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CN108654580A - A kind of order mesoporous zirconium phosphate material, preparation method and its application in waste water - Google Patents

A kind of order mesoporous zirconium phosphate material, preparation method and its application in waste water Download PDF

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CN108654580A
CN108654580A CN201810493339.8A CN201810493339A CN108654580A CN 108654580 A CN108654580 A CN 108654580A CN 201810493339 A CN201810493339 A CN 201810493339A CN 108654580 A CN108654580 A CN 108654580A
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zirconium phosphate
mesoporous zirconium
phosphate material
adsorption
mesoporous
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颜学武
廖雅杰
李洪
李晓山
黎皖豪
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Nanjing University of Science and Technology
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Nanjing University of Science and Technology
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28078Pore diameter
    • B01J20/28083Pore diameter being in the range 2-50 nm, i.e. mesopores
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/04Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/048Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium containing phosphorus, e.g. phosphates, apatites, hydroxyapatites
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/006Radioactive compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/16Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes

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  • Organic Chemistry (AREA)
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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

The invention discloses a kind of order mesoporous zirconium phosphate material, preparation method and its applications in waste water.Using template as the structure directing agent of synthesising mesoporous basic zirconium phosphate so that alcohol solvent slowly volatilizees, and one-step synthesis forms the basic zirconium phosphate with three dimensions;The present invention's uses the zirconium phosphate material of meso-hole structure for adsorbent, simultaneously, chemisorption is carried out to the uranyl ion in solution under the conditions of isothermal vibration, the uranyl ion in waste water is rapidly complexed with the phosphonic functional groups of material surface, more efficient absorption uranyl ion;The order mesoporous zirconium phosphate material preparation method of the present invention is simply inexpensive, can handle the demand of nuclear power station Uranium in Waste Water, and treated, and sample is also easy to recycle, and has preferable application market.

Description

一种有序介孔磷酸锆材料、制备方法及其在废水中的应用A kind of ordered mesoporous zirconium phosphate material, its preparation method and its application in wastewater

技术领域technical field

本发明应用于处理放射性铀废水的环保领域,具体涉及介孔磷酸锆制备和利用其吸附分离废水中放射性铀酰离子。The invention is applied to the environmental protection field of treating radioactive uranium wastewater, and in particular relates to the preparation of mesoporous zirconium phosphate and its use for adsorption and separation of radioactive uranyl ions in wastewater.

背景技术Background technique

核能是近代新开发利用的能源,核能作为较清洁的能源,有着效能高的优点。同样地,在铀矿等含有放射性核素矿山开采以及冶炼的过程中产生的放射性废物,不仅给人类赖以生存的环境带来污染,在生产过程中排放的放射性核素也造成资源的浪费。Nuclear energy is a newly developed and utilized energy in modern times. As a relatively clean energy source, nuclear energy has the advantage of high efficiency. Similarly, the radioactive waste produced during the mining and smelting of uranium ore and other mines containing radionuclides not only pollutes the environment on which human beings depend, but also causes waste of resources due to the radionuclides discharged during the production process.

目前,处理放射性废水的主要机理是将中低水平的放射性废水中的放射性物质富集成为高放射性水平的废水,其余废水达到排放标准而进行下一步的处理。从废水中提铀的主要方法有吸附法、浮选法、溶剂萃取分离法、生物处理法、离子交换法、化学沉淀法、超导磁分离法等。吸附法是目前研究最多的方法之一,吸附法提取铀的研究重点是研究开发新型铀吸附材料。At present, the main mechanism for treating radioactive wastewater is to enrich the radioactive substances in low- and medium-level radioactive wastewater into high-level radioactive wastewater, and the rest of the wastewater reaches the discharge standard for further treatment. The main methods for extracting uranium from wastewater include adsorption, flotation, solvent extraction separation, biological treatment, ion exchange, chemical precipitation, superconducting magnetic separation, etc. The adsorption method is one of the most researched methods at present, and the research focus of the extraction of uranium by the adsorption method is to research and develop new uranium adsorption materials.

