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CN106362807A - Visible light driven photocatalysis hydrogen production catalyst as well as preparation method and application thereof - Google Patents

Visible light driven photocatalysis hydrogen production catalyst as well as preparation method and application thereof Download PDF

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CN106362807A
CN106362807A CN201610808987.9A CN201610808987A CN106362807A CN 106362807 A CN106362807 A CN 106362807A CN 201610808987 A CN201610808987 A CN 201610808987A CN 106362807 A CN106362807 A CN 106362807A
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hydrogen production
photocatalytic
visible light
photocatalytic hydrogen
production catalyst
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李书军
彭青坡
陈学年
王若雅
吴丹
梅鸿飞
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Henan Normal University
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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/39Photocatalytic properties
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    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/04Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
    • C01B3/042Decomposition of water
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    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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Abstract

本发明公开了一种可见光驱动的光催化产氢催化剂及其制备方法和应用。本发明的技术方案要点为:以钛酸异丙酯和含钽多酸Ta‑POMs‑1为前驱体,通过溶胶凝胶法制备光催化产氢催化剂Ta‑POM‑1/TiO2;通过优化和选择染料分子的种类和用量、牺牲试剂的种类和用量以及催化剂的用量来优化该催化剂在可见光下催化产氢的反应条件。与母体TiO2和POMs相比,制得的Ta‑POM‑1/TiO2复合光催化材料表现出更好的可见光吸收和更高的光催化产氢活性,因此在光催化领域具有较好的应用前景。

The invention discloses a photocatalytic hydrogen production catalyst driven by visible light, a preparation method and application thereof. The main points of the technical scheme of the present invention are: using isopropyl titanate and tantalum-containing polyacid Ta-POMs-1 as precursors, preparing photocatalytic hydrogen production catalyst Ta-POM-1/ TiO2 by sol-gel method; through optimization And select the type and amount of the dye molecule, the type and amount of the sacrificial reagent and the amount of the catalyst to optimize the reaction conditions for the catalyst to catalyze hydrogen production under visible light. Compared with the parent TiO 2 and POMs, the prepared Ta‑POM‑1/TiO 2 composite photocatalytic material exhibits better visible light absorption and higher photocatalytic hydrogen production activity, so it has a better application in the field of photocatalysis. Application prospects.

Description

一种可见光驱动的光催化产氢催化剂及其制备方法和应用A photocatalytic hydrogen production catalyst driven by visible light and its preparation method and application

技术领域technical field

本发明属于复合光催化材料的合成技术领域,具体涉及一种可见光驱动的光催化产氢催化剂及其制备方法和应用。The invention belongs to the technical field of synthesis of composite photocatalytic materials, and in particular relates to a photocatalytic hydrogen production catalyst driven by visible light and its preparation method and application.

背景技术Background technique

进入21世纪以来,人类在享受科技发展所带来的舒适与便利的同时,所面临的两大生存危机也日益凸显:煤、石油等化石能源的日益枯竭;生存环境逐渐恶化,化石资源的燃烧所释放的CO2、SO2等有害气体又带来了温室效应、酸雨等诸多环境问题。寻找清洁的可再生能源是实现可持续发展、提高人类生活质量的迫切需要。氢气的热效率是普通汽油的三倍而且燃烧产物对环境无污染,是理想的清洁能源。开发经济有效的方法实现快速制氢有着非常重要的经济和社会意义。Since entering the 21st century, while enjoying the comfort and convenience brought by the development of science and technology, human beings are facing two major survival crises: the depletion of fossil energy such as coal and oil; the gradual deterioration of the living environment, and the burning of fossil resources. The released CO 2 , SO 2 and other harmful gases have brought many environmental problems such as greenhouse effect and acid rain. Finding clean and renewable energy is an urgent need to achieve sustainable development and improve the quality of human life. The thermal efficiency of hydrogen is three times that of ordinary gasoline, and the combustion products have no pollution to the environment, so it is an ideal clean energy. It is of great economic and social significance to develop cost-effective methods to achieve rapid hydrogen production.

