CN101850255B - Y-Sb-based composite magnetic particle optical catalyst in nuclear shell structures and application - Google Patents
Y-Sb-based composite magnetic particle optical catalyst in nuclear shell structures and application Download PDFInfo
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Abstract
本发明核-壳结构的催化材料,用如下结构式:γ-Fe2O3-Y3-xYbxSbO7(0.5≤x≤1)、γ-Fe2O3-Y3-xGaxSbO7(0.5≤x≤1)、SiO2-Y3-xYbxSbO7(0.5≤x≤1)、SiO2-Y3-xGaxSbO7(0.5≤x≤1)、MnO-Y3-xYbxSbO7(0.5≤x≤1)或MnO-Y3-xGaxSbO7(0.5≤x≤1),γ-Fe2O3、SiO2和MnO的粒径为0.06-2微米,Y3-xYbxSbO7、Y3-xGaxSbO7包裹后粒径为0.07-2.1微米。催化材料为Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)。通过磁场装置和光催化材料构成的反应系统降解废水,磁场强度选取0.3~0.6T,光源为氙灯或高压汞灯;采用三种核-壳结构的催化材料在水溶液中降解废水。整个光照反应在密闭不透光的环境下进行。
The catalytic material with the core-shell structure of the present invention has the following structural formula: γ-Fe 2 O 3 -Y 3-x Yb x SbO 7 (0.5≤x≤1), γ-Fe 2 O 3 -Y 3-x Ga x SbO 7 (0.5≤x≤1), SiO 2 -Y 3-x Yb x SbO 7 (0.5≤x≤1), SiO 2 -Y 3-x Ga x SbO 7 (0.5≤x≤1), MnO- Y 3-x Yb x SbO 7 (0.5≤x≤1) or MnO-Y 3-x Ga x SbO 7 (0.5≤x≤1), the particle size of γ-Fe 2 O 3 , SiO 2 and MnO is 0.06 -2 microns, Y 3-x Yb x SbO 7 , Y 3-x Ga x SbO 7 coated particle size is 0.07-2.1 microns. The catalytic materials are Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1). Wastewater is degraded through a reaction system composed of a magnetic field device and photocatalytic materials. The magnetic field strength is selected from 0.3 to 0.6T, and the light source is a xenon lamp or a high-pressure mercury lamp. Three kinds of catalytic materials with a core-shell structure are used to degrade wastewater in an aqueous solution. The entire light reaction was carried out in a closed and light-tight environment.
Description
技术领域 technical field
本发明涉及一种新型光催化剂、制备及应用,尤其粉末催化材料Y3-xYbxSbO7(0.5≤x≤1)、Y3-xGaxSbO7(0.5≤x≤1)及“磁性颗粒核-光催化剂壳”结构的γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、γ-Fe2O3-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)、SiO2-Y3-xGaxSbO7(0.5≤x≤1)、MnO(反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)、MnO-Y3-xGaxSbO7(0.5≤x≤1),经光催化去除水体中的有机污染物的应用,及光催化分解水制取氢气的应用。The present invention relates to a new type of photocatalyst, its preparation and application, especially powder catalytic materials Y 3-x Yb x SbO 7 (0.5≤x≤1), Y 3-x Ga x SbO 7 (0.5≤x≤1) and " γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), γ-Fe 2 O 3 -Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1), SiO 2 - Y 3-x Ga x SbO 7 (0.5≤x≤1), MnO (antiferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1), MnO-Y 3-x Ga x SbO 7 (0.5≤x≤1), the application of photocatalytic removal of organic pollutants in water, and the application of photocatalytic decomposition of water to produce hydrogen.
背景技术 Background technique
水中有毒难降解性有机物(PTS)的处理一直是水处理领域中的难点、热点课题。PTS有对人体及生态环境风险高等特点,因此,发达国家对这类污染物均有严格的控制标准。由于常规生化处理方法对这类物质的去除效果差(或基本无处理效果),必须采用特殊处理单元过程对其有针对性的去除。因此,水中难降解性有机物的新型处理技术的开发研究成为目前国际环境工程领域的热点和前沿课题。The treatment of toxic and refractory organic substances (PTS) in water has always been a difficult and hot topic in the field of water treatment. PTS has the characteristics of high risk to human body and ecological environment. Therefore, developed countries have strict control standards for such pollutants. Since conventional biochemical treatment methods have poor removal effects (or almost no treatment effect) on such substances, special treatment unit processes must be used to remove them in a targeted manner. Therefore, the development and research of new treatment technology for refractory organic matter in water has become a hot and frontier topic in the field of international environmental engineering.
半导体(典型的如TiO2)光催化法就是世界各国学者公认的处理水中难降解性有机物最有效、最有市场前景的技术,它在降解水体中的难降解性有机污染物方面具有巨大的应用潜力,在难降解性有机物的矿化分解等方面比电催化、湿式催化氧化技术具有明显的优点。但光催化技术在水处理与废水处理上尚未工业化,主要存在如下两个问题:(1)悬浮体系光催化体系光催化效率高,存在催化剂后处理问题,如果将光催化剂固定在玻璃等材料上可以解决光催化剂的分离回收问题,但其光催化效率却明显低于悬浮体系;(2)二氧化钛仅能吸收紫外光,在可见光范围没有响应,对太阳光的利用率低(4%),而太阳光谱中紫外光部分只占不到5%,而波长为400-750nm的可见光则占太阳光谱的43%,如果能将太阳光中的紫外光波段和可见光波段同时充分利用起来,光量子效率将会得到很大提高。因此,在保证较高的光催化效率的前提下解决光催化剂的回收和量子效率问题成了光催化废水处理工业化应用的关键。Semiconductor (typically such as TiO 2 ) photocatalysis is recognized by scholars from all over the world as the most effective and promising technology for the treatment of refractory organic matter in water, and it has great applications in the degradation of refractory organic pollutants in water Compared with electrocatalysis and wet catalytic oxidation technology, it has obvious advantages in mineralization and decomposition of refractory organic matter. However, photocatalytic technology has not been industrialized in water treatment and wastewater treatment, and there are two main problems: (1) The photocatalytic efficiency of the suspension system photocatalytic system is high, and there is a problem of post-treatment of the catalyst. If the photocatalyst is fixed on glass and other materials It can solve the problem of separation and recovery of photocatalyst, but its photocatalytic efficiency is significantly lower than that of the suspension system; (2) titanium dioxide can only absorb ultraviolet light, has no response in the visible light range, and has a low utilization rate of sunlight (4%), while The ultraviolet part of the solar spectrum only accounts for less than 5%, while the visible light with a wavelength of 400-750nm accounts for 43% of the solar spectrum. If the ultraviolet and visible light bands in sunlight can be fully utilized at the same time, the photon quantum efficiency will increase will be greatly improved. Therefore, solving the problems of photocatalyst recovery and quantum efficiency under the premise of ensuring high photocatalytic efficiency has become the key to the industrial application of photocatalytic wastewater treatment.
目前,提高光催化剂的光利用率主要有两个方向。一是二氧化钛可见光化,如N、S、C等非金属元素部分取代二氧化钛中的氧元素,能够降低光催化材料的带隙能,扩展了其光响应范围,在一定程度上提高了光量子效率;二是研究开发高效的可见光催化剂。近年来,研究者们开展了探索新型可见光光催化剂的研究工作,取得了丰硕成果:Bi12GeO20粉末能有效降解甲基橙等有机物;采用Co3O4/BiVO4可以降解苯酚;采用Ta3N5粒子可以降解亚甲基蓝染料;采用Na2Ta2O6可以降解刚果红溶液;采用Ga2BiTaO7可以降解亚甲基蓝染料。付希贤研制了钙钛矿型复合氧化物LaFeO3、LaFe1-xCuxO3等,结果表明LaFeO3、LaFe1-xCuxO3(x=0.02、0.05)具有较小的带隙,可以有效利用可见光对水相中的有机物进行光催化降解。邹志刚等人成功地合成了CaBi2O4等能利用可见光有效地降解水和空气中的甲醛、乙醛、亚甲基蓝和H2S等有害物的新型光催化材料。朱永法、赵进才等利用自制的新型材料(如Bi2WO6等)快速有效地降解了水相中罗丹明B,其效果较传统方法有大幅度的提高。本课题组首次成功制备了In2BiTaO7粉体光催化降解水体中亚甲基蓝染料,135分钟后亚甲基蓝被完全降解,总有机碳(TOC)去除率为100%。因此,扩大光催化材料的光响应范围是提高光催化量子效率的一个有效方法。目前所报道的可见光光催化材料多是粉未状,在悬浮体系中有很好的光催化活性,因此开发新型的粉末状光催化材料去除水体中的有机污染物不但能产生显著的经济效益,而且还能产生巨大的环境效益和社会效益。At present, there are two main directions to improve the light utilization efficiency of photocatalysts. One is the visible light of titanium dioxide, such as N, S, C and other non-metallic elements partially replacing the oxygen elements in titanium dioxide, which can reduce the band gap energy of photocatalytic materials, expand its photoresponse range, and improve the photon quantum efficiency to a certain extent; The second is to research and develop highly efficient visible light catalysts. In recent years, researchers have carried out research work on exploring new visible light photocatalysts, and achieved fruitful results: Bi 12 GeO 20 powder can effectively degrade organic compounds such as methyl orange; Co 3 O 4 /BiVO 4 can degrade phenol; 3 N 5 particles can degrade methylene blue dye; Na 2 Ta 2 O 6 can degrade Congo red solution; Ga 2 BiTaO 7 can degrade methylene blue dye. Fu Xixian developed perovskite-type composite oxides LaFeO 3 , LaFe 1-x Cux O 3 , etc., and the results showed that LaFeO 3 , LaFe 1-x Cux O 3 (x=0.02, 0.05) had smaller band The visible light can be effectively used to photocatalytically degrade the organic matter in the water phase. Zou Zhigang and others successfully synthesized new photocatalytic materials such as CaBi 2 O 4 that can effectively degrade harmful substances such as formaldehyde, acetaldehyde, methylene blue and H 2 S in water and air by using visible light. Zhu Yongfa, Zhao Jincai, etc. used self-made new materials (such as Bi 2 WO 6 , etc.) to quickly and effectively degrade rhodamine B in the aqueous phase, and the effect was greatly improved compared with traditional methods. For the first time, our research group successfully prepared In 2 BiTaO 7 powder for photocatalytic degradation of methylene blue dye in water. After 135 minutes, methylene blue was completely degraded, and the removal rate of total organic carbon (TOC) was 100%. Therefore, expanding the photoresponse range of photocatalytic materials is an effective way to improve the quantum efficiency of photocatalysis. Most of the visible light photocatalytic materials reported so far are in powder form and have good photocatalytic activity in the suspension system. Therefore, the development of new powder photocatalytic materials to remove organic pollutants in water can not only produce significant economic benefits, but also But also can produce huge environmental benefits and social benefits.