吸附法处理放射性废水不会给水体带来二次污染物质,吸附剂与放射性核素形成的沉淀物质可以较容易的与水体分离。且通过脱附过程,可以将废液中的放射性核素重新资源化利用。现在分离富集废水中的铀酰离子所面对的问题是:(1)材料制备过程复杂,成本高,不易放大生产,不利于实际应用。(2)一般吸附剂如硅藻土,沸石,活性炭,膨润土的物理吸附,吸附量低。(文献1:S.Kumar,V.A.Loganathan,R.B.Gupta,M.O.Barnett,Anassessment of U(VI)removal from groundwater using biochar produced fromhydrothermal carbonization,J.Environ.Manage.2011,92:2504–2512)(3)在多种离子存在时不具有特异选择吸附性,文献2(Xia Liu,Jiaxing Li,Xiangxue Wang,ChanglunChen,Xiangke Wang.High performance of phosphate-functionalized graphene oxidefor the selective adsorption of U(VI)from acidic solution.Journal of NuclearMaterials.2015,466:56-64)研究了磷酸功能化的材料吸附废水中的铀酰离子获得了较好的效果,吸附量远远高于非磷酸功能化的材料。Adsorption treatment of radioactive wastewater will not bring secondary pollutants to the water body, and the precipitate formed by the adsorbent and radionuclides can be easily separated from the water body. And through the desorption process, the radionuclides in the waste liquid can be reused as resources. The problems faced by the separation and enrichment of uranyl ions in wastewater are: (1) The material preparation process is complicated, the cost is high, and it is not easy to scale up production, which is not conducive to practical application. (2) Physical adsorption of general adsorbents such as diatomite, zeolite, activated carbon, and bentonite has low adsorption capacity. (Document 1: S.Kumar, V.A.Loganathan, R.B.Gupta, M.O.Barnett, Anassessment of U(VI) removal from groundwater using biochar produced from hydrothermal carbonization, J.Environ.Manage.2011, 92:2504–2512) (3) in There is no specific selective adsorption in the presence of multiple ions, literature 2 (Xia Liu, Jiaxing Li, Xiangxue Wang, Changlun Chen, Xiangke Wang. High performance of phosphate-functionalized graphene oxide for the selective adsorption of U(VI) from acidic solution. Journal of Nuclear Materials.2015, 466:56-64) studied that phosphoric acid-functionalized materials adsorb uranyl ions in wastewater and achieved better results, and the adsorption capacity is much higher than that of non-phosphoric acid-functionalized materials.

发明内容Contents of the invention

针对现有处理含铀废水的吸附材料存在的问题,本发明提供了一种有序介孔磷酸锆材料,本发明所制备的吸附剂介孔磷酸锆具有有序纳米孔道,较高的比表面积,选择吸附性,结构稳定,易回收且对环境友好等优点。为实现上述优点,本实验采取的技术方案为:Aiming at the problems existing in the existing adsorbent materials for treating uranium-containing wastewater, the present invention provides an ordered mesoporous zirconium phosphate material. The adsorbent mesoporous zirconium phosphate prepared by the present invention has ordered nanopore channels and a relatively high specific surface area , selective adsorption, stable structure, easy recycling and environmental friendliness. In order to achieve the above advantages, the technical scheme adopted in this experiment is as follows:

一种有序介孔磷酸锆材料,采用溶胶-凝胶法及溶剂挥发自组装(EISA)制备介孔磷酸锆材料,利用模板剂作为合成介孔磷酸锆的结构导向剂,使得乙醇溶剂缓慢挥发,一步合成形成具有三维空间的磷酸锆。包括以下步骤:An ordered mesoporous zirconium phosphate material, prepared by sol-gel method and solvent evaporation self-assembly (EISA), using a template as a structure-directing agent for synthesizing mesoporous zirconium phosphate, so that ethanol solvent volatilizes slowly , one-step synthesis to form zirconium phosphate with three-dimensional space. Include the following steps:

(1)模板剂F127为导向剂溶解在无水乙醇溶剂中。(1) The template agent F127 was dissolved in anhydrous ethanol solvent as the directing agent.

(2)以ZroCl2.8H2O和PO(OCH3)3分别作为锆源和磷源,加入(1)中,磁力搅拌4-10h。(2) Add ZroCl 2 .8H 2 O and PO(OCH 3 ) 3 as zirconium source and phosphorus source respectively to (1), and magnetically stir for 4-10 hours.

(3)将(2)的溶液倒入培养皿中,在333K放置48h,然后383K放置24h,得到前驱体干凝胶。(3) Pour the solution of (2) into a petri dish, place it at 333K for 48 hours, and then place it at 383K for 24 hours to obtain the precursor xerogel.

(4)前驱体干凝胶下放置在马弗炉中773K煅烧,所得材料命名为MZrP-773K。(4) The precursor xerogel was placed in a muffle furnace for calcination at 773K, and the obtained material was named MZrP-773K.

优选的,步骤(1)中F127:(P+Zr)的摩尔比为0.01。Preferably, the molar ratio of F127:(P+Zr) in step (1) is 0.01.

优选的,步骤(2)中ZroCl2.8H2O和PO(OCH3)3的摩尔比为0.75。Preferably, the molar ratio of ZroCl 2 .8H 2 O to PO(OCH 3 ) 3 in step (2) is 0.75.

进一步,步骤(3)中,步骤(2)溶液倒入培养皿时覆盖一层保鲜膜,并带有小孔,防止无水乙醇溶剂挥发过快。Further, in step (3), when the solution in step (2) is poured into the petri dish, it is covered with a layer of plastic wrap with small holes to prevent the absolute ethanol solvent from volatilizing too quickly.