TiO2由于具有高效、廉价和稳定等优点被人们用于太阳能电池、降解污染物、空气净化和光解水产氢等领域,成为最具潜力的光催化材料之一。然而TiO2具有较宽的带隙,只能吸收紫外光,不能有效利用太阳能。而且,在光催化过程中TiO2产生的光生电子和空穴很容易复合,大大降低了其光催化效率。上述两个问题严重制约了TiO2的进一步发展。Due to its high efficiency, low cost and stability, TiO 2 has been used in the fields of solar cells, pollutant degradation, air purification and hydrogen production by photolysis of water, and has become one of the most potential photocatalytic materials. However, TiO2 has a wide band gap and can only absorb ultraviolet light, so it cannot effectively utilize solar energy. Moreover, the photogenerated electrons and holes generated by TiO2 are easily recombined during the photocatalytic process, which greatly reduces its photocatalytic efficiency. The above two problems seriously restrict the further development of TiO2 .

多金属氧酸盐(POMs)具有可逆的氧化还原性质,也是一类优秀的光催化材料。但是这类化合物往往在水中或有机溶剂中有很大的溶解度,难以回收利用。TiO2/POMs是一类多孔TiO2负载多酸的复合材料(Y. Guo Et.al. J. Mol. Catal. A 2007, 136–148)。这类复合材料与母体TiO2和POMs相比具有具有较大的比表面和多孔性,而且具有较低的带隙能级,能增强对可见光的吸收,是一类优秀的非均相光催化剂。这类复合物在光催化过程中,POMs可以有效地存储和传递光生电子、能有效抑制TiO2中电子-空穴的复合,因此催化效率大大提高。关于TiO2/POMs光催化降解有机污染物人们已经做了很多研究(Y. Yang et.al.J. Mol. Catal. A 2005, 203–207),但其光催化分解水的研究尚未见报道。Polyoxometalates (POMs) have reversible redox properties and are also a class of excellent photocatalytic materials. However, these compounds often have high solubility in water or organic solvents, making them difficult to recycle. TiO 2 /POMs is a class of porous TiO 2 loaded polyacid composites (Y. Guo Et.al. J. Mol. Catal. A 2007, 136–148). Compared with the parent TiO 2 and POMs, this type of composite material has a larger specific surface and porosity, and has a lower band gap energy level, which can enhance the absorption of visible light, and is an excellent class of heterogeneous photocatalysts. . In the photocatalytic process of such composites, POMs can effectively store and transfer photogenerated electrons, and can effectively inhibit the recombination of electrons and holes in TiO 2 , so the catalytic efficiency is greatly improved. Many studies have been done on the photocatalytic degradation of organic pollutants by TiO 2 /POMs (Y. Yang et.al.J. Mol. Catal. A 2005, 203–207), but the research on photocatalytic water splitting has not been reported .

2012年发明人成功获得了一种具有高效光解水活性的含钽多酸催化剂Ta-POM-1,分子式为H4K8Na8[P8W60Ta12(H2O)4(OH)8O236]·nH2O。由于Ta5d轨道和W5d轨道的杂化使得整个分子的LUMO水平提高,该催化剂的产H2能力大大提高(J. Am. Chem. Soc., 2012, 134,19716–19721)。但是这些含钽多酸Ta-POMs和其它多酸化合物一样易溶于水、难以回收再利用,而且溶液状态下只有紫外光活性。因此将具有高效光催化活性的含钽多酸制备成不溶性材料是解决这一问题的有效方法。本专利采用溶胶-凝胶法将该新颖的Ta-POM制备成复合材料,代号为Ta-POM-1/TiO2,来解决其回收再利用和可见光响应的问题,并进一步优化了该复合材料光催化产氢的条件。In 2012, the inventor successfully obtained a tantalum-containing polyacid catalyst Ta-POM-1 with high-efficiency photolytic water-splitting activity, the molecular formula is H 4 K 8 Na 8 [P 8 W 60 Ta 12 (H 2 O) 4 (OH ) 8 O 236 ] nH 2 O. Due to the hybridization of Ta5d orbital and W5d orbital, the LUMO level of the whole molecule is increased, and the H 2 production capacity of the catalyst is greatly improved (J. Am. Chem. Soc., 2012, 134, 19716–19721). However, these tantalum-containing polyacid Ta-POMs, like other polyacid compounds, are easily soluble in water, difficult to recycle and reuse, and only have ultraviolet light activity in solution state. Therefore, preparing tantalum-containing polyacids with high photocatalytic activity into insoluble materials is an effective way to solve this problem. This patent uses the sol-gel method to prepare the novel Ta-POM into a composite material, code-named Ta-POM-1/TiO 2 , to solve the problems of its recycling and visible light response, and further optimize the composite material Conditions for photocatalytic hydrogen production.

发明内容Contents of the invention

本发明解决的技术问题是提供了一种可见光驱动的光催化产氢催化剂及其制备方法和应用。The technical problem solved by the present invention is to provide a photocatalytic hydrogen production catalyst driven by visible light and its preparation method and application.

