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CN108484929A - A kind of metal organic frame synthesis MIL-53 (Al)-AO based on amidoxime2Preparation method - Google Patents

A kind of metal organic frame synthesis MIL-53 (Al)-AO based on amidoxime2Preparation method Download PDF

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CN108484929A
CN108484929A CN201810591989.6A CN201810591989A CN108484929A CN 108484929 A CN108484929 A CN 108484929A CN 201810591989 A CN201810591989 A CN 201810591989A CN 108484929 A CN108484929 A CN 108484929A
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dmf
uranium
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刘建明
刘胜楠
刘通
李健华
刘月明
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Tianjin Chengjian University
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    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/223Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
    • B01J20/226Coordination polymers, e.g. metal-organic frameworks [MOF], zeolitic imidazolate frameworks [ZIF]
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F1/285Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F2101/006Radioactive compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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Abstract

The invention discloses a kind of, and the metal organic frame based on amidoxime synthesizes MIL 53 (Al) AO2Preparation method, one:With 2 amino terephthalic acid (TPA)s and Al (NO3)3·9H2O is dissolved in DMF and deionized water prepares MIL 53 (Al) NH2Mixture A1;Two:A1 is washed into impurity with DMF and acrylonitrile respectively and obtains solid product A2;Three:By A2 plus acrylonitrile and Al Cl3Fully dissolve to obtain intermediate product A3;Four:A3 is distributed in ultra-pure water and alcohol mixeding liquid, K is added2CO3And NH2OHHCl reacts to obtain mixture A4;Five:Vacuum drying is MIL 53 (Al) AO after A4 ethyl alcohol and milli-Q water are filtered and detached2.Advantageous effect of the present invention:There is provided that a kind of yield is big, and equipment is simple, MIL 53 (Al) AO of easily operated control2Preparation method;Uranium is carried for uranium-bearing water body, and efficient material is provided.

Description

一种基于酰胺肟的金属有机框架合成MIL-53(Al)-AO2的制备 方法Preparation of MIL-53(Al)-AO2 Based on Metal-Organic Framework Synthesis of Amidoxime method

技术领域technical field

本发明涉及含铀废水、海水提铀领域,具体涉及基于酰胺肟的金属有机框架合成MIL-53(Al)-AO2的制备方法。The invention relates to the fields of uranium-containing wastewater and seawater extraction of uranium, in particular to a preparation method for synthesizing MIL-53(Al) -AO2 based on amidoxime-based metal-organic framework.

背景技术Background technique

随着核电产业的快速发展,核能的和平利用,产生大量放射性废物,其中含有不同种类的放射性核素。此外,在核燃料生产和加工过程中,不可避免地有一部分铀被释放到自然环境中。铀尾矿中分散的铀(Ⅵ)的污染是世界关注的问题。游离的铀(Ⅵ)离子可以通过食物链积累,最终进入人体循环系统。放射性的铀(Ⅵ)离子能购破坏人体的生物组织。为了公众健康和生态系统的稳定,清除废水中的放射性核素,将其释放到自然环境中至关重要。With the rapid development of the nuclear power industry and the peaceful use of nuclear energy, a large amount of radioactive waste is produced, which contains different types of radionuclides. In addition, some uranium is inevitably released into the natural environment during the production and processing of nuclear fuel. Contamination of dispersed uranium(VI) in uranium tailings is a worldwide concern. Free uranium (VI) ions can accumulate through the food chain and eventually enter the human circulatory system. Radioactive uranium (Ⅵ) ions can destroy biological tissues of the human body. Removing radionuclides from wastewater and releasing them into the natural environment is critical for public health and ecosystem stability.