进一步优化,步骤(4)中煅烧的升温速率为1K/min,773K煅烧4h。Further optimization, the heating rate of calcination in step (4) is 1K/min, and calcination at 773K for 4h.

本发明与现有技术相比,优点是:Compared with the prior art, the present invention has the advantages of:

(1)本发明的吸附剂为介孔结构的磷酸锆材料,有序介孔结构提供了更大的吸附反应接触面积。(1) The adsorbent of the present invention is a zirconium phosphate material with a mesoporous structure, and the ordered mesoporous structure provides a larger adsorption reaction contact area.

(2)该材料在恒温震荡条件下对溶液中的铀酰离子进行化学吸附,废水中的铀酰离子快速地与材料表面的磷酸官能团络合,而非一般的物理吸附,从而更高效的吸附铀酰离子。(2) The material chemically adsorbs uranyl ions in the solution under constant temperature and shaking conditions, and the uranyl ions in the wastewater quickly complex with the phosphoric acid functional groups on the surface of the material instead of general physical adsorption, so that the adsorption is more efficient Uranyl ion.

(3)材料本身是耐酸性材料,在强酸条件下,吸附铀酰离子的介孔磷酸锆能够快速脱附铀酰离子,吸附材料可循环再利用,从而达到了分离富集废水中铀酰离子的目的。(3) The material itself is an acid-resistant material. Under strong acid conditions, the mesoporous zirconium phosphate that adsorbs uranyl ions can quickly desorb uranyl ions, and the adsorption material can be recycled, thereby achieving the separation and enrichment of uranyl ions in wastewater. the goal of.

(4)材料制备方法简单低成本,能够处理核电站废水中铀的需求,处理后的样品也易于再利用,具有较好的应用市场。(4) The preparation method of the material is simple and low-cost, and it can handle the demand for uranium in nuclear power plant wastewater, and the treated samples are easy to reuse, so it has a good application market.

附图说明Description of drawings

图1为本发明的有序介孔磷酸锆材料的XRD图;Fig. 1 is the XRD figure of ordered mesoporous zirconium phosphate material of the present invention;

图2为本发明的有序介孔磷酸锆材料的SEM;Fig. 2 is the SEM of ordered mesoporous zirconium phosphate material of the present invention;

图3为本发明的有序介孔磷酸锆材料的FTIR图;Fig. 3 is the FTIR figure of ordered mesoporous zirconium phosphate material of the present invention;

图4为本发明的有序介孔磷酸锆材料的N2吸脱附等温曲线;Fig. 4 is the N of ordered mesoporous zirconium phosphate material of the present invention Adsorption - desorption isotherm curve;

图5为本发明的有序介孔磷酸锆材料的XPS光谱图;Fig. 5 is the XPS spectrogram of ordered mesoporous zirconium phosphate material of the present invention;

图6为实施例中有序介孔磷酸锆材料在不同初始浓度下对铀酰离子的吸附效果图;Fig. 6 is a diagram showing the adsorption effect of ordered mesoporous zirconium phosphate materials on uranyl ions at different initial concentrations in the embodiment;

图7为实施例中有序介孔磷酸锆材料在不同pH下对铀酰离子的吸附效果图;Fig. 7 is a graph showing the adsorption effect of ordered mesoporous zirconium phosphate materials on uranyl ions at different pHs in the embodiment;

图8为实施例中有序介孔磷酸锆材料在不同吸附时间下对铀酰离子的吸附效果图;Fig. 8 is a diagram of the adsorption effect of ordered mesoporous zirconium phosphate materials on uranyl ions at different adsorption times in the embodiment;

图9为实施例中有序介孔磷酸锆材料在多种金属离子存在下对铀酰离子的吸附效果图。Fig. 9 is a graph showing the adsorption effect of ordered mesoporous zirconium phosphate materials on uranyl ions in the presence of various metal ions in the embodiment.

具体实施方式Detailed ways

(1)有序介孔磷酸锆材料的制备(1) Preparation of ordered mesoporous zirconium phosphate materials

本发明提供了一种介孔结构的材料在含铀废水处理领域的应用,发现其对废水中铀酰离子有较强的吸附性能并可多次使用。The invention provides an application of a mesoporous structure material in the field of uranium-containing wastewater treatment, and it is found that it has strong adsorption performance for uranyl ions in the wastewater and can be used for many times.

(2)材料性能表征测试(2) Material performance characterization test

利用SEM、TEM、XRD、FTIR、BET和XPS对材料进行表征测试。The materials were characterized by SEM, TEM, XRD, FTIR, BET and XPS.