本发明为解决上述技术问题采用如下技术方案,一种可见光驱动的光催化产氢催化剂,其特征在于该光催化产氢催化剂由二氧化钛TiO2和含钽多酸Ta-POMs-1复合而成,其中含钽多酸Ta-POMs-1的化学式为H4K8Na8[P8W60Ta12(H2O)4(OH)8O236]·nH2O。The present invention adopts the following technical scheme to solve the above technical problems, a photocatalytic hydrogen production catalyst driven by visible light, characterized in that the photocatalytic hydrogen production catalyst is composed of titanium dioxide TiO2 and Ta-POMs-1 containing tantalum polyacid, The chemical formula of Ta-POMs-1 containing tantalum polyacid is H 4 K 8 Na 8 [P 8 W 60 Ta 12 (H 2 O) 4 (OH) 8 O 236 ]·nH 2 O.

本发明所述的可见光驱动的光催化产氢催化剂的制备方法,其特征在于具体步骤为:将10mL钛酸异丙酯溶于30mL异丙醇中得到溶液A;将1g含钽多酸Ta-POMs-1溶于2mL去离子水中得到溶液B;在超声条件下将溶液B滴加到溶液A中,滴加完成后继续超声处理直至形成凝胶,老化12小时后,将凝胶放入高压反应釜中以2℃/min的升温速率升温至150℃保持12小时,冷却至室温后,将样品过滤并用80℃去离子水多次洗涤直至淋洗液的紫外-可见吸收光谱没有多酸的吸收峰,然后将所得的固体样品于150℃干燥活化12小时得到目标产物光催化产氢催化剂Ta-POM-1/TiO2The preparation method of the photocatalytic hydrogen production catalyst driven by visible light of the present invention is characterized in that the specific steps are: dissolving 10mL isopropyl titanate in 30mL isopropanol to obtain solution A; POMs-1 was dissolved in 2mL deionized water to obtain solution B; under ultrasonic conditions, solution B was added dropwise to solution A, and after the addition was completed, ultrasonic treatment was continued until a gel was formed. After aging for 12 hours, the gel was placed in high pressure In the reaction kettle, the temperature was raised to 150°C at a rate of 2°C/min and kept for 12 hours. After cooling to room temperature, the sample was filtered and washed with 80°C deionized water for several times until the ultraviolet-visible absorption spectrum of the eluent was free of acid. absorption peak, and then dry and activate the obtained solid sample at 150° C. for 12 hours to obtain the target product photocatalytic hydrogen production catalyst Ta-POM-1/TiO 2 .

本发明所述的可见光驱动的光催化产氢催化剂在光催化产氢中的应用,其特征在于具体过程为:向石英光催化反应器中加入180mL去离子水和70mL牺牲试剂甲醇,然后加入0.35g光催化产氢催化剂Ta-POM-1/TiO2、0.1g光敏剂罗丹明b和8mg助催化剂氯铂酸,用高纯氮气鼓气30分钟,然后密闭并在黑暗条件下搅拌吸附12小时,再用500W氙灯照射,产生的气体用排水法收集,并用气相色谱检测为H2The application of the photocatalytic hydrogen production catalyst driven by visible light in the present invention in photocatalytic hydrogen production is characterized in that the specific process is: add 180mL deionized water and 70mL sacrificial reagent methanol to the quartz photocatalytic reactor, and then add 0.35 g photocatalytic hydrogen production catalyst Ta-POM-1/TiO 2 , 0.1 g photosensitizer rhodamine b and 8 mg cocatalyst chloroplatinic acid, blow with high-purity nitrogen for 30 minutes, then airtight and adsorb under dark conditions for 12 hours , and then irradiated with a 500W xenon lamp, the gas produced was collected by the drainage method and detected as H 2 by gas chromatography.

本发明所述的可见光驱动的光催化产氢催化剂在光催化产氢中的应用,其特征在于具体过程为:向石英光催化反应器中加入180mL去离子水和25mL牺牲试剂三乙醇胺,然后加入0.35g催化剂Ta-POM-1/TiO2、0.1g光敏剂曙红Y和8mg助催化剂氯铂酸,用高纯氮气鼓气30分钟,然后密闭并在黑暗条件下搅拌吸附12小时,再用500W氙灯照射,产生的气体用排水法收集,并用气相色谱检测为H2The application of the photocatalytic hydrogen production catalyst driven by visible light in the present invention in photocatalytic hydrogen production is characterized in that the specific process is: add 180mL deionized water and 25mL sacrificial reagent triethanolamine to the quartz photocatalytic reactor, and then add 0.35g of catalyst Ta-POM-1/TiO 2 , 0.1g of photosensitizer Eosin Y and 8mg of cocatalyst chloroplatinic acid were blown with high-purity nitrogen for 30 minutes, then airtight and stirred and adsorbed for 12 hours under dark conditions, and then used Irradiated by a 500W xenon lamp, the gas produced was collected by the drainage method and detected as H 2 by gas chromatography.

