催化剂氧化ppcps的效率,同时避免光催化剂的二次污染。3) In the cyclodextrin-Cu 2 O blend film prepared by the present invention, the surface modification of the photocatalyst Cu 2 O by cyclodextrin changes the surface properties of cuprous oxide, effectively inhibits the agglomeration of cuprous oxide, and greatly improves the photocatalytic performance. The efficiency of the catalyst to oxidize ppcps while avoiding the secondary pollution of the photocatalyst.

4)本发明所制备的环糊精基-Cu2O共混膜,膜内光催化剂氧化亚铜对有机物的光催化降解作用和光催化剂氧化亚铜的抑菌作用以及环糊精对膜亲疏水性能的改性同时抑制了膜污染,使膜的使用周期得以增加,从而降低经济损耗。4) The cyclodextrin base-Cu 2 O blend film prepared by the present invention has the photocatalytic degradation effect of photocatalyst cuprous oxide on organic matter in the film, the bacteriostatic effect of photocatalyst cuprous oxide, and the hydrophilic and hydrophobic effect of cyclodextrin on the film. The modification of performance also inhibits membrane fouling, which increases the service life of the membrane, thereby reducing economic losses.

5)本发明所制备的环糊精基-Cu2O共混膜,其制备过程简单,反应易于控制,经济上可行,可通过调整环糊精基-Cu2O的各组分比,最大化的实现对各类ppcps的富集和降解。5) The cyclodextrin-Cu 2 O blend film prepared by the present invention has a simple preparation process, easy control of the reaction, and is economically feasible. By adjusting the ratio of each component of the cyclodextrin-Cu 2 O, the maximum The realization of the enrichment and degradation of various types of ppcps.

具体实施方式Detailed ways

下面将结合本发明实施例,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

实施例1Example 1

一种用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法:1)取5mol/L的NaOH溶液30mL和1mol/L的CuSO410mL溶液加入反应釜中,磁力搅拌均匀后,加入1.5mol/L的葡萄糖溶液20mL 于上述混合溶液中,将反应釜放置于恒温箱中高温反应,控制恒温箱温度为330℃,反应6h后将反应釜冷却至室温,抽滤,并用无水乙醇清洗5次,最后置于真空干燥箱内烘干(真空度为4800pa,烘干温度为60℃,烘干时间为5h),制得氧化亚铜粉末粒径为200nm-300nm。 2)取氧化亚铜粉末5g加入三颈烧瓶中,加入5mL甲苯低温下搅拌至溶液成糊状,然后滴加14mL乙烯基三乙氧基硅烷,并加热升温至 130℃,回流4h后冷却至室温,接着加入8.0gβ-环糊精交联聚合物,混合均匀后在氮气保护下,恒温128℃搅拌2h,然后冷却至室温,静置 18h,待固体充分沉降后过滤,滤饼依次分别用丙酮、乙醚、甲醇、蒸馏水充分3次洗涤,将滤渣在电热真空干燥箱内烘干得β-环糊精基 -Cu2O复合材料(真空干燥条件与步骤1)相同)。3)将一定量的PVDF 粉末和有机溶剂N,N-二甲基乙酰胺加入圆底烧瓶中,搅拌,得到均一透明的膜材料液后,在搅拌状态下添加一定量的PVP粉末和步骤2) 制备的β-环糊精基-Cu2O复合材料(PVDF粉末在所述有机溶剂中的浓度为0.25g/mL,PVP粉末在所述有机溶剂中的浓度为1:15g/mL,环糊精基-Cu2O复合材料与PVDF粉末的质量比为1:12),充分混合后超声分散得到悬浮铸膜液,所述铸膜液静置自然脱泡,倾倒在玻璃板上凝胶定型后刮膜,经烘箱干燥(温度为55-60℃,烘干时间为2-20h) 后得到β-环糊精基-Cu2O共混膜。A preparation method of a cyclodextrin-based Cu 2 O blend film for treating ppcps in regenerated water: 1) add 30 mL of 5 mol/L NaOH solution and 10 mL of 1 mol/L CuSO 4 solution into the reactor, stir magnetically After homogeneous, add 20 mL of 1.5 mol/L glucose solution to the above mixed solution, place the reaction kettle in a thermostat for high temperature reaction, control the temperature of the thermostat to be 330 ° C, cool the reaction kettle to room temperature after 6 hours of reaction, suction filtration, It was washed with absolute ethanol for 5 times, and finally dried in a vacuum drying oven (the vacuum degree was 4800pa, the drying temperature was 60°C, and the drying time was 5h) to obtain the cuprous oxide powder with a particle size of 200nm-300nm. 2) Take 5 g of cuprous oxide powder into a three-necked flask, add 5 mL of toluene and stir at low temperature until the solution becomes a paste, then dropwise add 14 mL of vinyltriethoxysilane, and heat up to 130 ° C, reflux for 4 hours, and then cool to a At room temperature, 8.0g of β-cyclodextrin cross-linked polymer was added, mixed uniformly, under nitrogen protection, stirred at a constant temperature of 128 °C for 2 hours, then cooled to room temperature, and stood for 18 hours. Acetone, ether, methanol, and distilled water were thoroughly washed three times, and the filter residue was dried in an electric heating vacuum drying oven to obtain a β-cyclodextrin-Cu 2 O composite material (the vacuum drying conditions were the same as in step 1). 3) Add a certain amount of PVDF powder and organic solvent N,N-dimethylacetamide into the round-bottomed flask, stir to obtain a uniform and transparent membrane material liquid, add a certain amount of PVP powder under stirring and step 2 ) prepared β-cyclodextrin-Cu 2 O composite material (the concentration of PVDF powder in the organic solvent is 0.25 g/mL, the concentration of PVP powder in the organic solvent is 1:15 g/mL, and the The mass ratio of dextrin-based-Cu 2 O composite material and PVDF powder is 1:12), and after thorough mixing, ultrasonic dispersion is obtained to obtain a suspension casting liquid. After setting, the film is scraped and dried in an oven (temperature is 55-60° C., drying time is 2-20h) to obtain a β-cyclodextrin-Cu 2 O blended film.