(3)材料的吸附性能测试(3) Material adsorption performance test

吸附材料在不同初始浓度,pH,接触时间和多种金属离子存在条件下下对铀酰离子的吸附性能,以及材料的吸附动力模型。The adsorption properties of adsorption materials for uranyl ions under different initial concentrations, pH, contact time and the presence of various metal ions, as well as the adsorption kinetic model of materials.

实施例Example

介孔磷酸锆材料的制备Preparation of Mesoporous Zirconium Phosphate Materials

(1)采用溶胶-凝胶法和溶剂挥发自组装(EISA),将1.2g模板剂F127加入于13ml的无水乙醇溶剂中,采用油浴加热,控温在303K,磁力搅拌至澄清。(1) Using sol-gel method and solvent evaporation self-assembly (EISA), add 1.2g of template agent F127 into 13ml of absolute ethanol solvent, heat in an oil bath, control the temperature at 303K, and stir magnetically until clarified.

(2)称取1.6125g(5mmol)的锆源ZroCl2.8H2O原材料加到步骤(1)的溶液中,搅拌至完全溶解;将0.5253g(3.75mmol)的磷源PO(OCH3)3溶在2ml的无水乙醇后,缓慢滴加到上述溶液中,其中P/Zr=0.5-1.0,磁力搅拌6h。(2) Weigh 1.6125g (5mmol) of zirconium source ZroCl 2 .8H 2 O and add it to the solution in step (1), stir until completely dissolved; add 0.5253g (3.75mmol) of phosphorus source PO(OCH 3 ) 3 was dissolved in 2ml of absolute ethanol, slowly added dropwise to the above solution, where P/Zr=0.5-1.0, and magnetically stirred for 6h.

(3)将(2)的溶液倒入培养皿中,在培养皿上覆盖一层保鲜膜并留有小孔,在烘箱中333K放置48h,然后383K放置24h,得到干凝胶即为介孔磷酸锆的前驱体。(3) Pour the solution of (2) into a petri dish, cover a layer of plastic wrap on the petri dish and leave a small hole, place it in an oven at 333K for 48 hours, and then place it at 383K for 24 hours to obtain a dry gel that is mesoporous Precursor of zirconium phosphate.

(4)将上述的前驱体干凝胶放置在马弗炉中煅烧,升温速率为1℃/min,在773K煅烧4h,自然降温至303K。(4) The above-mentioned precursor xerogel was calcined in a muffle furnace at a heating rate of 1 °C/min, calcined at 773K for 4 hours, and then naturally cooled to 303K.

材料性能测试Material Performance Testing

1 X射线衍射分析(XRD)1 X-ray diffraction analysis (XRD)

本发明实施例吸附剂介孔磷酸锆的X射线衍射分析如图1所示,采用德国Bruker公司生产的D8Advance型X射线衍射仪(XRD)对试样进行物相分析,测试条件为:石墨单色器,Cu-Kα辐射,辐射波长λ=0.15418nm,管电压40kV,管电流40mA,扫描角度范围2θ=0.6-10。在图1中,四条曲线a,b,c,d表示材料制备时P/Zr的摩尔比分别为0.75,1,0.5,0.25,从图1中可以清楚地看到,在小角范围内扫描,在2θ=0.80-0.9°处四条曲线都出现很强的衍射峰,其为(100)晶面,但是可以明显的发现,随着P/Zr的摩尔比的增加,该处衍射峰逐渐增强;当P/Zr=0.75时衍射峰强度最强;当P/Zr>0.75时衍射峰强度又明显降低。而2θ=1.55-1.65°处的衍射峰其为(110)晶面,在图1上a,b曲线在该位置出现一个较弱的衍射峰,而c,d曲线在该位置没有出现衍射峰。所以通过XRD表征明显看出,当材料制备的P/Zr=0.75时合成的介孔磷酸锆材料的结构更均一有序,P/Zr=0.75是材料制备的最佳摩尔比,再采用谢乐公式计算出摩尔比P/Zr=0.75的合成材料的孔道直径为5.673nm,通过对材料做扫描电镜(SEM)和N2吸附脱附测试进一步说明材料的结构。The X-ray diffraction analysis of the adsorbent mesoporous zirconium phosphate of the embodiment of the present invention is as shown in Figure 1, adopts the D8Advance type X-ray diffractometer (XRD) that German Bruker Company produces to carry out phase analysis to sample, and test condition is: graphite single Chromatic device, Cu-Kα radiation, radiation wavelength λ=0.15418nm, tube voltage 40kV, tube current 40mA, scanning angle range 2θ=0.6-10. In Figure 1, the four curves a, b, c, and d indicate that the molar ratio of P/Zr during material preparation is 0.75, 1, 0.5, 0.25, respectively. It can be clearly seen from Figure 1 that scanning in the small angle range, All four curves at 2θ=0.80-0.9° have strong diffraction peaks, which are (100) crystal planes, but it can be clearly found that with the increase of the molar ratio of P/Zr, the diffraction peaks at this place are gradually enhanced; When P/Zr=0.75, the intensity of diffraction peak is the strongest; when P/Zr>0.75, the intensity of diffraction peak decreases obviously. And the diffraction peak at 2θ=1.55-1.65° is the (110) crystal plane. In Figure 1, a and b curves have a weaker diffraction peak at this position, while c and d curves do not have a diffraction peak at this position . Therefore, it is obvious from the XRD characterization that the structure of the synthesized mesoporous zirconium phosphate material is more uniform and orderly when the material is prepared with P/Zr=0.75, and P/Zr=0.75 is the best molar ratio for material preparation. The formula calculates that the pore diameter of the synthetic material with the molar ratio P/Zr=0.75 is 5.673nm, and the structure of the material is further illustrated by scanning electron microscopy (SEM) and N2 adsorption and desorption tests on the material.