发明内容 Contents of the invention
本发明的目的是:提出一种粉末催化材料Y3-xYbxSbO7和Y3-xGaxSbO7(0.5≤x≤1)及制备工艺路线及方法、性能表征及应用。此外,也提出一种“磁性颗粒核-光催化剂壳”结构的γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、γ-Fe2O3(铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、MnO(反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、MnO(反铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)制备工艺、性能表征及应用。The object of the present invention is to propose a powder catalytic material Y 3-x Yb x SbO 7 and Y 3-x Ga x SbO 7 (0.5≤x≤1), its preparation process route and method, performance characterization and application. In addition, a "magnetic particle core-photocatalyst shell" structure of γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell) is also proposed , γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalytic shell), SiO 2 (paramagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalytic shell), MnO (antiferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), MnO (antiferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1)( Photocatalyst shell) preparation process, performance characterization and application.
本发明的技术方案是:核-壳结构的催化材料γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、γ-Fe2O3(铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、MnO(反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、MnO(反铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)。γ-Fe2O3、SiO2和MnO的粒径为0.06-2微米,Y3-xYbxSbO7、Y3-xGaxSbO7包裹后粒径为0.07-2.1微米。The technical solution of the present invention is: catalytic material γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell) with core-shell structure, γ- Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 ( 0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell), MnO (antiferromagnetic particle core) -Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), MnO (antiferromagnetic particle core) -Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell ). The particle size of γ-Fe 2 O 3 , SiO 2 and MnO is 0.06-2 microns, and the particle size of Y 3-x Yb x SbO 7 , Y 3-x Ga x SbO 7 is 0.07-2.1 microns.
核-壳结构的催化材料Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)。Core-shell structured catalytic materials Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1).
制备方法是采用脉冲激光溅射沉积的制备方法:The preparation method is the preparation method of pulsed laser sputtering deposition:
a.靶材制备:以固相烧结的方法制备Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)靶材,靶材直径为10mm,厚度为2mm;a. Target preparation: prepare Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1) targets by solid-state sintering, and the target diameter 10mm, thickness 2mm;
b.选取衬底:选用铁磁性颗粒γ-Fe2O3、顺磁性颗粒SiO2或反铁磁性颗粒MnO作为衬底;b. Select the substrate: use ferromagnetic particles γ-Fe 2 O 3 , paramagnetic particles SiO 2 or antiferromagnetic particles MnO as the substrate;
c.采用脉冲激光溅射沉积,激光主波长为248nm,激光功率密度为2~3J/cm2,以氮气为保护气氛,氮气和氧气(纯度为99.99%)的压力为8~10Pa,沉积室内初始压力为6×10-5Pa~2×10-3Pa,靶材至衬底的距离为3~7厘米,衬底的温度为300~700℃,分别溅射Y3-xYbxSbO7(0.5≤x≤1)靶材和Y3-xGaxSbO7(0.5≤x≤1)靶材至铁磁性颗粒γ-Fe2O3、顺磁性颗粒SiO2或反铁磁性颗粒MnO衬底表面,在γ-Fe2O3、SiO2或MnO衬底上沉积厚度不同的膜,薄膜沉积时间为90~120分钟,将上述六种膜分别于氮气或在氩气中在1340±10℃和1340±10℃温度下处理60±10min,使之晶化而得到所需的磁性复合催化材料γ-Fe2O3-Y3-xYbxSbO7(0.5≤x≤1)、γ-Fe2O3-Y3-xGaxSbO7(0.5≤x≤1)、SiO2-Y3-xYbxSbO7(0.5≤x≤1)、SiO2-Y3-xGaxSbO7(0.5≤x≤1)、MnO-Y3-xYbxSbO7(0.5≤x≤1)或MnO-Y3-xGaxSbO7(0.5≤x≤1)。c. Deposition by pulsed laser sputtering, the main wavelength of the laser is 248nm, the laser power density is 2-3J/cm 2 , nitrogen is used as the protective atmosphere, the pressure of nitrogen and oxygen (purity is 99.99%) is 8-10Pa, the deposition chamber The initial pressure is 6×10 -5 Pa to 2×10 -3 Pa, the distance from the target to the substrate is 3 to 7 cm, and the temperature of the substrate is 300 to 700°C, respectively sputtering Y 3-x Yb x SbO 7 (0.5≤x≤1) targets and Y 3-x Ga x SbO 7 (0.5≤x≤1) targets to ferromagnetic particles γ-Fe 2 O 3 , paramagnetic particles SiO 2 or antiferromagnetic particles MnO On the surface of the substrate, films with different thicknesses are deposited on γ-Fe 2 O 3 , SiO 2 or MnO substrates. The film deposition time is 90 to 120 minutes. Treat at 10°C and 1340±10°C for 60±10min to crystallize it to obtain the desired magnetic composite catalytic material γ-Fe 2 O 3 -Y 3-x Yb x SbO 7 (0.5≤x≤1), γ-Fe 2 O 3 -Y 3-x Ga x SbO 7 (0.5≤x≤1), SiO 2 -Y 3-x Yb x SbO 7 (0.5≤x≤1), SiO 2 -Y 3-x Ga x SbO 7 (0.5≤x≤1), MnO-Y 3-x Yb x SbO 7 (0.5≤x≤1), or MnO-Y 3-x Ga x SbO 7 (0.5≤x≤1).
或采用多靶磁控溅射沉积的方法:Or use the method of multi-target magnetron sputtering deposition:
a.靶材制备:准备纯金属Yb或Ga与Sb和Y金属靶材,靶材直径为5~6厘米;a. Target preparation: prepare pure metal Yb or Ga and Sb and Y metal targets, the target diameter is 5-6 cm;
b.选取衬底:选用铁磁性颗粒γ-Fe2O3、、顺磁性颗粒SiO2或反铁磁性颗粒MnO作为衬底;b. Select the substrate: use ferromagnetic particles γ-Fe 2 O 3 , paramagnetic particles SiO 2 or antiferromagnetic particles MnO as the substrate;
c.采用多靶磁控溅射,溅射功率为60~200W,以氩气为保护气氛,氩气和氧气(纯度为99.99%)的压力为4~32mTorr,氧气的流量比(O2/(O2+Ar))为30%~50%,沉积室内初始压力为3.3×10-6Torr~1×10-5Torr,靶材至衬底的距离为4~15厘米,衬底的温度为0~400℃,薄膜沉积速率为1~2nm/min;c. Using multi-target magnetron sputtering, the sputtering power is 60-200W, using argon as the protective atmosphere, the pressure of argon and oxygen (purity is 99.99%) is 4-32mTorr, the flow ratio of oxygen (O 2 / (O 2 +Ar)) is 30% to 50%, the initial pressure in the deposition chamber is 3.3×10 -6 Torr to 1×10 -5 Torr, the distance from the target to the substrate is 4 to 15 cm, and the temperature of the
在氧气和氩气的混合气体中共溅射纯金属Y、Yb和Sb靶材至铁磁性颗粒γ-Fe2O3、顺磁性颗粒SiO2或反铁磁性颗粒MnO衬底表面,在衬底上沉积形成Y3-xYbxSbO7(0.5≤x≤1)膜层,将上述三种膜层于氮气或氩气中在1340±10℃处理60±10min;使之晶化而得到所需的光催化剂核壳结构γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)或MnO(反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)。Co-sputter pure metal Y, Yb and Sb targets in a mixed gas of oxygen and argon to the surface of ferromagnetic particles γ-Fe 2 O 3 , paramagnetic particles SiO 2 or antiferromagnetic particles MnO substrate, on the substrate Deposit and form Y 3-x Yb x SbO 7 (0.5≤x≤1) film layer, treat the above three film layers in nitrogen or argon at 1340±10°C for 60±10min; make it crystallize to obtain the desired Photocatalyst core-shell structure γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) or MnO (antiferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1).
在氧气和氩气的混合气体中共溅射纯金属Y、Ga和Sb靶材至铁磁性颗粒γ-Fe2O3、顺磁性颗粒SiO2或反铁磁性颗粒MnO衬底表面,在衬底上沉积形成Y3-xGaxSbO7(0.5≤x≤1)膜层,将上述三种膜层于氮气或氩气中在1340±10℃处理60±10min;使之晶化而得到所需的γ-Fe2O3(铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)或MnO(反铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)。Co-sputter pure metal Y, Ga and Sb targets in a mixed gas of oxygen and argon to the surface of ferromagnetic particles γ-Fe 2 O 3 , paramagnetic particles SiO 2 or antiferromagnetic particles MnO substrate, on the substrate Deposit and form a Y 3-x Ga x SbO 7 (0.5≤x≤1) film layer, and treat the above three film layers in nitrogen or argon at 1340±10°C for 60±10min; make it crystallize to obtain the desired γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) or MnO (antiferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1).