制备的β-环糊精基-Cu2O共混膜材料用于膜反应器中,反应器连续通过0.02mg/L双氯芬酸溶液中,置于温度为25℃的自然光中条件下反应,12h后测得双氯芬酸浓度变为0.0032mg/L,去除率为84%。为了对照,采用单独的PVDF膜材料,将1mg/L双氯芬酸溶液连续通过反应器,同条件下,12h后双氯芬酸去除率为48.6%。对β-环糊精基-Cu2O共混膜进行光催化性能测试,实验前在黑暗条件下β-环糊精基-Cu2O共混膜达到吸附平衡,然后同等条件下进行光照处理,测试膜样品大小3.5cm×4cm,发现光催化剂氧化亚铜将双氯芬酸的去除率提高了1.23倍。同时通过终端过滤试验对β-环糊精基-Cu2O共混膜材料和单独的膜材料进行膜通量测试,发现在β-环糊精基-Cu2O共混膜中膜污染临界时间原来的1.53倍左右。该实施例表明该材料具有高效富集双氯芬酸并且光催化降解双氯芬酸的功能;同时该β-环糊精基-Cu2O共混膜的膜污染现象得到抑制。The prepared β-cyclodextrin-Cu 2 O blended membrane material was used in a membrane reactor. The reactor was continuously passed through a 0.02 mg/L diclofenac solution and placed in a natural light at a temperature of 25 °C for the reaction. After 12 h The measured concentration of diclofenac became 0.0032 mg/L, and the removal rate was 84%. For comparison, a single PVDF membrane material was used, and 1 mg/L diclofenac solution was continuously passed through the reactor. Under the same conditions, the removal rate of diclofenac after 12 h was 48.6%. The photocatalytic performance of the β-cyclodextrin-Cu 2 O blend film was tested. Before the experiment, the β-cyclodextrin-Cu 2 O blend film reached the adsorption equilibrium under dark conditions, and then subjected to light treatment under the same conditions. The film sample size was 3.5 cm × 4 cm, and it was found that the photocatalyst cuprous oxide increased the removal rate of diclofenac by 1.23 times. At the same time, the membrane flux test of β-cyclodextrin-Cu 2 O blend membrane material and single membrane material was carried out by terminal filtration test, and it was found that the membrane fouling critical in β-cyclodextrin-Cu 2 O blend membrane The time is about 1.53 times the original time. This example shows that the material has the functions of efficiently enriching diclofenac and photocatalytically degrading diclofenac; meanwhile, the membrane fouling phenomenon of the β-cyclodextrin-Cu 2 O blend film is suppressed.