卫生安全角度来看,铀具有化学毒性和放射性毒性,含铀废水具有相当浓度的铀能够对人体造成伤害,所以科学工程工作者不断探索新的方法来使含铀废水能够资源化,防止其对环境造成破坏。能源安全角度来看,铀是核工业发展的基础能源,确保能源安全的同时能够减少温室气体的排放。研究合成新型稳定高效的吸附剂,通过将吸附剂置于水溶液中以吸附水溶液中的铀,研究吸附剂的吸附能力、稳定性、吸附机制等从而为海水提取铀提供可能的研究方向。From the perspective of health and safety, uranium is chemically and radioactively toxic, and uranium-containing wastewater has a considerable concentration of uranium that can cause harm to the human body. Therefore, scientific and engineering workers continue to explore new methods to make uranium-containing wastewater recycle and prevent it from harming the human body. The environment wreaks havoc. From the perspective of energy security, uranium is the basic energy for the development of the nuclear industry, which can reduce greenhouse gas emissions while ensuring energy security. Research and synthesis of new stable and efficient adsorbents, by placing the adsorbent in aqueous solution to adsorb uranium in aqueous solution, and study the adsorption capacity, stability, adsorption mechanism, etc. of the adsorbent, so as to provide possible research directions for seawater extraction of uranium.

海水中溶解元素的主要成分是Cl、Na、Mg、S、Ca、Br、C、Sr、B,其比例超过99.9%。痕量的铀离子也存在于海水中。根据海水中的平均盐含量(约为3.5%),总盐浓度是铀含量的106–107倍。水介质中的铀具有长半衰期、复杂的配位化学,以及若干稳定的氧化态。铀在海水中的主要溶解态是六价铀(U6+)的三碳酸铀酰络合物[UO2(CO3)3]4–。海水中溶解铀物种的形态主要受CO2浓度和pH的影响。因此,海水中存在的HCO3 /CO3 2–缓冲剂有利于形成三碳酸铀酰络合物[UO2(CO3)3]4–。这个络合物在pH≈8是稳定,而在pH 6–8和5–7的范围容易分别分解为[UO2(CO3)2]2–和[UO2(CO3)]络合物。尽管海水中铀的浓度仅为3ppb(每立方米海水中含~3毫克的铀),所有海洋的巨大体积(约为13.7亿立方千米)中含大约45亿吨铀。如果这个资源有50%可以回收,将足以维持全球核反应堆运转约6500年。在多种锕系元素中,铀是核反应堆的主要和常见燃料。因此,人们有很大的兴趣从海水中提取铀,并使用它作为一种替代的可持续能源。The main components of dissolved elements in seawater are Cl, Na, Mg, S, Ca, Br, C, Sr, B, and their proportion exceeds 99.9%. Trace amounts of uranium ions are also present in seawater. Depending on the average salt content in seawater (about 3.5%), the total salt concentration is 10 6 -10 7 times the uranium content. Uranium in aqueous media has a long half-life, complex coordination chemistry, and several stable oxidation states. The main dissolved state of uranium in seawater is the uranyl tricarbonate complex of hexavalent uranium (U 6+ ) [UO 2 (CO 3 ) 3 ] 4– . The speciation of dissolved uranium species in seawater is mainly affected by CO2 concentration and pH. Therefore, the HCO 3 /CO 3 2– buffer in seawater is favorable for the formation of uranyl tricarbonate complex [UO 2 (CO 3 ) 3 ] 4– . This complex is stable at pH≈8, and easily decomposes into [UO 2 (CO 3 ) 2 ] 2– and [UO 2 (CO 3 )] complexes at pH 6–8 and 5–7, respectively . Although the concentration of uranium in seawater is only 3 ppb (-3 mg uranium per cubic meter of seawater), the vast volume of all oceans (approximately 1.37 billion cubic kilometers) contains about 4.5 billion tons of uranium. If 50% of this resource can be recovered, it will be enough to keep the world's nuclear reactors running for about 6,500 years. Among the various actinides, uranium is the main and common fuel for nuclear reactors. Therefore, there is great interest in extracting uranium from seawater and using it as an alternative sustainable energy source.