2、粉末催化材料Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)的制备方法:其特征是(1)粉末催化材料Y3-xYbxSbO7(0.5≤x≤1)或Y3-xGaxSbO7(0.5≤x≤1)的制备:采用高温固相烧结的方法制备Y3-xYbxSbO7(0.5≤x≤1)或Y3-xGaxSbO7(0.5≤x≤1)光催化粉末材料;以纯度为99.99%的Y2O3、Yb2O3和Sb2O5或Y2O3、Ga2O3和Sb2O5为原材料,将Y、Yb和Sb或Y、Ga和Sb以所述分子式的原子比的Y2O3、Yb2O3和Sb2O5或Y2O3、Ga2O3和Sb2O5充分混合,然后在球磨机中研磨,粉末的粒径达到1.4-1.8微米,在200±40℃烘干4±1小时,压制成片,放入高温烧结炉中烧制。将炉温升至700±20℃,保温8±2小时后随炉冷却,将粉末压片取出粉碎至粒径为1.3-1.6微米,再将这些粉末压制成片,放入高温烧结炉中烧结,最高炉温为730±20℃,保温6±1小时后随炉冷却,将粉末压片取出粉碎至粒径为1.2-1.5微米,再将这些粉末压制成片,放入高温烧结炉中烧结,升温条件如下:2. The preparation method of powder catalytic materials Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1): the characteristics are (1) the powder catalytic material Y Preparation of 3-x Yb x SbO 7 (0.5≤x≤1) or Y 3-x Ga x SbO 7 (0.5≤x≤1): Y 3-x Yb x SbO 7 ( 0.5≤x≤1) or Y 3-x Ga x SbO 7 (0.5≤x≤1) photocatalytic powder material; Y 2 O 3 , Yb 2 O 3 and Sb 2 O 5 or Y 2 with a purity of 99.99% O 3 , Ga 2 O 3 and Sb 2 O 5 are raw materials, Y, Yb and Sb or Y, Ga and Sb are Y 2 O 3 , Yb 2 O 3 and Sb 2 O 5 or Y 2 O 3 , Ga 2 O 3 and Sb 2 O 5 are fully mixed, then ground in a ball mill, the particle size of the powder reaches 1.4-1.8 microns, dried at 200±40°C for 4±1 hours, pressed into tablets, put Firing in a high temperature sintering furnace. Raise the temperature of the furnace to 700±20°C, keep it warm for 8±2 hours, then cool down with the furnace, take out the pressed powder and crush it to a particle size of 1.3-1.6 microns, then press the powder into a tablet, put it into a high-temperature sintering furnace for sintering , the maximum furnace temperature is 730±20°C, keep warm for 6±1 hours and then cool with the furnace, take out the powder tablet and pulverize it to a particle size of 1.2-1.5 microns, then press the powder into a tablet, put it into a high-temperature sintering furnace for sintering , the heating conditions are as follows:
a.由20℃升温至400℃,升温时间为40±10min;b.在400℃保温40±10min;c.由400℃升温至730℃,升温时间为40±10min;d.在730℃保温480-800min;e.由730℃升温至1340±50℃,升温时间为50±10min;f.在1340±50℃保温3800±400min,炉冷。a. From 20°C to 400°C, the heating time is 40±10min; b. At 400°C for 40±10min; c. From 400°C to 730°C, the heating time is 40±10min; d. At 730°C 480-800min; e. From 730°C to 1340±50°C, the heating time is 50±10min; f. At 1340±50°C for 3800±400min, furnace cooling.
粉末压片经最高温度1340±50℃保温3800±400min后随炉冷却,取出粉末压片粉碎至粒径为0.06-0.32微米,最终制备成功纯净的Y3-xYbxSbO7或Y3-xGaxSbO7(0.5≤x≤1)粉末光催化材料;The powder tablet is kept at a maximum temperature of 1340±50°C for 3800±400min, then cooled in the furnace, the powder tablet is taken out and crushed to a particle size of 0.06-0.32 microns, and finally pure Y 3-x Yb x SbO 7 or Y 3- x Ga x SbO 7 (0.5≤x≤1) powder photocatalytic material;
(2)采用溶胶-凝胶法制备粉末光催化材料Y3-xYbxSbO7(0.5≤x≤1)或Y3-xGaxSbO7(0.5≤x≤1):利用改进的Sol-Gel方法,采用有机金属前驱物,制备Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)。前驱体乙酸镱(Yb(CH3CO2)3)或乙酸镓(Ga(CH3CO2)3)与乙酸钇水合物(Y(CH3CO2)3·xH2O)和氯化锑(SbCl5)溶于异丙醇中,且以Y、Yb和Sb或Y、Ga和Sb以所述分子式的原子比,利用上述前驱体按照分段式溶胶-凝胶制备方法,制备混合氧化物,然后在200±30℃烘干3±1小时,压制成片,放入高温烧结炉中烧制,升温条件如下:a.由20℃升温至400℃,升温时间为40±10min;b.在400℃保温40±10min;c.由400℃升温至730℃,升温时间为40±10min;d.在730℃保温480-800min;e.由730℃升温至1050±30℃,升温时间为20±10min;f.在1050±30℃保温2200±400min,炉冷。粉末压片经最高温度1050±30℃保温2200±400min后随炉冷却,取出粉末压片粉碎至粒径为0.04-0.20微米,最终制备成功纯净的Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)粉末光催化材料。(2) Preparation of powder photocatalytic material Y 3-x Yb x SbO 7 (0.5≤x≤1) or Y 3-x Ga x SbO 7 (0.5≤x≤1) by sol-gel method: using the improved Sol - Gel method, using organometallic precursors to prepare Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1). Precursors ytterbium acetate (Yb(CH 3 CO 2 ) 3 ) or gallium acetate (Ga(CH 3 CO 2 ) 3 ) and yttrium acetate hydrate (Y(CH 3 CO 2 ) 3 ·xH 2 O) and antimony chloride (SbCl 5 ) was dissolved in isopropanol, and with Y, Yb and Sb or Y, Ga and Sb in the atomic ratio of the molecular formula, using the above precursors according to the segmented sol-gel preparation method, a mixed oxide Then dry it at 200±30°C for 3±1 hours, press it into tablets, and put it into a high-temperature sintering furnace for firing. The heating conditions are as follows: a. From 20°C to 400°C, the heating time is 40±10min; b. .Insulate at 400°C for 40±10min; c.Heat from 400°C to 730°C, the heating time is 40±10min; d.Insulate at 730°C for 480-800min; 20±10min; f. Keep warm at 1050±30°C for 2200±400min, furnace cool. The powder tablet was kept at the highest temperature of 1050±30°C for 2200±400min, then cooled in the furnace, the powder tablet was taken out and crushed to a particle size of 0.04-0.20 microns, and finally pure Y 3-x Yb x SbO 7 (0.5≤x ≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1) powder photocatalytic materials.
本发明的有益效果是:通过物理方法或溶胶-凝胶方法成功制备了粉末催化材料Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1),同时制备了新型“磁性颗粒核-光催化剂壳”结构的γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、γ-Fe2O3(铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)、MnO(反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、MnO(反铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)。并对其进行了一系列表征,研究了上述新型光催化材料在可见光或紫外光照射下降解被污染水体中有机污染物的效率及降解机理,研究在可见光或紫外光照射下分解水制取氢气的效率和光学活性,通过磁场-光催化反应系统,促进了复合磁性光催化材料在有机物废水中的梯度分布,同时也促进了磁性复合光催化材料的均匀分布,进而促进了光源和有机污染物的充分接触,极大地提高了有机污染物的降解效率。The beneficial effects of the present invention are: powder catalytic materials Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x ≤1), and at the same time, a novel "magnetic particle core-photocatalyst shell" structure of γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalytic shell), SiO 2 (paramagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1), MnO (antiferromagnetic particle core) -Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), MnO (antiferromagnetic particle core) -Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell ). A series of characterizations have been carried out to study the efficiency and degradation mechanism of the above-mentioned new photocatalytic materials in degrading organic pollutants in polluted water under the irradiation of visible light or ultraviolet light, and to study the production of hydrogen by decomposing water under the irradiation of visible light or ultraviolet light. The efficiency and optical activity of the magnetic field-photocatalytic reaction system promotes the gradient distribution of the composite magnetic photocatalytic material in the organic wastewater, and also promotes the uniform distribution of the magnetic composite photocatalytic material, thereby promoting the light source and organic pollutants. The full contact with it greatly improves the degradation efficiency of organic pollutants.
附图说明 Description of drawings
图1A为Y2YbSbO7的XRD图谱,图1B.为Y2GaSbO7的XRD图谱。Figure 1A is the XRD spectrum of Y 2 YbSbO 7 , and Figure 1B is the XRD spectrum of Y 2 GaSbO 7 .
图2为Y2YbSbO7的实测XRD数据与模拟XRD数据的Rietveld软件结构精修图谱(-:XRD实验数据;...:XRD模拟数据;---:XRD实验数据与模拟数据的差值;|:观测到的反射位置)。Figure 2 is the Rietveld software structural refinement map of the measured XRD data and simulated XRD data of Y 2 YbSbO 7 (-: XRD experimental data; ...: XRD simulated data; ---: the difference between XRD experimental data and simulated data ;|: observed reflection position).
图3为Y2GaSbO7的实测XRD数据与模拟XRD数据的Rietveld软件结构精修图谱(-:XRD实验数据;...:XRD模拟数据;---:XRD实验数据与模拟数据的差值;|:观测到的反射位置)。Figure 3 is the Rietveld software structural refinement map of the measured XRD data and simulated XRD data of Y 2 GaSbO 7 (-: XRD experimental data; ...: XRD simulated data; ---: difference between XRD experimental data and simulated data ;|: observed reflection position).
图4为Y2YbSbO7和Y2GaSbO7的漫反射吸收图谱。Fig. 4 is the diffuse reflection absorption spectrum of Y 2 YbSbO 7 and Y 2 GaSbO 7 .
图5为针对Y2YbSbO7和Y2GaSbO7,(αhv)2和hv关系图谱。Fig. 5 is a graph showing the relationship between (αhv) 2 and hv for Y 2 YbSbO 7 and Y 2 GaSbO 7 .
图6为可见光照射下,以Y2YbSbO7和Y2GaSbO7为催化剂降解罗丹明B所获得的吸光度与入射光波长关系图谱。Fig. 6 is a graph showing the relationship between the absorbance and the wavelength of incident light obtained by degrading rhodamine B with Y 2 YbSbO 7 and Y 2 GaSbO 7 as catalysts under visible light irradiation.
图7为在可见光照射下,以Y2YbSbO7和Y2GaSbO7为催化剂降解罗丹明B所获得的罗丹明B浓度和入射光照射时间关系图谱。Fig. 7 is a graph showing the relationship between Rhodamine B concentration and incident light irradiation time obtained by degrading Rhodamine B with Y 2 YbSbO 7 and Y 2 GaSbO 7 as catalysts under visible light irradiation.
图8为可见光照射下以Y2YbSbO7和Y2GaSbO7为催化剂降解罗丹明B所获得的一级动力学曲线。Fig. 8 is a first-order kinetic curve obtained by using Y 2 YbSbO 7 and Y 2 GaSbO 7 as catalysts to degrade rhodamine B under visible light irradiation.
图9为可见光照射下,以Y2YbSbO7和Y2GaSbO7为催化剂降解罗丹明B所获得的CO2产率。Fig. 9 shows the yield of CO 2 obtained by degrading rhodamine B with Y 2 YbSbO 7 and Y 2 GaSbO 7 as catalysts under visible light irradiation.