2扫描电镜(SEM)形貌分析2 Scanning electron microscope (SEM) morphology analysis

扫描电镜和透射电镜形貌分析如图2所示,采用Quant 250FEG(FEI)扫描电子显微镜对所制得的样品进行形貌表征,加速电压为30kV。图2为材料介孔磷酸锆材料的扫描电镜图,从图中可见,在放大5500倍至2um左右,材料表面平滑,切口平整,块状结构,结合XRD表征结果分析,材料属于具有三维有序纳米孔道的块状结构。Scanning electron microscope and transmission electron microscope morphology analysis As shown in Figure 2, the morphology of the prepared samples was characterized using a Quant 250FEG (FEI) scanning electron microscope with an accelerating voltage of 30kV. Figure 2 is the scanning electron microscope image of the material mesoporous zirconium phosphate material. It can be seen from the figure that the surface of the material is smooth, the incision is flat, and the block structure is magnified by 5500 times to about 2um. Combined with the analysis of XRD characterization results, the material belongs to a three-dimensional order The bulk structure of nanopores.

3傅里叶红外光谱分析(FT-IR)3 Fourier transform infrared spectroscopy (FT-IR)

傅里叶红外光谱分析采用美国Thermo Fisher Scientific公司生产的Nicoletis10傅里叶变换红外光谱仪。材料的FT-IR光谱如图3所示,与煅烧材料相比,1630cm-1的吸收带归因于不对称水分子的O-H弯曲振动;3000~2800cm-1,1463cm-1和1355cm-1的吸收带属于模板剂F127中的不饱和C-H伸缩振动吸收峰,此峰经过773K煅烧后消失,说明高温煅烧可以完全去除模板和残留溶剂;而1000-1200cm-1处的吸收带对应于不对称P-O的伸缩振动峰;吸收带1640cm-1则归因于P-O的伸缩振动峰和弯曲振动峰,在经过吸附后材料此处的谱带明显弱于未做吸附实验的材料,说明P-O基团参与材料吸附过程;吸收谱带在960cm-1处,磷酸盐中P-OH的对称伸缩振动归属于磷酸盐中的峰,在960cm-1处消失,煅烧后磷酸盐的弯曲振动吸收峰出现在600cm-1处,表明磷在煅烧材料中以PO的形式存在。The Fourier transform infrared spectrometer was analyzed using a Nicoletis 10 Fourier transform infrared spectrometer produced by Thermo Fisher Scientific, USA. The FT-IR spectrum of the material is shown in Figure 3. Compared with the calcined material, the absorption band at 1630cm-1 is attributed to the O-H bending vibration of asymmetric water molecules; The absorption band belongs to the unsaturated C-H stretching vibration absorption peak in the template agent F127, which disappears after calcination at 773K, indicating that high-temperature calcination can completely remove the template and residual solvent; and the absorption band at 1000-1200cm-1 corresponds to the asymmetric P-O stretching vibration peak; the absorption band of 1640cm-1 is attributed to the stretching vibration peak and bending vibration peak of P-O. Adsorption process; the absorption band is at 960cm-1, the symmetrical stretching vibration of P-OH in phosphate belongs to the peak in phosphate, and disappears at 960cm-1, and the bending vibration absorption peak of phosphate appears at 600cm-1 after calcination 1, indicating that phosphorus exists in the form of PO in the calcined material.