传统方法主要有化学沉淀、离子交换、蒸发浓缩、萃取、膜分离、电化学、沉降结晶、凝结絮凝和吸附法。吸附法具有适用范围广、高效以及富集效率高等特点,非常适合用于含铀废水中铀的分离和海水中铀的富集。但是,由于目前大多吸附剂的选择性吸附能力较低,不利于废水中铀的提取重复利用。The traditional methods mainly include chemical precipitation, ion exchange, evaporation concentration, extraction, membrane separation, electrochemistry, sedimentation crystallization, coagulation flocculation and adsorption. The adsorption method has the characteristics of wide application range, high efficiency and high enrichment efficiency, and is very suitable for the separation of uranium in uranium-containing wastewater and the enrichment of uranium in seawater. However, due to the low selective adsorption capacity of most adsorbents at present, it is not conducive to the extraction and reuse of uranium in wastewater.

酰胺肟官能团同时含有肟基和氨基,其未成键的孤对电子与铀酰离子发生配位作用形成螯合物。由于酰胺肟基对铀有很强的螯合作用,使其能够应用于修饰无机纳米材料和高分子聚合物,以提高吸附剂对铀的吸附容量。由于金属有机框架自身的比表面积、孔体积、金属含量具备相当程度的优势性能,以及金属有机框架能够以简单的实验条件在合成完成后根据实验目的进行相应改性。同时,酰胺肟基化合物所具备对铀很强的络合能力,酰胺肟基官能团在金属有机框架提高吸附剂对铀的吸附容量方面提供了新的突破。The amidoxime functional group contains both an oxime group and an amino group, and its unbonded lone pair of electrons coordinates with uranyl ions to form a chelate. Since the amidoxime group has a strong chelating effect on uranium, it can be applied to modify inorganic nano-materials and polymers to improve the adsorption capacity of the adsorbent for uranium. Because the specific surface area, pore volume, and metal content of metal organic frameworks have considerable advantages, and metal organic frameworks can be modified according to the purpose of the experiment after the synthesis is completed under simple experimental conditions. At the same time, the amidoxime-based compound has a strong complexing ability for uranium, and the amidoxime-based functional group provides a new breakthrough in improving the adsorption capacity of adsorbents for uranium by metal-organic frameworks.

发明内容Contents of the invention

针对现有的铀金属离子吸附富集和分离存在的问题,本发明结合偕胺肟基吸附速度快、高铀(Ⅵ)负载容量的性质和具备高度选择性的特点,提供了一种产量大,设备简单,易于操作控制,对水体中的铀表现出高效的选择性吸附效应的MIL-53(Al)-AO2的制备方法。MIL-53(Al)-AO2是一种引入酰胺肟基团的金属有机框架材料。Aiming at the problems existing in the existing adsorption, enrichment and separation of uranium metal ions, the present invention provides a high-yield The preparation method of MIL-53(Al)-AO 2 is simple in equipment, easy to operate and control, and exhibits efficient selective adsorption effect on uranium in water. MIL-53(Al)-AO 2 is a metal-organic framework material that introduces amidoxime groups.

为实现上述目的,本发明采用的技术方案是:一种基于酰胺肟的金属有机框架合成MIL-53(Al)-AO2的制备方法,步骤如下:In order to achieve the above object, the technical solution adopted in the present invention is: a kind of preparation method based on the metal organic framework of amidoxime synthesis MIL-53(Al)-AO , the steps are as follows:

(1)用0.56g的2-氨基对苯二甲酸和1.125g的Al(NO3)3·9H2O溶解于80mL N-N二甲基甲酰胺DMF和20mL去离子水混合液体中,充分搅拌后将混合液体置于200mL聚四氟乙烯内衬的不锈钢反应釜中,将反应釜置于真空干燥箱中调温度至150℃进行反应24小时,待反应结束后使其自然冷却至室温,用0.22μm孔尺寸的聚四氟乙烯微孔滤膜滤抽滤并用DMF溶液反复洗涤得到含MIL-53(Al)-NH2的混合物A1。(2)将步骤(1)中的混合物A1置于圆底烧瓶中,再次加入DMF洗杂质,用回流装置加热回流除去样品孔道中残留的2-氨基对苯二甲酸,用抽滤泵和滤膜抽滤使其固液分离,再用丙烯腈反复洗涤抽滤洗去DMF后,放到真空干燥箱干燥得到MIL-53(Al)-NH2的固体产物A2;(3)将步骤(2)所得固体产物A2置于200mL聚四氟乙烯内衬的不锈钢反应釜中,加入100mL丙烯腈和0.5g Al Cl3充分溶解并在恒温75℃下反应48h,后冷却至室温,用抽滤泵和滤膜抽滤得到MIL-53(Al)-N(CN)2,为中间产物A3;(4)将步骤(3)所得中间产物A3分布于10mL超纯水和90mL乙醇混合液中,再加入1.0gK2CO3和1.0gNH2OH·HCl充分搅拌溶解,密封条件下磁力搅拌并加热至80℃反应48h,后冷却至室温,用抽滤泵和滤膜抽滤得到含MIL-53(Al)-AO2的混合物A4;(5)将步骤(4)的固体产物A4,用乙醇和超纯水洗涤抽滤并分离固体产物,在60℃下真空干燥24h,即得MIL-53(Al)-AO2(1) Dissolve 0.56g of 2-aminoterephthalic acid and 1.125g of Al(NO 3 ) 3 ·9H 2 O in a mixed liquid of 80mL NN dimethylformamide DMF and 20mL deionized water, and stir thoroughly The mixed liquid was placed in a 200mL polytetrafluoroethylene-lined stainless steel reaction kettle, and the reaction kettle was placed in a vacuum drying oven and adjusted to 150°C for 24 hours of reaction. After the reaction was completed, it was naturally cooled to room temperature. A polytetrafluoroethylene microporous membrane with a pore size of μm was suction-filtered and washed repeatedly with DMF solution to obtain a mixture A1 containing MIL-53(Al)-NH 2 . (2) Place the mixture A1 in the step (1) in a round-bottomed flask, add DMF again to wash the impurities, heat and reflux with a reflux device to remove the residual 2-aminoterephthalic acid in the sample channel, and use a suction filter pump and filter Membrane suction filtration makes its solid-liquid separation, and then washes DMF repeatedly with acrylonitrile suction filtration, puts into vacuum drying oven and obtains MIL-53(Al)-NH 2 solid product A2; (3) step (2 ) The obtained solid product A2 was placed in a 200mL polytetrafluoroethylene-lined stainless steel reaction kettle, and 100mL acrylonitrile and 0.5g AlCl were added to fully dissolve and react at a constant temperature of 75°C for 48h, then cooled to room temperature, and filtered with a suction pump and membrane suction filtration to obtain MIL-53(Al)-N(CN) 2 , which is the intermediate product A3; (4) distribute the intermediate product A3 obtained in step (3) in 10mL ultrapure water and 90mL ethanol mixed solution, and then Add 1.0g K 2 CO 3 and 1.0g NH 2 OH·HCl and stir well to dissolve. Under sealed conditions, stir magnetically and heat to 80°C for 48 hours, then cool to room temperature, and use suction filtration pump and filter membrane to obtain MIL-53( Al)-AO mixture A4; (5) the solid product A4 of step (4), was washed with ethanol and ultrapure water and suction filtered to separate the solid product, and dried in vacuum at 60° C for 24h to obtain MIL-53 ( Al)-AO 2 .