图10为可见光照射下,以Y2YbSbO7和Y2GaSbO7为催化剂降解罗丹明B时,总有机碳TOC与入射光照射时间关系图谱。Fig. 10 is a diagram showing the relationship between total organic carbon TOC and incident light irradiation time when Y 2 YbSbO 7 and Y 2 GaSbO 7 are used as catalysts to degrade rhodamine B under visible light irradiation.
图11为Y2YbSbO7和Y2GaSbO7的能带结构图。Fig. 11 is a diagram of energy band structures of Y 2 YbSbO 7 and Y 2 GaSbO 7 .
具体实施方式Detailed ways
粉末催化材料Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1);此外,新型“磁性颗粒核-光催化剂壳”结构的γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、γ-Fe2O3(铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)、MnO(反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、MnO(反铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)。Powdered catalytic materials Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1); in addition, the γ -Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 ( Paramagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1), MnO (antiferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell ), MnO (antiferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell).
(1)制备能够在可见光波段或紫外光波段响应的新型光催化剂Y3-xYbxSbO7(0.5≤x≤1)、Y3-xGaxSbO7(0.5≤x≤1);制备能够在可见光波段或紫外光波段响应的新型“磁性颗粒核-光催化剂壳”结构的γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、γ-Fe2O3(铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、SiO2(顺磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)、MnO(反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)、MnO(反铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)。采用紫外-可见分光光度计和紫外-可见漫反射光谱仪对上述制备的新型催化剂在可见光(或紫外光)照射下产生的吸收谱进行了测定,表征了其光吸收性质。测定了上述新型催化剂X射线光电子能谱(XPS),探讨了上述新型催化剂表面的电子层结构特征及在磁场作用下催化剂晶体内电子和空穴的输运机制,分析了磁性颗粒表面负载的催化剂各微区元素组成,并结合理论计算结果分析了上述新型催化剂的能级结构及电子态密度。(1) Preparation of new photocatalysts Y 3-x Yb x SbO 7 (0.5≤x≤1), Y 3-x Ga x SbO 7 (0.5≤x≤1) that can respond in the visible light band or ultraviolet light band; preparation γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) with a novel "magnetic particle core-photocatalyst shell" structure capable of responding in the visible light band or ultraviolet light band (photocatalyst shell), γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalytic shell), SiO 2 (paramagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1), MnO (antiferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell), MnO (antiferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1)( photocatalyst shell). The absorption spectrum of the new catalyst prepared above was measured under visible light (or ultraviolet light) irradiation by using a UV-Vis spectrophotometer and a UV-Vis diffuse reflectance spectrometer, and its light absorption properties were characterized. The X-ray photoelectron spectroscopy (XPS) of the above-mentioned new catalyst was measured, the structure characteristics of the electron layer on the surface of the above-mentioned new catalyst and the transport mechanism of electrons and holes in the catalyst crystal under the action of a magnetic field were discussed, and the catalyst supported on the surface of magnetic particles was analyzed. The elemental composition of each micro-area, and combined with the theoretical calculation results, the energy level structure and electronic density of states of the above-mentioned new catalysts were analyzed.
(2)采用X射线衍射仪(XRD)对上述新型催化剂进行了物相分析;采用透射电镜(TEM)分析了上述新型催化剂的微观结构特征;利用扫描电镜(SEM)对上述新型催化剂进行了组织形貌分析,并结合扫描电镜能谱(SEM-EDS)和X射线光电子能谱(XPS)测定了它们的成分组成,揭示了新型催化剂表面的电子层结构特征。深层次揭示了新型光催化剂的微观结构对光催化降解有机污染物效率的影响规律。(2) X-ray diffractometer (XRD) was used to analyze the phase of the above-mentioned new catalyst; the microstructure characteristics of the above-mentioned new catalyst were analyzed by transmission electron microscope (TEM); Morphological analysis, combined with scanning electron microscopy (SEM-EDS) and X-ray photoelectron spectroscopy (XPS), determined their composition, revealing the electronic layer structure characteristics of the new catalyst surface. It deeply reveals the influence of the microstructure of the new photocatalyst on the efficiency of photocatalytic degradation of organic pollutants.
在可见光(或紫外光)照射下降解水体内染料、阿特拉津或五氯苯酚等难降解有机污染物的过程中,通过液相色谱/质谱(LC/MS)联用仪及离子色谱仪,测试跟踪了降解上述有机污染物过程中的中间产物和最终产物,获得了在新型核-壳磁性复合催化剂颗粒作用下,在可见光(或紫外光)照射下降解水体内多种有机污染物的可能途径,揭示了水体内染料、阿特拉津或五氯苯酚等有机污染物的降解机制。In the process of degrading refractory organic pollutants such as dyes, atrazine or pentachlorophenol in water under the irradiation of visible light (or ultraviolet light), through liquid chromatography/mass spectrometry (LC/MS) and ion chromatography , the test tracked the intermediate products and final products in the process of degrading the above organic pollutants, and obtained the results of degrading various organic pollutants in water under the action of the new core-shell magnetic composite catalyst particles under the irradiation of visible light (or ultraviolet light). Possible pathways, revealing the degradation mechanism of organic pollutants such as dyes, atrazine or pentachlorophenol in water.
采用单波长可见光(或紫外光)照射水体内染料、阿特拉津或五氯苯酚等有机污染物,通过试验研究结果及理论计算成功推导出参与光催化降解反应的光生电荷(光生电子或者光生空穴)数量,进而推导出参与反应的可见光(或紫外光)光子数,结合计算出的入射光总光子数,最终得出在单波长可见光(或紫外光)作用下降解水体中染料、阿特拉津或五氯苯酚等有机污染物的光量子效率。Using single-wavelength visible light (or ultraviolet light) to irradiate organic pollutants such as dyes, atrazine or pentachlorophenol in water, the photogenerated charges (photogenerated electrons or photogenerated electrons or photogenerated electrons) involved in the photocatalytic degradation reaction were successfully deduced through experimental research results and theoretical calculations. hole) number, and then deduce the number of photons of visible light (or ultraviolet light) participating in the reaction, combined with the calculated total photon number of incident light, and finally obtain the degradation of dyes and albino in water under the action of single-wavelength visible light (or ultraviolet light) Photon Quantum Efficiency of Organic Pollutants such as Trazine or Pentachlorophenol.
表1Y2YbSbO7的原子结构参数Table 1 Atomic structure parameters of Y 2 YbSbO 7
表2Y2GaSbO7的原子结构参数Table 2 Atomic structure parameters of Y 2 GaSbO 7
具体实施方式 Detailed ways
1.粉末催化材料Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)的制备工艺路线如下:1. The preparation process route of powder catalytic materials Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1) is as follows:
(1)粉末催化材料Y3-xYbxSbO7(0.5≤x≤1)的制备:采用高温固相烧结的方法制备Y3-xYbxSbO7(0.5≤x≤1)光催化粉末材料。以纯度为99.99%的Y2O3、Yb2O3和Sb2O5为原材料,将Y、Yb、Sb以所述分子式的原子比的Y2O3、Yb2O3和Sb2O5充分混合,然后在球磨机中研磨,粉末的粒径达到1.4-1.8微米,在200±40℃烘干4±1小时,压制成片,放入高温烧结炉中烧制。将炉温升至700±20℃,保温8±2小时后随炉冷却,将粉末压片取出粉碎至粒径为1.3-1.6微米,再将这些粉末压制成片,放入高温烧结炉中烧结,最高炉温为730±20℃,保温6±1小时后随炉冷却,将粉末压片取出粉碎至粒径为1.2-1.5微米,再将这些粉末压制成片,放入高温烧结炉中烧结,升温条件如下:(1) Preparation of powder catalytic material Y 3-x Yb x SbO 7 (0.5≤x≤1): Y 3-x Yb x SbO 7 (0.5≤x≤1) photocatalytic powder was prepared by high-temperature solid-state sintering Material. Using Y 2 O 3 , Yb 2 O 3 and Sb 2 O 5 with a purity of 99.99% as raw materials, Y, Yb, and Sb in the atomic ratio of Y 2 O 3 , Yb 2 O 3 and Sb 2 O 5 Mix well, then grind in a ball mill, the particle size of the powder reaches 1.4-1.8 microns, dry at 200±40°C for 4±1 hours, press into tablets, and put it into a high-temperature sintering furnace for firing. Raise the temperature of the furnace to 700±20°C, keep it warm for 8±2 hours, then cool down with the furnace, take out the pressed powder and crush it to a particle size of 1.3-1.6 microns, then press the powder into a tablet, put it into a high-temperature sintering furnace for sintering , the maximum furnace temperature is 730±20°C, keep warm for 6±1 hours and then cool with the furnace, take out the powder tablet and pulverize it to a particle size of 1.2-1.5 microns, then press the powder into a tablet, put it into a high-temperature sintering furnace for sintering , the heating conditions are as follows:
a.由20℃升温至400℃,升温时间为40±10min;b.在400℃保温40±10min;c.由400℃升温至730℃,升温时间为40±10min;d.在730℃保温480-800min;e.由730℃升温至1340±50℃,升温时间为50±10min;f.在1340±50℃保温3800±400min,炉冷。a. From 20°C to 400°C, the heating time is 40±10min; b. At 400°C for 40±10min; c. From 400°C to 730°C, the heating time is 40±10min; d. At 730°C 480-800min; e. From 730°C to 1340±50°C, the heating time is 50±10min; f. At 1340±50°C for 3800±400min, furnace cooling.
粉末压片经最高温度1340±50℃保温3800±400min后随炉冷却,取出粉末压片粉碎至粒径为0.06-0.32微米,最终制备成功纯净的Y3-xYbxSbO7(0.5≤x≤1)粉末光催化材料。The powder tablet was kept at a maximum temperature of 1340±50°C for 3800±400min, then cooled in the furnace, the powder tablet was taken out and crushed to a particle size of 0.06-0.32 microns, and finally pure Y 3-x Yb x SbO 7 (0.5≤x ≤1) Powder photocatalytic material.