4比表面积分析(BET)4 specific surface area analysis (BET)

图4为本发明实施例的CoMn2O4和CoMn2O4/rGO的N2吸脱附等温曲线,采用美国Micromeritics公司生产的ASAP 2020物理吸附仪测定。所制备的介孔磷酸锆材料的吸附脱附等温线均属于典型的IV型等温线,产生滞后现象,并出现滞后环,说明两种材料均存在孔隙结构。根据BET吸附等温方程和BJH模型计算得到的比表面积为217.6157m2g-1,孔径为5.8859nm,本发明的介孔磷酸锆材料的比表面积要比以前文献报道的非纳米结构材料要大。这提供了更大的比表面积和更多的活性位点,有利于反应过程中的对铀酰离子的吸附。Fig. 4 is the N 2 adsorption-desorption isotherm curves of CoMn 2 O 4 and CoMn 2 O 4 /rGO according to the examples of the present invention, which are measured by ASAP 2020 physical adsorption instrument produced by Micromeritics Company of the United States. The adsorption-desorption isotherms of the prepared mesoporous zirconium phosphate materials belong to the typical type IV isotherms, resulting in hysteresis and hysteresis loops, indicating that both materials have pore structures. The specific surface area calculated according to the BET adsorption isotherm equation and BJH model is 217.6157m 2 g -1 , and the pore diameter is 5.8859nm. The specific surface area of the mesoporous zirconium phosphate material of the present invention is larger than that of the non-nanostructured materials reported in previous literatures. This provides a larger specific surface area and more active sites, which is beneficial to the adsorption of uranyl ions during the reaction.

5 XPS测试5 XPS test

为进一步证明铀酰离子吸附在介孔磷酸锆材料表面,采用日本真空生产的PHIQUANTERA II型仪器得到该材料的XPS全谱。介孔磷酸锆材料的XPS全谱如图5所示,从图中可以看出,该材料包含4中元素,它们分别是锆(Zr)、氧(O)、磷(P)和碳(C),但该材料在吸附后,XPS谱图在392eV,381eV处出现较强的铀的特征峰U4f,这说明废水中的铀(U)的确被吸附在材料的表面。In order to further prove that uranyl ions are adsorbed on the surface of the mesoporous zirconium phosphate material, the full XPS spectrum of the material was obtained using a PHIQUANTERA II instrument produced by Japan Vacuum. The full XPS spectrum of the mesoporous zirconium phosphate material is shown in Figure 5. It can be seen from the figure that the material contains four elements, which are zirconium (Zr), oxygen (O), phosphorus (P) and carbon (C ), but after the material is adsorbed, a strong characteristic peak U4f of uranium appears in the XPS spectrum at 392eV and 381eV, which indicates that uranium (U) in the wastewater is indeed adsorbed on the surface of the material.

材料的吸附性能应用The application of adsorption performance of materials

如图6为不同初始浓度的铀酰离子对吸附的影响。以介孔磷酸锆材料为吸附剂吸附废水中的铀酰离子。吸附反应在恒温震荡箱中进行,控制温度298K,震荡速率180r/min。取6组为pH为4.5但是不同初始浓度(10mg/L,40mg/L,70mg/L,100mg/L,130mg/L,160mg/L)不同的含有铀溶液50mL,然后分别加入0.01g的介孔磷酸锆,恒温震荡24h后,测得各组介孔磷酸锆对铀酰离子的吸附量和去除率。结果如图6所示,随着初始浓度的升高,介孔磷酸锆对铀酰离子的吸附量越来越高,从11mg/g增加到114mg/g,但铀酰离子的去除率越来越低,从37%降到25%左右,所以由图可得,在初始浓度为100mg/L时,吸附剂对铀酰离子的吸附量和去除率都较高,其为最佳初始浓度。Figure 6 shows the effect of different initial concentrations of uranyl ions on the adsorption. The mesoporous zirconium phosphate material is used as an adsorbent to adsorb uranyl ions in wastewater. The adsorption reaction is carried out in a constant temperature shaking box, the temperature is controlled at 298K, and the shaking rate is 180r/min. Take 6 groups of uranium-containing solutions with a pH of 4.5 but different initial concentrations (10mg/L, 40mg/L, 70mg/L, 100mg/L, 130mg/L, 160mg/L) containing 50mL of uranium solutions, and then add 0.01g of medium Porous zirconium phosphate was shaken at constant temperature for 24 hours, and the adsorption capacity and removal rate of uranyl ions in each group of mesoporous zirconium phosphate were measured. The results are shown in Figure 6. As the initial concentration increases, the adsorption capacity of mesoporous zirconium phosphate to uranyl ions is getting higher and higher, from 11 mg/g to 114 mg/g, but the removal rate of uranyl ions is getting lower and higher. The lower it is, it drops from 37% to about 25%, so it can be seen from the figure that when the initial concentration is 100mg/L, the adsorption capacity and removal rate of the adsorbent for uranyl ions are high, which is the optimal initial concentration.