本发明的有益效果是:针对目前含铀废水处理和海水提铀,本发明提供了一种产量大,设备简单,易于操作控制的一种酰胺肟引入金属有机框架合成MIL-53(Al)-AO2的制备方法。引入偕胺肟基,通过结合偕胺肟基快吸附速度、高铀(Ⅵ)负载容量的性质,在比表面积变小的情况下还能提高对铀的高效的选择性和保留吸附能力。本发明为含铀水体提铀提供了一种高效材料。The beneficial effect of the present invention is: aiming at the current uranium-containing wastewater treatment and seawater extraction of uranium, the present invention provides a kind of amidoxime with large output, simple equipment and easy operation and control to synthesize MIL-53(Al)- Preparation method of AO2 . The introduction of the amidoxime group, combined with the fast adsorption speed of the amidoxime group and the properties of high uranium (VI) loading capacity, can also improve the high-efficiency selectivity and retention adsorption capacity for uranium in the case of a smaller specific surface area. The invention provides a high-efficiency material for extracting uranium from uranium-containing water bodies.

附图说明Description of drawings

图1是MIL‐53(Al)‐AO2合成路线图;Figure 1 is a synthetic route diagram of MIL-53(Al)-AO 2 ;

图2是MIL-53(Al)(A),MIL-53(Al)-NH2(B)和MIL-53(Al)-AO2(C)的扫描电镜图像;Figure 2 is the SEM images of MIL-53(Al)(A), MIL-53(Al)-NH 2 (B) and MIL-53(Al)-AO 2 (C);

图3是MIL-53(Al)-AO2的N2物理吸脱附曲线。Fig. 3 is the N2 physical adsorption-desorption curve of MIL-53(Al) -AO2 .

具体实施方式Detailed ways

下面结合具体实施方式对本发明作进一步详细说明:Below in conjunction with specific embodiment the present invention is described in further detail:

步骤S1:用0.56g的2-氨基对苯二甲酸和1.125g的Al(NO3)3·9H2O溶解于80mL N-N二甲基甲酰胺DMF和20mL去离子水混合液体中,充分搅拌后将混合液体置于200mL聚四氟乙烯内衬的不锈钢反应釜中,将反应釜置于真空干燥箱中调温度至150℃进行反应24小时,待反应结束后使其自然冷却至室温,用0.22μm孔尺寸的聚四氟乙烯微孔滤膜滤抽滤并用DMF溶液反复洗涤得到含MIL-53(Al)-NH2的混合物A1。Step S1: Dissolve 0.56g of 2-aminoterephthalic acid and 1.125g of Al(NO 3 ) 3 ·9H 2 O in a mixed liquid of 80mL NN dimethylformamide DMF and 20mL deionized water, and stir thoroughly The mixed liquid was placed in a 200mL polytetrafluoroethylene-lined stainless steel reaction kettle, and the reaction kettle was placed in a vacuum drying oven and adjusted to 150°C for 24 hours of reaction. After the reaction was completed, it was naturally cooled to room temperature. A polytetrafluoroethylene microporous membrane with a pore size of μm was suction-filtered and washed repeatedly with DMF solution to obtain a mixture A1 containing MIL-53(Al)-NH 2 .

步骤S2:将步骤S1中的混合物A1置于圆底烧瓶中,再次加入DMF洗杂质,用回流装置加热回流除去样品孔道中残留的2-氨基对苯二甲酸,用抽滤泵和滤膜抽滤使其固液分离,再用丙烯腈反复洗涤抽滤洗去DMF后,放到真空干燥箱干燥得到MIL-53(Al)-NH2的固体产物A2;Step S2: Put the mixture A1 in step S1 in a round-bottomed flask, add DMF again to wash the impurities, heat and reflux with a reflux device to remove the residual 2-aminoterephthalic acid in the sample channel, and use a suction filter pump and a filter membrane to pump Filtrate to separate the solid from the liquid, then repeatedly wash with acrylonitrile to remove DMF by suction filtration, and then dry in a vacuum oven to obtain the solid product A2 of MIL-53(Al)-NH ;