实施例2Example 2

一种用于处理再生水中ppcps的环糊精基-Cu2O共混膜,制备方法为:1)取5mol/L的NaOH溶液30mL和1mol/L的CuSO410mL 溶液加入反应釜中,磁力搅拌均匀后,加入1.5mol/L的葡萄糖溶液 20mL于上述混合溶液中,将反应釜放置于恒温箱中高温反应,控制恒温箱温度为480℃,反应6h后将反应釜冷却至室温,抽滤,滤渣用无水乙醇清洗3次,最后置于真空干燥箱内烘干(条件与实施例1 相同),制得氧化亚铜粉末粒径为50nm左右。2)取氧化亚铜粉末 5g加入三颈烧瓶中,加入5mL甲苯低温下搅拌至溶液成糊状,然后滴加18mL乙烯基三乙氧基硅烷,并加热升温至140℃,回流4h后冷却至室温,接着加入8.0gβ-环糊精交联聚合物,混合均匀后在氮气保护下,恒温128℃搅拌2h,然后冷却至室温,静置30h,待固体充分沉降后过滤,滤饼分别依次用丙酮、乙醚、甲醇、蒸馏水充分洗涤5次, 将滤渣在电热真空干燥箱内烘干得β-环糊精基-Cu2O复合材料(干燥条件与步骤1)相同)。3)将一定量的PVDF粉末和有机溶剂N,N-二甲基乙酰胺加入圆底烧瓶中,搅拌,得到均一透明的膜材料液后,在搅拌状态下添加一定量的PVP粉末和β-环糊精基-Cu2O复合材料 (PVDF粉末在所述有机溶剂中的浓度为0.25g/mL,PVP粉末在所述有机溶剂中的浓度为1:10g/mL,环糊精基-Cu2O复合材料与PVDF粉末的质量比为1:5),充分混合后超声分散得到悬浮铸膜液,所述铸膜液静置自然脱泡,倾倒在玻璃板上凝胶定型后刮膜,经烘箱干燥后得到β-环糊精基-Cu2O共混膜(烘干条件与实施例1步骤3)相同)。A cyclodextrin-based Cu 2 O blend film for treating ppcps in regenerated water, the preparation method is as follows: 1) 30 mL of 5 mol/L NaOH solution and 10 mL of 1 mol/L CuSO 4 solution are added into a reaction kettle, and the magnetic After stirring evenly, add 20 mL of 1.5 mol/L glucose solution to the above mixed solution, place the reaction kettle in a thermostat for high temperature reaction, control the temperature of the thermostat to be 480°C, cool the reaction kettle to room temperature after 6 hours of reaction, and filter with suction. , the filter residue was washed 3 times with anhydrous ethanol, and finally placed in a vacuum drying oven for drying (conditions were the same as in Example 1) to obtain a cuprous oxide powder with a particle size of about 50 nm. 2) Take 5 g of cuprous oxide powder into a three-necked flask, add 5 mL of toluene and stir at low temperature until the solution becomes a paste, then dropwise add 18 mL of vinyltriethoxysilane, and heat up to 140 ° C, reflux for 4 hours, and then cool to a At room temperature, 8.0g of β-cyclodextrin cross-linked polymer was added, mixed uniformly, under nitrogen protection, stirred at a constant temperature of 128 ° C for 2 hours, then cooled to room temperature, left standing for 30 hours, and filtered after the solid was fully settled. Acetone, ether, methanol and distilled water were fully washed for 5 times, and the filter residue was dried in an electric heating vacuum drying oven to obtain β-cyclodextrin-Cu 2 O composite material (drying conditions were the same as in step 1). 3) Add a certain amount of PVDF powder and organic solvent N,N-dimethylacetamide into the round-bottomed flask, stir to obtain a uniform and transparent membrane material liquid, add a certain amount of PVP powder and β- Cyclodextrin-Cu 2 O composite material (the concentration of PVDF powder in the organic solvent is 0.25 g/mL, the concentration of PVP powder in the organic solvent is 1:10 g/mL, and the concentration of cyclodextrin-Cu The mass ratio of 2 O composite material and PVDF powder is 1:5), and after fully mixing, ultrasonic dispersion is performed to obtain a suspension casting liquid. After drying in an oven, a β-cyclodextrin-Cu 2 O blend film was obtained (drying conditions were the same as in step 3 of Example 1).