本发明与母体TiO2和POMs相比,制得的Ta-POM-1/TiO2复合光催化材料表现出更好的可见光吸收和更高的光催化产氢活性,因此在光催化领域具有较好的应用前景。Compared with the parent TiO 2 and POMs, the Ta-POM-1/TiO 2 composite photocatalytic material prepared by the present invention shows better visible light absorption and higher photocatalytic hydrogen production activity, so it has a comparative advantage in the field of photocatalysis Good application prospects.

附图说明Description of drawings

图1是本发明合成的Ta-POM-1/TiO2和Ta-POMs-1及锐钛矿TiO2的固体漫反射光谱图,其在可见光区域有较好的吸收;Fig. 1 is Ta-POM-1/TiO of the present invention synthesis 2 and Ta-POMs-1 and anatase TiO 2 solid diffuse reflectance spectrograms, it has better absorption in the visible region;

图2是本发明合成的Ta-POM-1/TiO2和各原料组分的拉曼光谱;Fig. 2 is the Ta-POM-1/TiO of the present invention synthesis 2 and the Raman spectrum of each raw material component;

图3是本发明合成的Ta-POM-1/TiO2和锐钛矿TiO2的粉末XRD图谱;Fig. 3 is the Ta-POM-1/TiO that the present invention synthesizes 2 and anatase TiO 2 The powder XRD pattern of collection;

图4是本发明合成的Ta-POM-1/TiO2的可见光催化产氢活性效果图,横坐标为时间,纵坐标为产氢量;Fig. 4 is the Ta-POM-1/ TiO synthesized by the present invention The visible light catalytic hydrogen production activity effect figure, abscissa is time, and ordinate is hydrogen production amount;

图5是本发明合成的Ta-POM-1/TiO2的在不同染料(罗丹明b,简写为Rh-b和曙红Y,简写为EY)和牺牲试剂(甲醇和三乙醇胺)存在下的光催化产氢活性。Figure 5 is the synthesis of Ta-POM-1/TiO 2 in the present invention in the presence of different dyes (rhodamine b, abbreviated as Rh-b and eosin Y, abbreviated as EY) and sacrificial reagents (methanol and triethanolamine) Photocatalytic hydrogen production activity.

具体实施方式detailed description

以下通过实施例对本发明的上述内容做进一步详细说明,但不应该将此理解为本发明上述主题的范围仅限于以下的实施例,凡基于本发明上述内容实现的技术均属于本发明的范围。The above-mentioned contents of the present invention are described in further detail below through the embodiments, but this should not be interpreted as the scope of the above-mentioned themes of the present invention being limited to the following embodiments, and all technologies realized based on the above-mentioned contents of the present invention all belong to the scope of the present invention.

实施例Example

Ta-POM-1/TiO2复合光催化材料的制备Preparation of Ta-POM-1/TiO 2 Composite Photocatalytic Material

1、前驱体含钽多酸H4K8Na8[P8W60Ta12(H2O)4(OH)8O236]·nH2O,标记为Ta-POM-1,按照文献合成:J. Am. Chem. Soc., 2012, 134, 19716−19721。1. The precursor contains tantalum polyacid H 4 K 8 Na 8 [P 8 W 60 Ta 12 (H 2 O) 4 (OH) 8 O 236 ]·nH 2 O, marked as Ta-POM-1, synthesized according to the literature : J. Am. Chem. Soc., 2012, 134, 19716−19721.