步骤S3:将步骤S2所得固体产物A2置于200mL聚四氟乙烯内衬的不锈钢反应釜中,加入100mL丙烯腈和0.5g Al Cl3充分溶解并在恒温75℃下反应48h,后冷却至室温,用抽滤泵和滤膜抽滤得到MIL-53(Al)-N(CN)2,为中间产物A3;Step S3: Put the solid product A2 obtained in step S2 into a 200mL polytetrafluoroethylene-lined stainless steel reactor, add 100mL acrylonitrile and 0.5g AlCl3 to fully dissolve and react at a constant temperature of 75°C for 48h, then cool to room temperature , using suction filtration pump and filter membrane to obtain MIL-53(Al)-N(CN) 2 , which is the intermediate product A3;

步骤S4:将步骤S3所得中间产物A3分布于10mL超纯水和90mL乙醇混合液中,再加入1.0gK2CO3和1.0g NH2OH·HCl充分搅拌溶解,密封条件下磁力搅拌并加热至80℃反应48h,后冷却至室温,用抽滤泵和滤膜抽滤得到含MIL-53(Al)-AO2的混合物A4;Step S4: Distribute the intermediate product A3 obtained in step S3 in 10 mL of ultrapure water and 90 mL of ethanol mixture, then add 1.0 g of K 2 CO 3 and 1.0 g of NH 2 OH·HCl and stir to dissolve, stir magnetically under sealed conditions and heat to React at 80°C for 48h, then cool to room temperature, and filter with a suction filter pump and filter membrane to obtain a mixture A4 containing MIL-53(Al)-AO 2 ;

步骤S5:将步骤S4的固体产物A4,用乙醇和超纯水洗涤抽滤并分离固体产物,在60℃下真空干燥24h,即得MIL-53(Al)-AO2Step S5: The solid product A4 in step S4 was washed with ethanol and ultrapure water and filtered to isolate the solid product, and dried in vacuum at 60°C for 24 hours to obtain MIL-53(Al)-AO 2 .

如图1所示,MIL-53(Al)-AO2的合成路线结果表明酰胺肟基官能团可通过使用一系列较为简单便捷、实验条件不苛刻的氰乙基化反应合成方法直接接枝在MIL-53(Al)-NH2的苯环上。As shown in Figure 1, the synthesis route of MIL-53(Al)-AO 2 shows that the amidoxime functional group can be directly grafted on the MIL by using a series of relatively simple and convenient cyanoethylation reaction synthesis methods without harsh experimental conditions. On the benzene ring of -53(Al)-NH 2 .

如图2所示,扫描电镜图像(SEM)通过EPMA-8705QH2扫描电镜获得,在扫描电镜表征前需对样品材料进行60s喷金处理。根据MIL-53(Al)和MIL-53(Al)-NH2的扫描电镜图像可知,颗粒之间比较分散、无团聚现象,同时,扫描电镜图像表明MIL-53(Al)-NH2和MIL-53(Al)-AO2的空间尺寸没有明显的改变,间接说明酰胺肟基引入MIL-53(Al)-NH2的过程中其晶体形状没有发生较大变化。As shown in Figure 2, the scanning electron microscope image (SEM) was obtained by an EPMA-8705QH2 scanning electron microscope, and the sample material needs to be sprayed with gold for 60s before the SEM characterization. According to the scanning electron microscope images of MIL-53(Al) and MIL-53(Al)-NH 2 , the particles are relatively dispersed without agglomeration. At the same time, the scanning electron microscope images show that MIL-53(Al)-NH 2 and MIL The spatial size of -53(Al)-AO 2 did not change significantly, indirectly indicating that the crystal shape of the amidoxime group did not change significantly during the process of introducing the amidoxime group into MIL-53(Al)-NH 2 .