制备的β-环糊精基-Cu2O共混膜材料用于膜反应器中,反应器连续通过5μg/L布洛芬溶液中,置于温度为25℃的自然光中条件下反应,12h后测得布洛芬浓度为0.42μg/L,去除率为91.6%。The prepared β-cyclodextrin-Cu 2 O blended membrane material was used in a membrane reactor. The reactor was continuously passed through 5 μg/L ibuprofen solution and placed in natural light at a temperature of 25 °C for 12 h. The concentration of ibuprofen was measured to be 0.42 μg/L, and the removal rate was 91.6%.

实施例3Example 3

一种用于处理再生水中ppcps的环糊精基-Cu2O共混膜,制备方法为:1)取5mol/L的NaOH溶液30mL和1mol/L的CuSO410mL溶液加入反应釜中,磁力搅拌均匀后,加入1.5mol/L的葡萄糖溶液 20mL于上述混合溶液中,将反应釜放置于恒温箱中高温反应,控制恒温箱温度为280℃,反应6h后将反应釜冷却至室温,抽滤,滤渣用无水乙醇清洗4次,最后置于真空干燥箱内烘干(条件与实施例1 步骤1)相同),制得氧化亚铜粉末粒径为100nm左右。2)取氧化亚铜粉末10g加入三颈烧瓶中,加入10mL甲苯低温下搅拌至溶液成糊状,然后滴加15mL氨丙基三乙氧基硅烷(KH550),并加热升温至 135℃,回流4h后冷却至室温,接着加入16.0gβ-环糊精聚合物,混合均匀后在氮气保护下,恒温128℃搅拌6h,然后冷却至室温,静置24h,待固体充分沉降后过滤,滤饼依次分别用丙酮、乙醚、甲醇、蒸馏水充分洗涤4次,将滤渣在电热真空干燥箱内烘干得β-环糊精基-Cu2O 复合材料(烘干条件一实施例1步骤2)相同)。2)将一定量的PVDF 粉末和有机溶剂N,N-二甲基乙酰胺加入圆底烧瓶中,搅拌,得到均一透明的膜材料液后,在搅拌状态下添加一定量的PVP粉末和β-环糊精基-Cu2O复合材料(PVDF粉末在所述有机溶剂中的浓度为 0.25g/mL,PVP粉末在所述有机溶剂中的浓度为1:12g/mL,环糊精基 -Cu2O复合材料与PVDF粉末的质量比为1:8),充分混合后超声分散得到悬浮铸膜液,所述铸膜液静置自然脱泡,倾倒在玻璃板上凝胶定型后刮膜,经烘箱干燥后得到β-环糊精基-Cu2O共混膜(干燥条件与实施例1步骤3)相同)。A cyclodextrin-based Cu 2 O blend membrane for treating ppcps in regenerated water, the preparation method is as follows: 1) 30 mL of 5mol/L NaOH solution and 10 mL of 1 mol/L CuSO 4 solution are added into a reaction kettle, and the magnetic After stirring evenly, add 20 mL of 1.5 mol/L glucose solution to the above mixed solution, place the reaction kettle in a thermostat for high temperature reaction, control the temperature of the thermostat to be 280°C, cool the reaction kettle to room temperature after 6 hours of reaction, and filter with suction. , the filter residue was washed 4 times with absolute ethanol, and finally dried in a vacuum drying oven (conditions were the same as in step 1 of Example 1) to obtain a cuprous oxide powder with a particle size of about 100 nm. 2) Add 10 g of cuprous oxide powder into a three-necked flask, add 10 mL of toluene and stir at low temperature until the solution becomes a paste, then dropwise add 15 mL of aminopropyltriethoxysilane (KH550), and heat up to 135 ° C, reflux After 4 hours, it was cooled to room temperature, and then 16.0 g of β-cyclodextrin polymer was added, mixed uniformly, and stirred at a constant temperature of 128 °C for 6 hours under nitrogen protection, then cooled to room temperature, and allowed to stand for 24 hours. Fully wash with acetone, ether, methanol, and distilled water for 4 times respectively, and dry the filter residue in an electric heating vacuum drying oven to obtain a β-cyclodextrin-Cu 2 O composite material (drying conditions are the same as in Example 1, Step 2)) . 2) Add a certain amount of PVDF powder and organic solvent N,N-dimethylacetamide into the round-bottomed flask, stir to obtain a uniform and transparent membrane material liquid, add a certain amount of PVP powder and β- Cyclodextrin-Cu 2 O composite material (the concentration of PVDF powder in the organic solvent was 0.25 g/mL, the concentration of PVP powder in the organic solvent was 1:12 g/mL, and the concentration of cyclodextrin-Cu The mass ratio of 2 O composite material and PVDF powder is 1:8), after fully mixing, ultrasonic dispersion is obtained to obtain a suspension casting liquid, the casting liquid is left to stand for natural defoaming, poured on a glass plate for gel setting, and then scraped. After drying in an oven, a β-cyclodextrin-Cu 2 O blend film was obtained (the drying conditions were the same as those in step 3 of Example 1).