2、将10mL钛酸异丙酯溶于30mL异丙醇中得到溶液A;将1g含钽多酸Ta-POM-1溶于2mL去离子水中得到溶液B;在超声条件下将溶液B逐滴加入溶液A中,滴加完毕后继续超声处理直至形成凝胶,老化12小时后,将凝胶放入高压反应釜中以2℃/min的升温速度升温至150℃保持12小时,冷却至室温后,将样品过滤并用80℃去离子水多次洗涤直至淋洗液的紫外-可见吸收光谱没有多酸的吸收峰,然后将所得的固体样品于150℃干燥活化12小时得到目标光催化剂Ta-POM-1/TiO22. Dissolve 10mL of isopropyl titanate in 30mL of isopropanol to obtain solution A; dissolve 1g of tantalum-containing polyacid Ta-POM-1 in 2mL of deionized water to obtain solution B; under ultrasonic conditions, dissolve solution B drop by drop Add it into solution A, continue to sonicate until the gel is formed after the dropwise addition, after aging for 12 hours, put the gel in an autoclave and raise the temperature to 150°C at a rate of 2°C/min for 12 hours, then cool to room temperature Finally, the sample was filtered and washed with 80°C deionized water for several times until the eluent had no absorption peak of polyacid in the UV-Vis absorption spectrum, and then the obtained solid sample was dried and activated at 150°C for 12 hours to obtain the target photocatalyst Ta- POM-1/TiO 2 .

如附图1的固体漫反射光测所示,与Ta-POMs-1及锐钛矿TiO2相比,所制备的光催化产氢催化剂对光的吸收明显向长波方向移动,可以提高光催化产氢催化剂对可见光的有效利用。如附图2所示,复合光催化材料Ta-POM-1/TiO2的拉曼光谱中989cm-1处多酸的特征吸收峰表明复合材料中Ta-POM-1的存在。而附图3中复合光催化材料的粉末XRD图谱与母体TiO2相比极为相近,表明Ta-POM-1的出现并未改变TiO2母体的晶格结构,而是均匀分散在框架的孔隙中。氮气吸附测试结果表明,Ta-POM-1/TiO2的Langmuir比表面积为203m2/g,BET比表面积为150m2/g;孔径分布分析表明该复合光催化材料具有典型的介孔性。As shown in the solid diffuse reflectance photometry of accompanying drawing 1, compared with Ta-POMs-1 and anatase TiO 2 , the photocatalytic hydrogen production catalyst prepared has a significant shift in the light absorption to the long-wave direction, which can improve the photocatalytic Efficient utilization of visible light by hydrogen-producing catalysts. As shown in Figure 2, the characteristic absorption peak of polyacid at 989cm -1 in the Raman spectrum of the composite photocatalytic material Ta-POM-1/ TiO2 indicates the existence of Ta-POM-1 in the composite material. The powder XRD spectrum of the composite photocatalytic material in Figure 3 is very similar to that of the matrix TiO2 , indicating that the appearance of Ta-POM-1 did not change the lattice structure of the TiO2 matrix, but was evenly dispersed in the pores of the frame . The nitrogen adsorption test results show that the Langmuir specific surface area of Ta-POM-1/TiO 2 is 203m 2 /g, and the BET specific surface area is 150m 2 /g; the pore size distribution analysis shows that the composite photocatalytic material has typical mesopority.

光催化活性的测试方法Photocatalytic activity test method

向石英光催化反应器中加入一定量的去离子水和牺牲试剂甲醇,然后加入一定量的光催化剂Ta-POM-1/TiO2、光敏剂罗丹明b(简写为Rh-b)和助催化剂氯铂酸(分子式为H2PtCl6),用高纯氮气鼓气30分钟,然后密闭并在黑暗条件下搅拌吸附12小时,再用500W氙灯照射,产生的气体用排水法收集,并用气相色谱检测为H2Add a certain amount of deionized water and sacrificial reagent methanol to the quartz photocatalytic reactor, and then add a certain amount of photocatalyst Ta-POM-1/TiO 2 , photosensitizer Rhodamine b (abbreviated as Rh-b) and cocatalyst Chloroplatinic acid (molecular formula is H 2 PtCl 6 ), gassed with high-purity nitrogen for 30 minutes, then sealed and stirred and adsorbed for 12 hours under dark conditions, and then irradiated with a 500W xenon lamp. The generated gas was collected by drainage and analyzed by gas chromatography. Detected as H 2 .

光催化产氢催化剂Ta-POM-1/TiO2用量对催化效果的影响。Effect of the amount of photocatalytic hydrogen production catalyst Ta-POM-1/ TiO2 on the catalytic performance.