如图7是不同pH的吸附溶液对吸附性能的影响。以介孔磷酸锆材料为吸附剂吸附废水中的铀酰离子。吸附反应在恒温震荡箱中进行,控制温度298K,震荡速率180r/min。取8组不同pH(pH=3,4,4.5,5,5.5,6,6.5,7)但初始浓度为100mg/L的含铀吸附液50ml,然后分别加入0.01g的介孔磷酸锆,恒温震荡24h后,测得各组介孔磷酸锆对铀酰离子的吸附量。结果如图7所示,当pH=3-6.5时,随着pH的升高,介孔磷酸锆吸附量不断增加,当pH>6.5后,介孔磷酸锆的吸附量降低,但当pH>5.5时,吸附液中的铀酰离子会与溶液中的OH-反应,生成淡黄色的沉淀,所以选择pH=5.5为最佳pH,。Figure 7 shows the effect of different pH adsorption solutions on the adsorption performance. The mesoporous zirconium phosphate material is used as an adsorbent to adsorb uranyl ions in wastewater. The adsorption reaction is carried out in a constant temperature shaking box, the temperature is controlled at 298K, and the shaking rate is 180r/min. Take 50ml of uranium-containing adsorption solutions with 8 groups of different pH (pH=3,4,4.5,5,5.5,6,6.5,7) but the initial concentration is 100mg/L, then add 0.01g of mesoporous zirconium phosphate respectively, After shaking for 24 hours, the adsorption capacity of mesoporous zirconium phosphate on uranyl ions was measured. The results are shown in Figure 7. When pH=3-6.5, the adsorption capacity of mesoporous zirconium phosphate increases continuously with the increase of pH. When pH>6.5, the adsorption capacity of mesoporous zirconium phosphate decreases, but when pH> When the pH is 5.5, the uranyl ions in the adsorption solution will react with the OH- in the solution to form a light yellow precipitate, so choose pH = 5.5 as the optimal pH.

如图8是不同的接触反应时间对吸附性能的影响。以介孔磷酸锆材料为吸附剂吸附废水中的铀酰离子。吸附反应在恒温震荡箱中进行,控制温度298K,震荡速率180r/min。取pH=5.5,初始浓度为100mg/L的吸附溶液50ml,加入0.01g的介孔磷酸锆,恒温震荡,取9次不同接触反应时间T(T=5min,10min,20min,30min,1h,2h,4h,6h,16h)的吸附溶液,测得各组介孔磷酸锆对铀酰离子的吸附量。结果如图8所示,当T小于6h时,随着接触反应时间的的增加,介孔磷酸锆吸附量不断增加,当T大于等于6h时,介孔磷酸锆材料对铀酰离子的吸附量趋于平缓,所以介孔磷酸锆材料对铀酰离子的最佳接触反应时间为6h,而再对所得数据进行拟合,得到最大吸附量为298.37mg/g。Figure 8 shows the effect of different contact reaction times on the adsorption performance. The mesoporous zirconium phosphate material is used as an adsorbent to adsorb uranyl ions in wastewater. The adsorption reaction is carried out in a constant temperature shaking box, the temperature is controlled at 298K, and the shaking rate is 180r/min. Take 50ml of adsorption solution with pH=5.5 and initial concentration of 100mg/L, add 0.01g of mesoporous zirconium phosphate, shake at constant temperature, take 9 different contact reaction times T (T=5min, 10min, 20min, 30min, 1h, 2h , 4h, 6h, 16h) of the adsorption solution, and measured the amount of adsorption of uranyl ions by mesoporous zirconium phosphate in each group. The results are shown in Figure 8. When T is less than 6h, the adsorption amount of mesoporous zirconium phosphate increases continuously with the increase of contact reaction time. When T is greater than or equal to 6h, the adsorption amount of mesoporous zirconium phosphate material to uranyl ions tends to be flat, so the best contact reaction time of mesoporous zirconium phosphate material to uranyl ions is 6h, and then fitting the obtained data, the maximum adsorption capacity is 298.37mg/g.

如图9是含多种金属离子的吸附溶液对吸附性能的影响。以介孔磷酸锆材料为吸附剂吸附废水中的铀酰离子。吸附反应在恒温震荡箱中进行,控制温度298K,震荡速率180r/min。取pH=5.5,初始浓度为100mg/L的吸附溶液50ml,其中含有多种金属离子(Na+,K+,Mg2+,Mn2+,Co2+,Ni2+,Sr2+)各100mg/L,加入0.01g的介孔磷酸锆,恒温震荡24h后,测得各组介孔磷酸锆对铀酰离子的吸附量。结果如图9所示,多种金属离子的存在时,介孔磷酸锆的对铀酰离子吸附量仍然高达290mg/g,约占总吸附量的85.37%,所以介孔磷酸锆对铀酰离子有选择性吸附。Figure 9 shows the effect of the adsorption solution containing various metal ions on the adsorption performance. The mesoporous zirconium phosphate material is used as an adsorbent to adsorb uranyl ions in wastewater. The adsorption reaction is carried out in a constant temperature shaking box, the temperature is controlled at 298K, and the shaking rate is 180r/min. Take 50ml of adsorption solution with pH=5.5 and initial concentration of 100mg/L, which contains 100mg/L of various metal ions (Na+, K+, Mg2+, Mn2+, Co2+, Ni2+, Sr2+), add 0.01g of mesoporous zirconium phosphate , after shaking at constant temperature for 24 hours, the adsorption capacity of mesoporous zirconium phosphate on uranyl ions was measured. The results are shown in Figure 9. In the presence of various metal ions, the adsorption capacity of mesoporous zirconium phosphate to uranyl ions is still as high as 290 mg/g, accounting for about 85.37% of the total adsorption capacity. There is selective adsorption.