如图3所示,氮气吸附脱附曲线通过美国康塔Nova Win孔径分析仪得出,通过采用BET测试法计算吸附剂的比表面积计算出MIL-53(Al)-AO2的BET比表面积为179㎡/g,根据查阅文献得MIL-53(Al)-NH2的比表面积为1309㎡/g。一般吸附材料的比表面积越大吸附量越大,但是MIL-53(Al)-AO2的BET比表面积比MIL-53(Al)-NH2小,对铀(Ⅵ)的吸附效果更好,说明该发明酰胺肟的引入对铀(Ⅵ)的吸附将有突破性的进展。As shown in Figure 3, the nitrogen adsorption and desorption curve is obtained by the American Canta Nova Win pore size analyzer, and the BET specific surface area of MIL-53(Al)-AO2 is calculated to be 179 by using the BET test method to calculate the specific surface area of the adsorbent. ㎡/g, according to literature review, the specific surface area of MIL-53(Al)-NH2 is 1309㎡/g. Generally, the larger the specific surface area of the adsorption material, the greater the adsorption capacity, but the BET specific surface area of MIL-53(Al)-AO2 is smaller than that of MIL-53(Al)-NH2, and the adsorption effect on uranium(Ⅵ) is better. The introduction of the invention amidoxime will have a breakthrough in the adsorption of uranium (Ⅵ).

Claims (3)

1. a kind of metal organic frame based on amidoxime synthesizes MIL-53 (Al)-AO2Preparation method, include the following steps:
Step S1:With the 2- amino terephthalic acid (TPA) of 0.56g and the Al (NO of 1.125g3)3·9H2O is dissolved in 80mL N-N diformazans In base formamide DMF and 20mL deionized water mixing liquid, mixing liquid is placed in 200mL polytetrafluoroethylene (PTFE) after being sufficiently stirred In the stainless steel cauldron of lining, reaction kettle is placed in temperature regulating in vacuum drying chamber and to 150 DEG C react 24 hours, waits reacting After make its cooled to room temperature, filtered with the polytetrafluoroethylene (PTFE) miillpore filter filter of 0.22 μm of pore size and use DMF solution Washing obtains containing MIL-53 (Al)-NH repeatedly2Mixture A1;
Step S2:Mixture A1 in step S1 is placed in round-bottomed flask, DMF is added again and washes impurity, with reflux plus Heat reflux removes remaining 2- amino terephthalic acid (TPA) in sample duct, makes its separation of solid and liquid with suction filter pump and filter membrane suction filtration, then With acrylonitrile repeatedly wash suction filtration wash away DMF after, be put into vacuum drying chamber and be dried to obtain MIL-53 (Al)-NH2Solid product A2;
Step S3:Step S2 obtained solid products A2 is placed in the stainless steel cauldron of 200mL polytetrafluoroethyllining linings, is added 100mL acrylonitrile and 0.5g Al Cl3Fully dissolving and 48h is reacted at 75 DEG C of constant temperature, postcooling to room temperature, with suction filter pump and Filter membrane filters to obtain MIL-53 (Al)-N (CN)2, it is intermediate product A3;
Step S4:Intermediate product A3 obtained by step S3 is distributed in 10mL ultra-pure waters and 90mL alcohol mixeding liquids, is added 1.0gK2CO3With 1.0g NH2OHHCl is sufficiently stirred dissolving, and magnetic agitation and 80 DEG C of reaction 48h are heated under air-proof condition, Postcooling filters to obtain containing MIL-53 (Al)-AO to room temperature, with suction filter pump and filter membrane2Mixture A4;
Step S5:By the solid product A4 of step S4, solid product is filtered and detached with ethyl alcohol and milli-Q water, at 60 DEG C Vacuum drying is for 24 hours to get MIL-53 (Al)-AO2
2. a kind of metal organic frame based on amidoxime according to claim 1 synthesizes MIL-53 (Al)-AO2Preparation Method, it is characterised in that:2- amino terephthalic acid (TPA), Al (NO described in step S13)3·9H2O, DMF and deionized water ratio are 0.56g:1.125g:80mL:20mL, 150 DEG C of reactions of constant temperature are for 24 hours.
3. the preparation of metal organic frame synthesis MIL-53 (Al)-AO2 based on amidoxime according to claim 1 a kind of Method, it is characterised in that:In step S2,150 DEG C of reflux 8h in 400ml DMF.
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