在保持去离子水180mL、牺牲试剂甲醇70mL、光敏剂Rh-b的用量0.1g和助催化剂氯铂酸的用量8.0mg的条件下,当改变一系列光催化产氢催化剂Ta-POM-1/TiO2的用量时发现光催化产氢催化剂Ta-POM-1/TiO2的用量为0.35g时催化效果最佳,1.5小时的产氢量为498μmol。Under the conditions of maintaining 180mL of deionized water, 70mL of sacrificial reagent methanol, 0.1g of photosensitizer Rh-b and 8.0mg of cocatalyst chloroplatinic acid, when changing a series of photocatalytic hydrogen production catalysts Ta-POM-1/ When the amount of TiO 2 is used, it is found that the catalytic effect of the photocatalytic hydrogen production catalyst Ta-POM-1/TiO 2 is 0.35g, and the hydrogen production amount in 1.5 hours is 498μmol.

催化剂用量(g)Catalyst dosage (g) 1.5小时产氢量/μmolHydrogen production in 1.5 hours/μmol 0.200.20 481481 0.350.35 498498 0.500.50 379379

牺牲试剂用量对催化效果的影响。The effect of the amount of sacrificial reagent on the catalytic effect.

在保持去离子水180mL、光催化产氢催化剂Ta-POM-1/TiO2用量0.35g、光敏剂Rh-b的用量0.1g和助催化剂氯铂酸的用量8.0mg的条件下,当改变甲醇的用量时发现当反应液中甲醇含量为28%(甲醇体积为70mL)时催化效果最佳。在甲醇用量小于70mL之前,光催化效率随着甲醇用量的增加而提高,产氢量逐步增加,但是当甲醇用量大于70mL之后催化效率趋于稳定,1.5小时的产氢量不随甲醇用量的增加而明显增加。Under the conditions of keeping 180mL of deionized water, photocatalytic hydrogen production catalyst Ta-POM-1/ TiO Consumption of 0.35g, photosensitizer Rh-b consumption of 0.1g and cocatalyst chloroplatinic acid consumption of 8.0mg, when changing methanol It is found that the catalytic effect is the best when the methanol content in the reaction solution is 28% (methanol volume is 70mL). Before the amount of methanol used was less than 70mL, the photocatalytic efficiency increased with the increase of the amount of methanol, and the amount of hydrogen produced gradually increased. However, when the amount of methanol used was greater than 70mL, the catalytic efficiency tended to be stable, and the amount of hydrogen produced in 1.5 hours did not increase with the amount of methanol. obviously increase.

溶液中甲醇含量(V/V %)Methanol content in solution (V/V %) 1.5小时产氢量/μmolHydrogen production in 1.5 hours/μmol 1212 339339 2020 424424 2828 498498 3636 491491

光敏剂用量对催化效果的影响。The effect of the amount of photosensitizer on the catalytic effect.

在保持去离子水180mL、牺牲试剂甲醇70mL、光催化产氢催化剂Ta-POM-1/TiO2用量0.35g和助催化剂氯铂酸的用量8.0mg的条件下,当改变光敏剂Rh-b用量时发现,Rh-b用量小于0.1g时,随着染料用量的增加,产氢量显著增加。但当Rh-b用量大于0.1g之后,继续增加Rh-b的用量产氢量反而下降。这可能是因为Rh-b用量较少时随着染料浓度的增加,有助于吸收可见光,提高量子效率;但当浓度过大时,Rh-b会阻碍催化剂对光的吸收,使催化效果减弱。因此Rh-b的最佳用量为0.1g。Under the conditions of maintaining 180mL of deionized water, 70mL of sacrificial reagent methanol, 0.35g of photocatalytic hydrogen production catalyst Ta-POM-1/ TiO and 8.0mg of cocatalyst chloroplatinic acid, when changing the amount of photosensitizer Rh-b It was found that when the amount of Rh-b was less than 0.1g, the amount of hydrogen produced increased significantly with the increase of the amount of dye. However, when the amount of Rh-b is greater than 0.1 g, the amount of hydrogen produced decreases when the amount of Rh-b is increased. This may be because when the amount of Rh-b is small, as the concentration of the dye increases, it helps to absorb visible light and improve the quantum efficiency; but when the concentration is too large, Rh-b will hinder the absorption of light by the catalyst and weaken the catalytic effect. . Therefore, the optimal dosage of Rh-b is 0.1g.

Rh-b用量(mmol)Rh-b dosage (mmol) 1.5小时产氢量/μmolHydrogen production in 1.5 hours/μmol 0.10.1 412412 0.20.2 498498 0.30.3 300300

助催化剂用量对催化效果的影响。The effect of co-catalyst dosage on catalytic performance.