制备的β-环糊精基-Cu2O共混膜材料用于膜反应器中,反应器连续通过0.2μg/L水杨酸溶液中,置于温度为25℃的自然光中条件下反应,8h后测得水杨酸浓度变为0.0298μg/L,去除率为85.1%。The prepared β-cyclodextrin-Cu 2 O blend membrane material was used in a membrane reactor. The reactor was continuously passed through a 0.2 μg/L salicylic acid solution and placed in a natural light with a temperature of 25 °C for the reaction. After 8 hours, the salicylic acid concentration was measured to become 0.0298 μg/L, and the removal rate was 85.1%.

Claims (18)

1.一种用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:包括以下步骤:1. a preparation method for the cyclodextrin base-Cu 2 O blend film for treating ppcps in regenerated water, it is characterized in that: comprising the following steps: 1)制备超细Cu2O粉末;1) Preparation of ultrafine Cu 2 O powder; 2)通过偶联剂制备超细环糊精基-Cu2O复合材料,具体为:取步骤1)制备的超细Cu2O粉末与甲苯搅拌成糊状,滴加偶联剂,加热回流反应,冷却至室温后加入环糊精基材料,在氮气保护下加热搅拌反应,冷却至室温后静置,分离提纯固体产物得环糊精基-Cu2O复合材料;2) Preparation of ultra-fine cyclodextrin-Cu 2 O composite material by coupling agent, specifically: taking the ultra-fine Cu 2 O powder prepared in step 1) and stirring it with toluene into a paste, adding coupling agent dropwise, and heating to reflux reaction, after cooling to room temperature, adding cyclodextrin-based material, heating and stirring the reaction under nitrogen protection, cooling to room temperature and standing, separating and purifying the solid product to obtain cyclodextrin-based-Cu 2 O composite material; 3)共混法制备环糊精基-Cu2O共混膜,具体为:将PVDF粉末和有机溶剂加入圆底烧瓶中,搅拌得到均一透明的膜材料液后,在搅拌状态下添加PVP粉末和步骤2)制备的环糊精基-Cu2O复合材料,充分混合后超声分散得到悬浮铸膜液,所述铸膜液静置自然脱泡,倾倒在玻璃板上凝胶定型后刮膜,经烘干后得到环糊精基-Cu2O共混膜。3) Preparation of cyclodextrin-Cu 2 O blend membrane by blending method, specifically: adding PVDF powder and organic solvent into a round-bottomed flask, stirring to obtain a uniform and transparent membrane material liquid, adding PVP powder under stirring and the cyclodextrin-Cu 2 O composite material prepared in step 2), fully mixed and ultrasonically dispersed to obtain a suspension casting liquid, the casting liquid is left to stand for natural defoaming, poured onto a glass plate for gel setting, and then scraped off the film , and the cyclodextrin-Cu 2 O blend film was obtained after drying. 2.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:步骤1)具体为:取NaOH溶液和CuSO4溶液加入反应釜中,磁力搅拌均匀后,加入葡萄糖溶液,加热反应,将反应釜冷却至室温,分离提纯固体产物制得超细氧化亚铜粉末。2. The method for preparing a cyclodextrin-based Cu 2 O blended film for treating ppcps in regenerated water according to claim 1, characterized in that: step 1) is specifically: taking NaOH solution and CuSO 4 solution and adding reaction In the kettle, after magnetic stirring is uniform, add glucose solution, heat the reaction, cool the reaction kettle to room temperature, separate and purify the solid product to obtain ultrafine cuprous oxide powder. 3.根据权利要求2所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述CuSO4,NaOH,葡萄糖的摩尔比为1:15:3。3. The method for preparing a cyclodextrin-Cu 2 O blended membrane for treating ppcps in regenerated water according to claim 2, wherein the molar ratio of the CuSO 4 , NaOH and glucose is 1:15 :3. 