(2)粉末催化材料Y3-xGaxSbO7(0.5≤x≤1)的制备:采用高温固相烧结的方法制备Y3-xGaxSbO7(0.5≤x≤1)光催化粉末材料。以纯度为99.99%的Y2O3、Ga2O3和Sb2O5为原材料,将Y、Ga、Sb以所述分子式的原子比的Y2O3、Ga2O3和Sb2O5充分混合,然后在球磨机中研磨,粉末的粒径达到1.4-1.8微米,在200±40℃烘干4±1小时,压制成片,放入高温烧结炉中烧制。将炉温升至700±20℃,保温8±2小时后随炉冷却,将粉末压片取出粉碎至粒径为1.3-1.6微米,再将这些粉末压制成片,放入高温烧结炉中烧结,最高炉温为730±20℃,保温6±1小时后随炉冷却,将粉末压片取出粉碎至粒径为1.2-1.5微米,再将这些粉末压制成片,放入高温烧结炉中烧结,升温条件如下:(2) Preparation of powder catalytic material Y 3-x Ga x SbO 7 (0.5≤x≤1): Y 3-x Ga x SbO 7 (0.5≤x≤1) photocatalytic powder was prepared by high-temperature solid-state sintering Material. Using Y 2 O 3 , Ga 2 O 3 and Sb 2 O 5 with a purity of 99.99% as raw materials , Y 2 O 3 , Ga 2 O 3 and Sb 2 O 5 in the atomic ratio of Y, Ga and Sb in the stated molecular formula Mix thoroughly, then grind in a ball mill, the particle size of the powder reaches 1.4-1.8 microns, dry at 200±40°C for 4±1 hours, press into tablets, and put them into a high-temperature sintering furnace for firing. Raise the temperature of the furnace to 700±20°C, keep it warm for 8±2 hours, then cool down with the furnace, take out the pressed powder and crush it to a particle size of 1.3-1.6 microns, then press the powder into a tablet, put it into a high-temperature sintering furnace for sintering , the maximum furnace temperature is 730±20°C, keep warm for 6±1 hours and then cool with the furnace, take out the powder tablet and pulverize it to a particle size of 1.2-1.5 microns, then press the powder into a tablet, put it into a high-temperature sintering furnace for sintering , the heating conditions are as follows:
a.由20℃升温至400℃,升温时间为40±10min;b.在400℃保温40±10min;c.由400℃升温至730℃,升温时间为40±10min;d.在730℃保温480-800min;e.由730℃升温至1340±50℃,升温时间为50±10min;f.在1340±50℃保温3900±400min,炉冷。a. From 20°C to 400°C, the heating time is 40±10min; b. At 400°C for 40±10min; c. From 400°C to 730°C, the heating time is 40±10min; d. At 730°C 480-800min; e. From 730°C to 1340±50°C, the heating time is 50±10min; f. At 1340±50°C for 3900±400min, furnace cooling.
粉末压片经最高温度1340±50℃保温3900±400min后随炉冷却,取出粉末压片粉碎至粒径为0.06-0.31微米,最终制备成功纯净的Y3-xGaxSbO7(0.5≤x≤1)粉末光催化材料。The powder tablet was kept at the highest temperature of 1340±50°C for 3900±400min, then cooled in the furnace, the powder tablet was taken out and crushed to a particle size of 0.06-0.31 microns, and finally pure Y 3-x Ga x SbO 7 (0.5≤x ≤1) Powder photocatalytic material.
(3)采用溶胶-凝胶法制备Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1):改变由Garz-Tovar et al采用的Sol-Gel方法,采用有机金属前驱物,制备Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)。购买前驱体乙酸镱(Yb(CH3CO2)3)、乙酸镓(Ga(CH3CO2)3)、乙酸钇水合物(Y(CH3CO2)3·xH2O)、氯化锑(SbCl5)溶于异丙醇中,利用上述前驱体按照分段式溶胶-凝胶制备方法,制备混合氧化物,然后在200±30℃烘干3±1小时,压制成片,放入高温烧结炉中烧制,升温条件如下:。(3) Preparation of Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1) by sol-gel method: change adopted by Garz-Tovar et al The Sol-Gel method uses organometallic precursors to prepare Y 3-x Yb x SbO 7 (0.5≤x≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1). Purchase precursors of ytterbium acetate (Yb(CH 3 CO 2 ) 3 ), gallium acetate (Ga(CH 3 CO 2 ) 3 ), yttrium acetate hydrate (Y(CH 3 CO 2 ) 3 ·xH 2 O), chloride Antimony (SbCl 5 ) was dissolved in isopropanol, and mixed oxides were prepared by using the above precursors according to the segmented sol-gel preparation method, and then dried at 200±30°C for 3±1 hours, pressed into tablets, and placed Into the high-temperature sintering furnace for firing, the heating conditions are as follows:.
a.由20℃升温至400℃,升温时间为40±10min;b.在400℃保温40±10min;c.由400℃升温至730℃,升温时间为40±10min;d.在730℃保温480-800min;e.由730℃升温至1050±30℃,升温时间为20±10min;f.在1050±30℃保温2200±400min,炉冷。粉末压片经最高温度1050±30℃保温2200±400min后随炉冷却,取出粉末压片粉碎至粒径为0.04-0.20微米,最终制备成功纯净的Y3-xYbxSbO7(0.5≤x≤1)和Y3-xGaxSbO7(0.5≤x≤1)粉末光催化材料。a. From 20°C to 400°C, the heating time is 40±10min; b. At 400°C for 40±10min; c. From 400°C to 730°C, the heating time is 40±10min; d. At 730°C 480-800min; e. From 730°C to 1050±30°C, the heating time is 20±10min; f. At 1050±30°C for 2200±400min, furnace cooling. The powder tablet was kept at the highest temperature of 1050±30°C for 2200±400min, then cooled in the furnace, the powder tablet was taken out and crushed to a particle size of 0.04-0.20 microns, and finally pure Y 3-x Yb x SbO 7 (0.5≤x ≤1) and Y 3-x Ga x SbO 7 (0.5≤x≤1) powder photocatalytic materials.
2.“磁性颗粒核-光催化剂壳”结构的磁性复合催化材料的制备工艺路线如下:2. The preparation process of the magnetic composite catalytic material with the structure of "magnetic particle core-photocatalyst shell" is as follows:
(1)γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)和γ-Fe2O3(铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)的制备:(1) γ-Fe 2O 3 (ferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell) and γ-Fe 2 O 3 (ferromagnetic particle core)- Preparation of Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell):
采用脉冲激光溅射沉积的方法:Deposition by pulsed laser sputtering:
a.靶材制备:通过上述固相烧结的方法制备Y3-xYbxSbO7(0.5≤x≤1)靶材和Y3-xGaxSbO7(0.5≤x≤1)靶材,靶材直径为10mm,厚度为2mm;a. Target preparation: prepare Y 3-x Yb x SbO 7 (0.5≤x≤1) targets and Y 3-x Ga x SbO 7 (0.5≤x≤1) targets by the above solid-phase sintering method, The target diameter is 10mm and the thickness is 2mm;
b.选取衬底:选用铁磁性颗粒γ-Fe2O3作为衬底;b. Select the substrate: use ferromagnetic particles γ-Fe 2 O 3 as the substrate;
c.采用脉冲激光溅射沉积仪,激光主波长为248nm,激光功率密度为2~3J/cm2,以氮气为保护气氛,氮气和氧气(纯度为99.99%)的压力为8~10Pa,沉积室内初始压力为6×10-5Pa~2×10-3Pa,靶材至衬底的距离为3~7厘米,衬底的温度为300~700℃,分别溅射Y3-xYbxSbO7(0.5≤x≤1)靶材和Y3-xGaxSbO7(0.5≤x≤1)靶材至γ-Fe2O3衬底表面,在γ-Fe2O3衬底上沉积厚度不同的膜,薄膜沉积时间为90~120分钟,将上述两种膜分别于氮气或在氩气中在1340±10℃和1340±10℃温度下处理60±10min,使之晶化而得到所需的磁性复合催化材料γ-Fe2O3-Y3-xYbxSbO7(0.5≤x≤1)和γ-Fe2O3-Y3-xGaxSbO7(0.5≤x≤1)。c. Using a pulsed laser sputtering deposition instrument, the main wavelength of the laser is 248nm, the laser power density is 2-3J/cm 2 , nitrogen is used as the protective atmosphere, and the pressure of nitrogen and oxygen (purity is 99.99%) is 8-10Pa. The initial pressure in the chamber is 6×10 -5 Pa to 2×10 -3 Pa, the distance from the target to the substrate is 3 to 7 cm, and the temperature of the substrate is 300 to 700°C, respectively sputtering Y 3-x Yb x SbO 7 (0.5≤x≤1) target and Y 3-x Ga x SbO 7 (0.5≤x≤1) target to γ-Fe 2 O 3 substrate surface, on γ-Fe 2 O 3 substrate Deposit films with different thicknesses. The film deposition time is 90-120 minutes. The above two films are respectively treated in nitrogen or argon at 1340±10°C and 1340±10°C for 60±10min to crystallize and form Obtain the required magnetic composite catalytic materials γ-Fe 2 O 3 -Y 3-x Yb x SbO 7 (0.5≤x≤1) and γ-Fe 2 O 3 -Y 3-x Ga x SbO 7 (0.5≤x ≤1).