加入的氯铂酸在光催化反应的最初阶段被还原为Pt并作为光催化产氢反应的助催化剂。在保持去离子水180mL、光催化产氢催化剂Ta-POM-1/TiO2用量0.35g、牺牲试剂甲醇70mL和光敏剂Rh-b用量0.1g,当改变助催化剂氯铂酸的用量时发现,当氯铂酸的用量为8mg时催化效果最佳;但是当氯铂酸的用量过大时会发生染料的加氢反应,从而使产氢反应速率大大降低。The added chloroplatinic acid was reduced to Pt at the initial stage of the photocatalytic reaction and served as a co-catalyst for the photocatalytic hydrogen production reaction. Keeping deionized water 180mL, photocatalytic hydrogen production catalyst Ta-POM-1/ TiO Consumption 0.35g, sacrificial reagent methanol 70mL and photosensitizer Rh-b consumption 0.1g, when changing the consumption of cocatalyst chloroplatinic acid, find that, When the amount of chloroplatinic acid is 8 mg, the catalytic effect is the best; but when the amount of chloroplatinic acid is too large, the hydrogenation reaction of the dye will occur, so that the hydrogen production reaction rate is greatly reduced.

溶液中氯铂酸含量(mg)Chloroplatinic acid content in the solution (mg) 产氢量/μmolHydrogen production/μmol 44 225225 88 498498 1212 218218

经过上述一系列对照试验,最终确定了为最佳催化条件为:去离子水的用量为180mL、光催化产氢催化剂Ta-POM-1/TiO2用量为0.35g、牺牲试剂甲醇用量为70mL、光敏剂Rh-b用量为0.1g和助催化剂氯铂酸的量为8mg,如附图4所示,在该条件下1.5小时的产氢量达到498μmol,催化效率是商业购买锐钛矿TiO2的4.65倍。After a series of comparative experiments above, the optimal catalytic conditions were finally determined as follows: the amount of deionized water was 180mL, the amount of photocatalytic hydrogen production catalyst Ta-POM-1/ TiO2 was 0.35g, and the amount of sacrificial reagent methanol was 70mL. The amount of photosensitizer Rh-b is 0.1g and the amount of cocatalyst chloroplatinic acid is 8mg, as shown in Figure 4, under this condition, the amount of hydrogen produced in 1.5 hours reaches 498 μmol, and the catalytic efficiency is the same as that of commercially purchased anatase TiO 2 4.65 times.

此外,我们还测试了该光催化产氢催化剂Ta-POM-1/TiO2在牺牲试剂为三乙醇胺和光敏剂为曙红Y的光催化活性。如附图5所示在去离子水、光催化产氢催化剂Ta-POM-1/TiO2和助催化剂氯铂酸用量完全相同的条件下,仅将牺牲试剂甲醇替换为25mL三乙醇胺和将光敏剂Rh-b替换为0.1g曙红Y时,产氢速率较慢但持久性更好,90小时内未见明显下降。In addition, we also tested the photocatalytic activity of the photocatalytic hydrogen production catalyst Ta-POM-1/TiO 2 when the sacrificial reagent was triethanolamine and the photosensitizer was eosin Y. As shown in accompanying drawing 5, under the condition that deionized water, photocatalytic hydrogen production catalyst Ta-POM-1/TiO 2 and cocatalyst chloroplatinic acid consumption are exactly the same, only sacrificial reagent methanol is replaced by 25mL triethanolamine and photosensitizer When the agent Rh-b was replaced by 0.1g eosin Y, the hydrogen production rate was slower but the persistence was better, and there was no obvious decrease within 90 hours.

以上实施例仅为说明本发明的技术思想,不能以此限定本发明的保护范围,凡是按照本发明提出的技术思想,在技术方案基础上所做的任何改动,均落入本发明保护范围之内。The above embodiments are only to illustrate the technical ideas of the present invention, and cannot limit the protection scope of the present invention with this. All technical ideas proposed according to the present invention, any changes made on the basis of technical solutions, all fall within the protection scope of the present invention. Inside.