通过溶胶-凝胶法和溶剂挥发自组装(EISA)成功合成出介孔磷酸锆材料,并将其应用于吸附废水中的铀酰离子。将介孔磷酸锆加到pH=5.5,初始浓度为100mg/L的吸附溶液,并放置在震荡速率180r/min,298K恒温震荡箱中6h,该吸附材料对铀酰离子的吸附量高达298.37mg/g。这是由于介孔磷酸锆较大的比表面积,增加了吸附活性位点,促进材料表面的磷酸官能团与铀酰离子的络合,从而说明该方法制备的介孔磷酸锆能够快速高效分离废水中的铀酰离子,是一种良好的吸附剂。Mesoporous zirconium phosphate materials were successfully synthesized by sol-gel method and solvent evaporation self-assembly (EISA), and applied to adsorb uranyl ions in wastewater. Add mesoporous zirconium phosphate to the adsorption solution with pH=5.5 and initial concentration of 100mg/L, and place it in a 298K constant temperature shaking box at a shaking rate of 180r/min for 6h. The adsorption capacity of this adsorption material for uranyl ions is as high as 298.37mg /g. This is due to the large specific surface area of mesoporous zirconium phosphate, which increases the active sites for adsorption and promotes the complexation of phosphoric acid functional groups on the surface of the material with uranyl ions, thus indicating that the mesoporous zirconium phosphate prepared by this method can quickly and efficiently separate waste The uranyl ion is a good adsorbent.

Claims (9)

1. a kind of order mesoporous zirconium phosphate material, which is characterized in that the material preparation is using template as synthesising mesoporous phosphoric acid The structure directing agent of zirconium so that alcohol solvent slowly volatilizees, and one-step synthesis forms the basic zirconium phosphate with three dimensions;Including following Step:
(1) it is that directed agents are dissolved in anhydrous ethanol solvent by template F127;
(2) with ZroCl2.8H2O and PO (OCH3)3Respectively as zirconium source and phosphorus source, it is added in (1), magnetic agitation 4-10h;
(3) solution of (2) is poured into culture dish, places at least 48h in 333K ± 5K, is then placed at least in 383K ± 5K For 24 hours, presoma xerogel is obtained;
(4) it is placed under 773K and calcines under presoma xerogel, obtain the basic zirconium phosphate MZrP-773K with three dimensions.
2. order mesoporous zirconium phosphate material according to claim 1, which is characterized in that in step (1) in step (2) F127:(P+Zr) molar ratio is 0.01.
3. order mesoporous zirconium phosphate material according to claim 1, which is characterized in that ZroCl in step (2)2.8H2O and PO(OCH3)3Molar ratio be 0.5-1.0.
4. order mesoporous zirconium phosphate material according to claim 1, which is characterized in that in step (3), step (2) it is molten Liquid covers one layer of preservative film when pouring into culture dish, and carries aperture, prevents anhydrous ethanol solvent volatilization too fast.
5. order mesoporous zirconium phosphate material according to claim 1, which is characterized in that the heating speed calcined in step (4) Rate is 1K/min, and 4h is calcined under temperature 773K.
6. a kind of preparation method based on the order mesoporous zirconium phosphate materials of claim 1-5.
7. a kind of application process based on any Mesoporous zirconium phosphate materials of claim 1-5, which is characterized in that the application process Specifically, using Mesoporous zirconium phosphate material as adsorbent, the uranyl ion in waste water is adsorbed;Actual conditions are, in isothermal vibration Under the conditions of, adsorbent Mesoporous zirconium phosphate is added in the solution containing uranyl ion t=298K, rotating speed=180r/min, absorption Time is 0.05-24h;It is desorbed again after absorption.
8. the application process of Mesoporous zirconium phosphate material according to claim 7, which is characterized in that the uranyl ion is molten The initial concentration of liquid is 10-200mg/L, and the initial pH of adsorbent solution is 3-7.
9. a kind of order mesoporous zirconium phosphate material according to claim 7, which is characterized in that desorption process is:It will absorption Mesoporous zirconium phosphate material afterwards, which is added in the nitric acid of a concentration of 3mol/L, shakes 4h, centrifuges, and washes 3 times, 343K drying.
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