采用多靶磁控溅射沉积的方法:Deposition method using multi-target magnetron sputtering:
a.靶材制备:准备纯金属Yb、Ga、Sb、Y金属靶材,靶材直径为5~6厘米;a. Target preparation: prepare pure metal Yb, Ga, Sb, Y metal targets with a diameter of 5-6 cm;
b.选取衬底:选用铁磁性颗粒γ-Fe2O3作为衬底;b. Select the substrate: use ferromagnetic particles γ-Fe 2 O 3 as the substrate;
c.采用多靶磁控溅射仪,溅射功率为60~200W,以氩气为保护气氛,氩气和氧气(纯度为99.99%)的压力为4~32mTorr,氧气的流量比(O2/(O2+Ar))为30%~50%,沉积室内初始压力为3.3×10-6Torr~1×10-5Torr,靶材至衬底的距离为4~15厘米,衬底的温度为0~400℃,薄膜沉积速率为1~2nm/min。在氧气和氩气的混合气体中共溅射纯金属Y、Yb和Sb靶材至γ-Fe2O3衬底表面,在衬底上沉积形成Y3-xYbxSbO7(0.5≤x≤1)膜层,将此膜层于氮气或氩气中在1340±10℃处理60±10min;使之晶化而得到所需的γ-Fe2O3(铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳);在氧气和氩气的混合气体中共溅射纯金属Y、Ga和Sb靶材至γ-Fe2O3衬底表面,在衬底上沉积形成Y3-xGaxSbO7(0.5≤x≤1)膜层,将此膜层于氮气或氩气中在1340±10℃处理60±10min;使之晶化而得到所需的γ-Fe2O3(铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)。c. Using a multi-target magnetron sputtering apparatus, the sputtering power is 60-200W, with argon as the protective atmosphere, the pressure of argon and oxygen (purity is 99.99%) is 4-32mTorr, the flow ratio of oxygen (O 2 /(O 2 +Ar)) is 30% to 50%, the initial pressure in the deposition chamber is 3.3×10 -6 Torr to 1×10 -5 Torr, the distance from the target to the substrate is 4 to 15 cm, and the The temperature is 0-400° C., and the film deposition rate is 1-2 nm/min. Co-sputter pure metal Y, Yb and Sb targets onto the surface of the γ-Fe 2 O 3 substrate in a mixed gas of oxygen and argon, and form Y 3-x Yb x SbO 7 (0.5≤x≤ 1) Film layer, treat this film layer in nitrogen or argon at 1340±10°C for 60±10min; crystallize it to obtain the desired γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3- x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell); co-sputter pure metal Y, Ga and Sb targets onto the surface of γ-Fe 2 O 3 substrate in a mixed gas of oxygen and argon, in Deposit and form a Y 3-x Ga x SbO 7 (0.5≤x≤1) film layer on the substrate, treat this film layer in nitrogen or argon at 1340±10°C for 60±10min; crystallize it to obtain the Required γ-Fe 2 O 3 (ferromagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell).
(2)SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)和SiO2(顺磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)的制备:(2) SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell) and SiO 2 (paramagnetic particle core)-Y 3-x Ga x SbO 7 Preparation of (0.5≤x≤1) (photocatalyst shell):
采用脉冲激光溅射沉积的方法:Deposition by pulsed laser sputtering:
a.靶材制备:通过上述固相烧结的方法制备Y3-xYbxSbO7(0.5≤x≤1)靶材和Y3-xGaxSbO7(0.5≤x≤1)靶材,靶材直径为10mm,厚度为2mm;a. Target preparation: prepare Y 3-x Yb x SbO 7 (0.5≤x≤1) targets and Y 3-x Ga x SbO 7 (0.5≤x≤1) targets by the above solid-phase sintering method, The target diameter is 10mm and the thickness is 2mm;
b.选取衬底:选用顺磁性颗粒SiO2作为衬底;b. Select the substrate: select paramagnetic particle SiO 2 as the substrate;
c.采用脉冲激光溅射沉积仪,激光主波长为248nm,激光功率密度为2~3J/cm2,以氮气为保护气氛,氮气和氧气(纯度为99.99%)的压力为8~10Pa,沉积室内初始压力为6×10- -5Pa~2×10-3Pa,靶材至衬底的距离为3~7厘米,衬底的温度为300~700℃,分别溅射Y3-xYbxSbO7(0.5≤x≤1)靶材和Y3-xGaxSbO7(0.5≤x≤1)靶材至SiO2衬底表面,在SiO2衬底上沉积厚度不同的膜,薄膜沉积时间为90~120分钟,将上述两种膜分别于氮气或在氩气中在1340±10℃和1340±10℃温度下处理60±10min,使之晶化而得到所需的磁性复合催化材料SiO2-Y3-xYbxSbO7(0.5≤x≤1)和SiO2-Y3-xGaxSbO7(0.5≤x≤1)。c. Using a pulsed laser sputtering deposition instrument, the main wavelength of the laser is 248nm, the laser power density is 2-3J/cm 2 , nitrogen is used as the protective atmosphere, and the pressure of nitrogen and oxygen (purity is 99.99%) is 8-10Pa. The initial pressure in the chamber is 6×10 - -5 Pa to 2×10 -3 Pa, the distance from the target to the substrate is 3 to 7 cm, and the temperature of the substrate is 300 to 700°C, respectively sputtering Y 3-x Yb x SbO 7 (0.5≤x≤1) target and Y 3-x Ga x SbO 7 (0.5≤x≤1) target to the SiO 2 substrate surface, deposit films with different thicknesses on the SiO 2 substrate, thin film The deposition time is 90 to 120 minutes, and the above two films are respectively treated in nitrogen or argon at 1340±10°C and 1340±10°C for 60±10min to crystallize them to obtain the desired magnetic composite catalyst. Materials SiO 2 -Y 3-x Yb x SbO 7 (0.5≤x≤1) and SiO 2 -Y 3-x Ga x SbO 7 (0.5≤x≤1).
采用多靶磁控溅射沉积的方法:Deposition method using multi-target magnetron sputtering:
a.靶材制备:准备纯金属Yb、Ga、Sb、Y金属靶材,靶材直径为5~6厘米;a. Target preparation: prepare pure metal Yb, Ga, Sb, Y metal targets with a diameter of 5-6 cm;
b.选取衬底:选用顺磁性颗粒SiO2作为衬底;b. Select the substrate: select paramagnetic particle SiO 2 as the substrate;
c.采用多靶磁控溅射仪,溅射功率为60~200W,以氩气为保护气氛,氩气和氧气(纯度为99.99%)的压力为4~32mTorr,氧气的流量比(O2/(O2+Ar))为30%~50%,沉积室内初始压力为3.3×10-6Torr~1×10-5Torr,靶材至衬底的距离为4~15厘米,衬底的温度为0~400℃,薄膜沉积速率为1~2nm/min。在氧气和氩气的混合气体中共溅射纯金属Y、Yb和Sb靶材至SiO2衬底表面,在衬底上沉积形成Y3-xYbxSbO7(0.5≤x≤1)膜层,将此膜层于氮气或氩气中在1340±10℃处理60±10min;使之晶化而得到所需的SiO2(顺磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳);在氧气和氩气的混合气体中共溅射纯金属Y、Ga和Sb靶材至SiO2衬底表面,在衬底上沉积形成Y3-xGaxSbO7(0.5≤x≤1)膜层,将此膜层于氮气或氩气中在1340±10℃处理60±10min;使之晶化而得到所需的SiO2(顺磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)。c. Using a multi-target magnetron sputtering apparatus, the sputtering power is 60-200W, with argon as the protective atmosphere, the pressure of argon and oxygen (purity is 99.99%) is 4-32mTorr, the flow ratio of oxygen (O 2 /(O 2 +Ar)) is 30% to 50%, the initial pressure in the deposition chamber is 3.3×10 -6 Torr to 1×10 -5 Torr, the distance from the target to the substrate is 4 to 15 cm, and the The temperature is 0-400° C., and the film deposition rate is 1-2 nm/min. Co-sputter pure metal Y, Yb and Sb targets onto the surface of SiO 2 substrate in a mixed gas of oxygen and argon, and deposit Y 3-x Yb x SbO 7 (0.5≤x≤1) film on the substrate , treat this film in nitrogen or argon at 1340±10°C for 60±10min; crystallize it to obtain the desired SiO 2 (paramagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤ x≤1) (photocatalyst shell); pure metal Y, Ga and Sb targets are co-sputtered to the surface of SiO 2 substrate in a mixed gas of oxygen and argon, and Y 3-x Ga x SbO is deposited on the substrate 7 (0.5≤x≤1) film layer, treat this film layer in nitrogen or argon at 1340±10°C for 60±10min; crystallize it to obtain the desired SiO 2 (paramagnetic particle core)-Y 3-x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell).
(3)MnO(反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳)和MnO(反铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)的制备:(3) MnO (antiferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤x≤1) (photocatalyst shell) and MnO (antiferromagnetic particle core)-Y 3-x Ga x SbO 7 Preparation of (0.5≤x≤1) (photocatalyst shell):
采用脉冲激光溅射沉积的方法:Deposition by pulsed laser sputtering:
a.靶材制备:通过上述固相烧结的方法制备Y3-xYbxSbO7(0.5≤x≤1)靶材和Y3-xGaxSbO7(0.5≤x≤1)靶材,靶材直径为10mm,厚度为2mm;a. Target preparation: prepare Y 3-x Yb x SbO 7 (0.5≤x≤1) targets and Y 3-x Ga x SbO 7 (0.5≤x≤1) targets by the above solid-phase sintering method, The target diameter is 10mm and the thickness is 2mm;
b.选取衬底:选用反铁磁性颗粒MnO作为衬底;b. Select the substrate: select antiferromagnetic particle MnO as the substrate;
c.采用脉冲激光溅射沉积仪,激光主波长为248nm,激光功率密度为2~3J/cm2,以氮气为保护气氛,氮气和氧气(纯度为99.99%)的压力为8~10Pa,沉积室内初始压力为6×10-5Pa~2×10-3Pa,靶材至衬底的距离为3~7厘米,衬底的温度为300~700℃,分别溅射Y3-xYbxSbO7(0.5≤x≤1)靶材和Y3-xGaxSbO7(0.5≤x≤1)靶材至MnO衬底表面,在MnO颗粒衬底上沉积厚度不同的膜,薄膜沉积时间为90~120分钟,将上述两种膜分别于氮气或在氩气中在1340±10℃和1340±10℃温度下处理60±10min,使之晶化而得到所需的磁性复合催化材料MnO-Y3-xYbxSbO7(0.5≤x≤1)和MnO-Y3-xGaxSbO7(0.5≤x≤1)。c. Using a pulsed laser sputtering deposition instrument, the main wavelength of the laser is 248nm, the laser power density is 2-3J/cm 2 , nitrogen is used as the protective atmosphere, and the pressure of nitrogen and oxygen (purity is 99.99%) is 8-10Pa. The initial pressure in the chamber is 6×10 -5 Pa to 2×10 -3 Pa, the distance from the target to the substrate is 3 to 7 cm, and the temperature of the substrate is 300 to 700°C, respectively sputtering Y 3-x Yb x SbO 7 (0.5≤x≤1) target and Y 3-x Ga x SbO 7 (0.5≤x≤1) target are deposited on the surface of MnO substrate, and films with different thicknesses are deposited on the MnO particle substrate. The film deposition time For 90 to 120 minutes, the above two films were respectively treated in nitrogen or argon at 1340±10°C and 1340±10°C for 60±10min to crystallize them to obtain the required magnetic composite catalytic material MnO -Y 3-x Yb x SbO 7 (0.5≤x≤1) and MnO-Y 3-x Ga x SbO 7 (0.5≤x≤1).