Claims (4)

1.一种可见光驱动的光催化产氢催化剂,其特征在于该光催化产氢催化剂由二氧化钛TiO2和含钽多酸Ta-POMs-1复合而成,其中含钽多酸Ta-POMs-1的化学式为H4K8Na8[P8W60Ta12(H2O)4(OH)8O236]·nH2O。1. A photocatalytic hydrogen production catalyst driven by visible light, characterized in that the photocatalytic hydrogen production catalyst is composed of titanium dioxide TiO2 and tantalum-containing polyacid Ta-POMs-1, wherein tantalum polyacid Ta-POMs-1 The chemical formula is H 4 K 8 Na 8 [P 8 W 60 Ta 12 (H 2 O) 4 (OH) 8 O 236 ]·nH 2 O. 2.一种权利要求1所述的可见光驱动的光催化产氢催化剂的制备方法,其特征在于具体步骤为:将10mL钛酸异丙酯溶于30mL异丙醇中得到溶液A;将1g含钽多酸Ta-POMs-1溶于2mL去离子水中得到溶液B;在超声条件下将溶液B滴加到溶液A中,滴加完成后继续超声处理直至形成凝胶,老化12小时后,将凝胶放入高压反应釜中以2℃/min的升温速率升温至150℃保持12小时,冷却至室温后,将样品过滤并用80℃去离子水多次洗涤直至淋洗液的紫外-可见吸收光谱没有多酸的吸收峰,然后将所得的固体样品于150℃干燥活化12小时得到目标产物光催化产氢催化剂Ta-POM-1/TiO22. A preparation method of a photocatalytic hydrogen production catalyst driven by visible light according to claim 1, characterized in that the specific steps are: 10mL isopropyl titanate is dissolved in 30mL isopropanol to obtain solution A; 1g containing Tantalum polyacid Ta-POMs-1 was dissolved in 2mL of deionized water to obtain solution B; under ultrasonic conditions, solution B was added dropwise to solution A, and after the addition was completed, ultrasonic treatment was continued until a gel was formed. After aging for 12 hours, the Put the gel in a high-pressure reactor and raise the temperature to 150°C at a rate of 2°C/min and keep it for 12 hours. After cooling to room temperature, the sample is filtered and washed with 80°C deionized water for several times until the ultraviolet-visible absorption of the eluent There is no absorption peak of polyacid in the spectrum, and then the obtained solid sample is dried and activated at 150° C. for 12 hours to obtain the target product photocatalytic hydrogen production catalyst Ta-POM-1/TiO 2 . 3.权利要求1所述的可见光驱动的光催化产氢催化剂在光催化产氢中的应用,其特征在于具体过程为:向石英光催化反应器中加入180mL去离子水和70mL牺牲试剂甲醇,然后加入0.35g光催化产氢催化剂Ta-POM-1/TiO2、0.1g光敏剂罗丹明b和8mg助催化剂氯铂酸,用高纯氮气鼓气30分钟,然后密闭并在黑暗条件下搅拌吸附12小时,再用500W氙灯照射,产生的气体用排水法收集,并用气相色谱检测为H23. The application of the photocatalytic hydrogen production catalyst driven by visible light in claim 1 in photocatalytic hydrogen production is characterized in that the specific process is: add 180mL deionized water and 70mL sacrificial reagent methanol to the quartz photocatalytic reactor, Then add 0.35g of photocatalytic hydrogen production catalyst Ta-POM-1/TiO 2 , 0.1g of photosensitizer rhodamine b and 8mg of cocatalyst chloroplatinic acid, blow it with high-purity nitrogen for 30 minutes, then seal it and stir in the dark Adsorb for 12 hours, and then irradiate with a 500W xenon lamp. The gas produced is collected by drainage method and detected as H 2 by gas chromatography. 4.权利要求1所述的可见光驱动的光催化产氢催化剂在光催化产氢中的应用,其特征在于具体过程为:向石英光催化反应器中加入180mL去离子水和25mL牺牲试剂三乙醇胺,然后加入0.35g光催化产氢催化剂Ta-POM-1/TiO2、0.1g光敏剂曙红Y和8mg助催化剂氯铂酸,用高纯氮气鼓气30分钟,然后密闭并在黑暗条件下搅拌吸附12小时,再用500W氙灯照射,产生的气体用排水法收集,并用气相色谱检测为H24. The application of the photocatalytic hydrogen production catalyst driven by visible light in claim 1 in photocatalytic hydrogen production is characterized in that the specific process is: adding 180mL deionized water and 25mL sacrificial reagent triethanolamine to the quartz photocatalytic reactor , then add 0.35g of photocatalytic hydrogen production catalyst Ta-POM-1/TiO 2 , 0.1g of photosensitizer Eosin Y and 8mg of cocatalyst chloroplatinic acid, blow with high-purity nitrogen for 30 minutes, then airtight and store in the dark Stir and adsorb for 12 hours, and then irradiate with a 500W xenon lamp. The gas generated is collected by drainage method and detected as H 2 by gas chromatography.
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