4.根据权利要求2所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述NaOH溶液的浓度为5 mol/L,CuSO4溶液的浓度为1 mol/L,葡萄糖溶液的浓度为1.5 mol/L。4. The preparation method of the cyclodextrin-Cu 2 O blended film for treating ppcps in regenerated water according to claim 2, characterized in that: the concentration of the NaOH solution is 5 mol/L, and the CuSO solution is 5 mol/L. The concentration of glucose solution is 1 mol/L, and the concentration of glucose solution is 1.5 mol/L. 5.根据权利要求2所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述加热反应,反应温度为230-380℃,反应时间为4-8h。5 . The method for preparing a cyclodextrin-Cu 2 O blended film for treating ppcps in regenerated water according to claim 2 , wherein the heating reaction is performed at a reaction temperature of 230-380° C. and a reaction time of 230-380° C. 6 . 4-8h. 6.根据权利要求2所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述分离提纯,具体为:抽滤取滤渣,用无水乙醇清洗3-5次,最后置于真空干燥箱内真空烘干。6. The preparation method of the cyclodextrin-Cu 2 O blended membrane for treating ppcps in regenerated water according to claim 2, characterized in that: the separation and purification is specifically: extracting the filter residue by suction filtration, Washed with water ethanol for 3-5 times, and finally placed in a vacuum drying box for vacuum drying. 7.根据权利要求6所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述真空烘干,真空度为1200-4800pa,烘干温度为55-60℃,烘干时间为2-20h。7. The method for preparing a cyclodextrin-Cu 2 O blended film for treating ppcps in regenerated water according to claim 6, characterized in that: the vacuum drying has a vacuum degree of 1200-4800pa, and drying The temperature is 55-60℃, and the drying time is 2-20h. 8.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述Cu2O粉末在甲苯中的浓度为1 g/mL,所述Cu2O粉末与偶联剂的质量/体积比为(5-10):(14-18)g/mL。8. The preparation method of the cyclodextrin-Cu 2 O blended film for treating ppcps in regenerated water according to claim 1, wherein the concentration of the Cu 2 O powder in toluene is 1 g/ mL, the mass/volume ratio of the Cu 2 O powder and the coupling agent is (5-10): (14-18) g/mL. 9.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述Cu2O粉末与环糊精基材料的质量比为(5-10):(8-16)。9 . The method for preparing a cyclodextrin-Cu 2 O blended film for treating ppcps in regenerated water according to claim 1 , wherein the mass ratio of the Cu 2 O powder to the cyclodextrin-based material is: 10 . as (5-10):(8-16). 10.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述回流反应,温度为130℃-140℃,回流时间为4h。10 . The method for preparing a cyclodextrin-Cu 2 O blend film for treating ppcps in reclaimed water according to claim 1 , wherein the reflux reaction is performed at a temperature of 130° C.-140° C. and a reflux time. 11 . for 4h. 11.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述加热搅拌反应,反应温度为128℃,反应时间为2h。11 . The method for preparing a cyclodextrin-Cu 2 O blended film for treating ppcps in regenerated water according to claim 1 , wherein the heating and stirring reaction is performed at a reaction temperature of 128° C. and a reaction time of 128° C. 12 . 