采用多靶磁控溅射沉积的方法:Deposition method using multi-target magnetron sputtering:
a.靶材制备:准备纯金属Yb、Ga、Sb、Y金属靶材,靶材直径为5~6厘米;a. Target preparation: prepare pure metal Yb, Ga, Sb, Y metal targets with a diameter of 5-6 cm;
b.选取衬底:选用反铁磁性颗粒MnO作为衬底;b. Select the substrate: select antiferromagnetic particle MnO as the substrate;
c.采用多靶磁控溅射仪,溅射功率为60~200W,以氩气为保护气氛,氩气和氧气(纯度为99.99%)的压力为4~32mTorr,氧气的流量比(O2/(O2+Ar))为30%~50%,沉积室内初始压力为3.3×10-6Torr~1×10-5Torr,靶材至衬底的距离为4~15厘米,衬底的温度为0~400℃,薄膜沉积速率为1~2nm/min。在氧气和氩气的混合气体中共溅射纯金属Y、Yb和Sb靶材至MnO颗粒衬底表面,在衬底上沉积形成Y3-xYbxSbO7(0.5≤x≤1)膜层,将此膜层于氮气或氩气中在1340±10℃处理60±10min;使之晶化而得到所需的MnO (反铁磁性颗粒核)-Y3-xYbxSbO7(0.5≤x≤1)(光催化剂壳);在氧气和氩气的混合气体中共溅射纯金属Y、Ga和Sb靶材至MnO衬底表面,在衬底上沉积形成Y3-xGaxSbO7(0.5≤x≤1)膜层,将此膜层于氮气或氩气中在1340±10℃处理60±10min;使之晶化而得到所需的MnO(反铁磁性颗粒核)-Y3-xGaxSbO7(0.5≤x≤1)(光催化剂壳)。c. Using a multi-target magnetron sputtering apparatus, the sputtering power is 60-200W, with argon as the protective atmosphere, the pressure of argon and oxygen (purity is 99.99%) is 4-32mTorr, the flow ratio of oxygen (O 2 /(O 2 +Ar)) is 30% to 50%, the initial pressure in the deposition chamber is 3.3×10 -6 Torr to 1×10 -5 Torr, the distance from the target to the substrate is 4 to 15 cm, and the The temperature is 0-400° C., and the film deposition rate is 1-2 nm/min. Co-sputter pure metal Y, Yb and Sb targets to the surface of MnO particle substrate in a mixed gas of oxygen and argon, and deposit Y 3-x Yb x SbO 7 (0.5≤x≤1) film layer on the substrate , treat this film in nitrogen or argon at 1340±10°C for 60±10min; crystallize it to obtain the desired MnO (antiferromagnetic particle core)-Y 3-x Yb x SbO 7 (0.5≤ x≤1) (photocatalyst shell); pure metal Y, Ga and Sb targets are co-sputtered to the surface of MnO substrate in a mixed gas of oxygen and argon, and Y 3-x Ga x SbO 7 is deposited on the substrate (0.5≤x≤1) film layer, treat this film layer in nitrogen or argon at 1340±10°C for 60±10min; crystallize it to obtain the required MnO (antiferromagnetic particle core)-Y 3 -x Ga x SbO 7 (0.5≤x≤1) (photocatalyst shell).
3.磁场-光催化反应系统的建立方法3. Establishment method of magnetic field-photocatalytic reaction system
核-壳结构的催化材料的应用,通过磁场装置和光催化材料构成的反应系统降解废水,磁场装置是强度可调式交变磁场发生器,磁场强度选取0.3~1T(特斯拉),光源为氙灯或高压汞灯;采用γ-Fe2O3(铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2YbSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)作为催化剂,或采用γ-Fe2O3-Y2GaSbO7、SiO2-Y2GaSbO7、MnO-Y2GaSbO7,上述三种磁性复合光催化材料的体积百分比各占三分之一,上述三种磁性复合催化剂颗粒在水溶液中呈梯度分布,并且可使其均匀分布在水溶液内上、中、下三层,采用截止滤光片(λ>420nm),并同时采用充氧曝气。整个光照反应在密闭不透光的环境下进行。磁场强度亦可为0.05~1.5T(特斯拉)。光源为300W氙灯和400W高压汞灯。选择水中典型难降解有机物五氯酚Pentachlorophenol、染料和阿特拉津Atrazine作为目标降解物。The application of catalytic materials with a core-shell structure degrades wastewater through a reaction system composed of a magnetic field device and photocatalytic materials. The magnetic field device is an alternating magnetic field generator with adjustable strength. The magnetic field strength is selected from 0.3 to 1T (Tesla), and the light source is a xenon lamp. or high-pressure mercury lamp; using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 YbSbO 7 (photocatalytic shell), SiO 2 (paramagnetic particle core)-Y 2 YbSbO 7 (photocatalytic shell) and MnO ( antiferromagnetic particle core)-Y 2 YbSbO 7 (photocatalyst shell) as a catalyst, or use γ-Fe 2 O 3 -Y 2 GaSbO 7 , SiO 2 -Y 2 GaSbO 7 , MnO-Y 2 GaSbO 7 , the above three The volume percentages of the three kinds of magnetic composite photocatalytic materials each account for one-third. The above three kinds of magnetic composite catalyst particles are distributed in a gradient in the aqueous solution, and can be evenly distributed in the upper, middle and lower layers of the aqueous solution. Light sheet (λ > 420nm), and oxygen aeration is used at the same time. The entire light reaction was carried out in a closed and light-tight environment. The magnetic field strength can also be 0.05-1.5T (Tesla). The light source is a 300W xenon lamp and a 400W high pressure mercury lamp. Pentachlorophenol, dyes and Atrazine, typical refractory organic compounds in water, were selected as target degradation products.
通过磁场控制复合磁性颗粒在含有有机物的水溶液中呈梯度分布,利用不同磁性(铁磁性、顺磁性和反铁磁性)的磁性颗粒核包覆新型光催化剂,这些磁性复合催化材料在定向磁场作用下可以促进同类磁性颗粒的混合,避免颗粒团聚,使其完全均匀地分散在水溶液中从而使磁性复合催化材料均匀分布在水溶液内上、中、下三层。还可根据需要灵活施加静磁场与交变磁场,可以在很大的长度和成分范围内方便地调整强磁性与弱磁性颗粒的分布,进而使磁性颗粒表面包覆的光催化剂能够与有机污染物及光源充分接触,在可见光(或紫外光)照射下有机污染物能够被高效率地降解。The composite magnetic particles are controlled by the magnetic field to be distributed in a gradient in the aqueous solution containing organic matter, and the magnetic particle cores of different magnetic properties (ferromagnetic, paramagnetic and antiferromagnetic) are used to coat the new photocatalyst. These magnetic composite catalytic materials are under the action of a directional magnetic field It can promote the mixing of similar magnetic particles, avoid particle agglomeration, and make them completely and uniformly dispersed in the aqueous solution so that the magnetic composite catalytic material is evenly distributed in the upper, middle and lower layers of the aqueous solution. The static magnetic field and alternating magnetic field can also be flexibly applied according to the needs, and the distribution of strong magnetic and weak magnetic particles can be easily adjusted in a large range of length and composition, so that the photocatalyst coated on the surface of the magnetic particles can be combined with organic pollutants. And the light source is fully exposed, and the organic pollutants can be degraded efficiently under the irradiation of visible light (or ultraviolet light).
核-壳结构催化材料的应用,还在于通过Y2YbSbO7或Y2GaSbO7粉末为催化剂,或分别负载Pt,NiO和RuO2辅助催化剂,光源为氙灯或高压汞灯,在密闭的由多个阀门控制的玻璃管路内部照明反应器内进行分解水制取氢气。The application of core-shell structure catalytic materials also lies in using Y 2 YbSbO 7 or Y 2 GaSbO 7 powder as a catalyst, or supporting Pt, NiO and RuO 2 as auxiliary catalysts respectively, the light source is a xenon lamp or a high-pressure mercury lamp, in a closed environment composed of multiple A glass pipeline controlled by a valve is used to decompose water to produce hydrogen in the reactor with internal lighting.
4.Y2YbSbO7和Y2GaSbO7的性能表征4. Characterization of Y 2 YbSbO 7 and Y 2 GaSbO 7
通过XRD、XPS结果得知Y2YbSbO7和Y2GaSbO7皆为单相,且实验原始材料高度纯净,无任何杂质相。The results of XRD and XPS show that both Y 2 YbSbO 7 and Y 2 GaSbO 7 are single-phase, and the experimental raw materials are highly pure without any impurity phase.
通过X射线荧光光谱仪测定Y2YbSbO7的平均原子摩尔百分比为Y∶Yb∶Sb∶O=2.00∶0.98∶1.01∶6.97。用Rietveld软件对Y2YbSbO7的XRD结果进行结构精修,结构精修因子RP值为RP=10.09%。Y2YbSbO7的空间群为Fd-3m,结构为立方晶系,烧绿石结构,晶胞参数a为10.49977(8)Y2YbSbO7各衍射峰的(222)、(400)、(440)、(622)、(444)、(800)、(662)、(840)、(844)等晶面指数被标定。Y2YbSbO7中各个原子的空间原子位置参数被确定(见表1)。采用紫外可见漫反射光谱仪对Y2YbSbO7在光的照射下产生的特征吸收边进行测定,获得Y2YbSbO7的带隙宽度为2.521eV,获得Y2YbSbO7的能带结构,导带由Y的4d轨道、Yb的4f轨道和Sb的5p轨道构成,价带由O的2p轨道构成。The average atomic mole percentage of Y 2 YbSbO 7 measured by X-ray fluorescence spectrometer was Y:Yb:Sb:O=2.00:0.98:1.01:6.97. The XRD results of Y 2 YbSbO 7 were refined by Rietveld software, and the structure refinement factor RP value was R P =10.09%. The space group of Y 2 YbSbO 7 is Fd-3m, the structure is cubic crystal system, pyrochlore structure, and the unit cell parameter a is 10.49977(8) The (222), (400), (440), (622), (444), (800), (662), (840), (844) and other crystal plane indices of each diffraction peak of Y 2 YbSbO 7 were calibrated. The spatial atomic position parameters of each atom in Y 2 YbSbO 7 were determined (see Table 1). The characteristic absorption edge of Y 2 YbSbO 7 under the irradiation of light was measured by ultraviolet-visible diffuse reflectance spectrometer, and the band gap width of Y 2 YbSbO 7 was 2.521eV, and the energy band structure of Y 2 YbSbO 7 was obtained. The conduction band was The 4d orbital of Y, the 4f orbital of Yb, and the 5p orbital of Sb are composed, and the valence band is composed of the 2p orbital of O.