2h. 12.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述静置,静置时间为18-30h,分离提纯具体为:过滤取滤渣,依次用丙酮、乙醚、甲醇、蒸馏水分别洗涤3-5次,真空干燥。12. The method for preparing a cyclodextrin-Cu 2 O blended membrane for treating ppcps in regenerated water according to claim 1, characterized in that: the standing time is 18-30 h, and the separation and purification Specifically, the filter residue is collected by filtration, washed with acetone, ether, methanol, and distilled water for 3-5 times respectively, and vacuum-dried. 13.根据权利要求12所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述真空干燥,真空度为1200-4800pa,温度为55-60℃,干燥时间为2-20h。13. The method for preparing a cyclodextrin-Cu 2 O blend film for treating ppcps in regenerated water according to claim 12, characterized in that: the vacuum drying has a vacuum degree of 1200-4800pa and a temperature of 55 -60℃, drying time is 2-20h. 14.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述环糊精基材料为β-环糊精交联聚合物。14. The method for preparing a cyclodextrin-Cu 2 O blended film for treating ppcps in reclaimed water according to claim 1, wherein the cyclodextrin-based material is β-cyclodextrin cross-linked polymer. 15.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述偶联剂为硅烷类偶联剂,选自氨丙基三乙氧基硅烷(KH550),乙烯基三乙氧基硅烷(A151),乙烯基三甲氧基硅烷(A171),巯丙基三甲氧基硅烷(KH580),巯丙基三乙氧基硅烷(KH590)中的一种或几种。15. The method for preparing a cyclodextrin-Cu 2 O blend film for treating ppcps in regenerated water according to claim 1, wherein the coupling agent is a silane coupling agent selected from ammonia propyltriethoxysilane (KH550), vinyltriethoxysilane (A151), vinyltrimethoxysilane (A171), mercaptopropyltrimethoxysilane (KH580), mercaptopropyltriethoxy One or more of silanes (KH590). 16.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述PVDF粉末在所述有机溶剂中的浓度为0.25g/mL,所述PVP粉末在所述有机溶剂中的浓度为1:10-1:15g/mL,所述环糊精基-Cu2O复合材料与PVDF粉末的质量比为1:5-1:12。16. The method for preparing a cyclodextrin-Cu 2 O blend film for treating ppcps in regenerated water according to claim 1, wherein the concentration of the PVDF powder in the organic solvent is 0.25g /mL, the concentration of the PVP powder in the organic solvent is 1:10-1:15g/mL, and the mass ratio of the cyclodextrin-Cu 2 O composite material to the PVDF powder is 1:5-1 :12. 17.根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述有机溶剂为N,N-二甲基乙酰胺,N,N-二甲基甲酰胺、N-甲基吡咯烷酮、二甲基亚砜中的一种。17. The method for preparing a cyclodextrin-Cu 2 O blend film for treating ppcps in regenerated water according to claim 1, wherein the organic solvent is N,N-dimethylacetamide, One of N,N-dimethylformamide, N-methylpyrrolidone and dimethylsulfoxide. 18.所根据权利要求1所述的用于处理再生水中ppcps的环糊精基-Cu2O共混膜的制备方法,其特征在于:所述烘干,温度为55-60℃,烘干时间为2-20h。18. The method for preparing a cyclodextrin-Cu 2 O blend film for treating ppcps in regenerated water according to claim 1, wherein the drying is performed at a temperature of 55-60° C. The time is 2-20h.
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