通过X射线荧光光谱仪测定Y2GaSbO7的平均原子摩尔百分比为Y∶Ga∶Sb∶O=2.00∶0.97∶1.02∶6.99。用Rietveld软件对Y2GaSbO7的XRD结果进行结构精修,结构精修因子RP值为RP=12.36%。Y2GaSbO7的空间群为Fd-3m,结构为立方晶系,烧绿石结构,晶胞参数a为10.17981(1)Y2GaSbO7各衍射峰的(222)、(400)、(440)、(622)、(444)、(800)、(662)、(840)、(844)等晶面指数被标定。Y2GaSbO7中各个原子的空间原子位置参数被确定(见表2)。采用紫外可见漫反射光谱仪对Y2GaSbO7在光的照射下产生的特征吸收边进行测定,获得Y2GaSbO7的带隙宽度为3.322eV,获得Y2GaSbO7的能带结构,导带由Y的4d轨道、Ga的4p轨道和Sb的5p轨道构成,价带由O的2p轨道构成。The average atomic mole percentage of Y 2 GaSbO 7 measured by X-ray fluorescence spectrometer is Y:Ga:Sb:O=2.00:0.97:1.02:6.99. The XRD results of Y 2 GaSbO 7 were refined by Rietveld software, and the structure refinement factor R P value was R P =12.36%. The space group of Y 2 GaSbO 7 is Fd-3m, the structure is cubic system, pyrochlore structure, and the unit cell parameter a is 10.17981(1) The (222), (400), (440), (622), (444), (800), (662), (840), (844) and other crystal plane indices of each diffraction peak of Y 2 GaSbO 7 are calibrated. The spatial atomic position parameters of each atom in Y 2 GaSbO 7 were determined (see Table 2). The characteristic absorption edge of Y 2 GaSbO 7 under the irradiation of light was measured by ultraviolet-visible diffuse reflectance spectrometer, and the band gap width of Y 2 GaSbO 7 was 3.322eV, and the energy band structure of Y 2 GaSbO 7 was obtained. The conduction band was The 4d orbital of Y, the 4p orbital of Ga, and the 5p orbital of Sb are formed, and the valence band is formed of the 2p orbital of O.
应用实例Applications
1.采用Y2GaSbO7粉末降解废水中的阿特拉津1. Degradation of Atrazine in Wastewater Using Y 2 GaSbO 7 Powder
将Y2GaSbO7粉末0.8g,放入300mL阿特拉津水溶液中形成悬浮体系,阿特拉津水溶液的初始浓度为0.1mmol L-1,初始pH值为7。选取300W的氙灯照射阿特拉津溶液,配上截止滤光片(λ>420nm)。实验过程中,用磁力搅拌器和充氧曝气的方式维持催化剂粉末呈悬浮状态。整个光照反应在密闭不透光的环境下进行。经400分钟,阿特拉津的去除率为92.2%,光量子效率为0.31%,总有机碳TOC的去除率(矿化率)达88.3%。Put 0.8 g of Y 2 GaSbO 7 powder into 300 mL of atrazine aqueous solution to form a suspension system. The initial concentration of the atrazine aqueous solution is 0.1 mmol L -1 and the initial pH value is 7. Select a 300W xenon lamp to irradiate the atrazine solution with a cut-off filter (λ>420nm). During the experiment, the catalyst powder was maintained in a suspended state by means of a magnetic stirrer and oxygen aeration. The entire light reaction was carried out in a closed and light-tight environment. After 400 minutes, the removal rate of atrazine was 92.2%, the photon quantum efficiency was 0.31%, and the removal rate (mineralization rate) of total organic carbon (TOC) reached 88.3%.
2.采用Y2YbSbO7粉末降解废水中的阿特拉津2. Degradation of Atrazine in Wastewater Using Y 2 YbSbO 7 Powder
将Y2YbSbO7粉末0.8g,放入300mL阿特拉津水溶液中形成悬浮体系,阿特拉津水溶液的初始浓度为0.1mmol L-1,初始pH值为7。选取300W的氙灯照射阿特拉津溶液,配上截止滤光片(λ>420nm)。实验过程中,用磁力搅拌器和充氧曝气的方式维持催化剂粉末呈悬浮状态。整个光照反应在密闭不透光的环境下进行。经400分钟,阿特拉津的去除率为89.3%,光量子效率为0.29%,总有机碳TOC的去除率(矿化率)达86.2%。Put 0.8 g of Y 2 YbSbO 7 powder into 300 mL of atrazine aqueous solution to form a suspension system. The initial concentration of the atrazine aqueous solution is 0.1 mmol L -1 and the initial pH value is 7. Select a 300W xenon lamp to irradiate the atrazine solution with a cut-off filter (λ>420nm). During the experiment, the catalyst powder was maintained in a suspended state by means of a magnetic stirrer and oxygen aeration. The entire light reaction was carried out in a closed and light-tight environment. After 400 minutes, the removal rate of atrazine was 89.3%, the photon quantum efficiency was 0.29%, and the removal rate (mineralization rate) of total organic carbon (TOC) was 86.2%.
3.采用Y2GaSbO7粉末降解废水中的五氯酚3. Using Y 2 GaSbO 7 powder to degrade pentachlorophenol in wastewater
将Y2GaSbO7粉末0.8g,放入300mL五氯酚水溶液中形成悬浮体系,五氯酚水溶液的初始浓度为0.1mmol L-1,初始pH值为7。选取300W的氙灯照射五氯酚溶液,配上截止滤光片(λ>420nm)。实验过程中,用磁力搅拌器和充氧曝气的方式维持催化剂粉末呈悬浮状态。整个光照反应在密闭不透光的环境下进行。经400分钟,五氯酚的去除率为93.4%,光量子效率为0.33%,总有机碳TOC的去除率(矿化率)达89.1%。Put 0.8g of Y 2 GaSbO 7 powder into 300mL pentachlorophenol aqueous solution to form a suspension system. The initial concentration of pentachlorophenol aqueous solution is 0.1mmol L -1 and the initial pH value is 7. Choose a 300W xenon lamp to irradiate the pentachlorophenol solution, and add a cut-off filter (λ>420nm). During the experiment, the catalyst powder was maintained in a suspended state by means of a magnetic stirrer and oxygen aeration. The entire light reaction was carried out in a closed and light-tight environment. After 400 minutes, the removal rate of pentachlorophenol was 93.4%, the light quantum efficiency was 0.33%, and the removal rate (mineralization rate) of total organic carbon (TOC) reached 89.1%.
4.采用Y2YbSbO7粉末降解废水中的五氯酚4. Using Y 2 YbSbO 7 powder to degrade pentachlorophenol in wastewater
将Y2YbSbO7粉末0.8g,放入300mL五氯酚水溶液中形成悬浮体系,五氯酚水溶液的初始浓度为0.1mmol L-1,初始pH值为7。选取300W的氙灯照射五氯酚溶液,配上截止滤光片(λ>420nm)。实验过程中,用磁力搅拌器和充氧曝气的方式维持催化剂粉末呈悬浮状态。整个光照反应在密闭不透光的环境下进行。经400分钟,五氯酚的去除率为91.2%,光量子效率为0.30%,总有机碳TOC的去除率(矿化率)达88.6%。Put 0.8g of Y 2 YbSbO 7 powder into 300mL pentachlorophenol aqueous solution to form a suspension system. The initial concentration of pentachlorophenol aqueous solution is 0.1mmol L -1 and the initial pH value is 7. Choose a 300W xenon lamp to irradiate the pentachlorophenol solution, and add a cut-off filter (λ>420nm). During the experiment, the catalyst powder was maintained in a suspended state by means of a magnetic stirrer and oxygen aeration. The entire light reaction was carried out in a closed and light-tight environment. After 400 minutes, the removal rate of pentachlorophenol was 91.2%, the light quantum efficiency was 0.30%, and the removal rate (mineralization rate) of total organic carbon TOC reached 88.6%.
5.采用γ-Fe2O3(铁磁性颗粒核)-Y2GaSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2GaSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2GaSbO7(光催化剂壳)降解废水中的阿特拉津利用自制的磁场-光催化反应系统,通过磁场强度可调式交变磁场发生器,磁场强度选取0.3~0.6T(特斯拉)。光源为300W氙灯。采用γ-Fe2O3(铁磁性颗粒核)-Y2GaSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2GaSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2GaSbO7(光催化剂壳)作为催化剂,上述三种磁性复合光催化材料的体积百分比各占三分之一,选择水中典型难降解的阿特拉津作为目标降解物。当磁场强度为0.3~0.6特斯拉时,上述三种磁性复合催化剂颗粒在含有阿特拉津的水溶液中呈梯度分布,并且可使其均匀分布在水溶液内上、中、下三层。此时选择900mL阿特拉津水溶液,同时所有磁性颗粒表面涂覆的Y2GaSbO7重量接近2.4g,阿特拉津水溶液的初始浓度为0.1mmol L-1,初始pH值为7。选取300W的氙灯照射阿特拉津溶液,配上截止滤光片(λ>420nm)。实验过程中,同样采用充氧曝气。整个光照反应在密闭不透光的环境下进行。最后灵活施加静磁场与交变磁场,可以使磁性颗粒表面包覆的光催化剂能够与有机污染物及光源充分接触,在可见光照射400分钟后,阿特拉津的去除率达到96.8%,光量子效率为0.33%,总有机碳TOC的去除率(矿化率)达93.2%。5. Using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 GaSbO 7 (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 2 GaSbO 7 (photocatalyst shell) and MnO (antiferromagnetic Particle core)-Y 2 GaSbO 7 (photocatalyst shell) degrades atrazine in wastewater using a self-made magnetic field-photocatalytic reaction system, through an alternating magnetic field generator with adjustable magnetic field strength, and the magnetic field strength is selected from 0.3 to 0.6T ( Tesla). The light source is a 300W xenon lamp. Using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 GaSbO 7 (photocatalytic shell), SiO 2 (paramagnetic particle core)-Y 2 GaSbO 7 (photocatalytic shell) and MnO (antiferromagnetic particle core) )-Y 2 GaSbO 7 (photocatalyst shell) was used as the catalyst, and the volume percentage of the above three magnetic composite photocatalytic materials each accounted for one-third, and atrazine, which is typically difficult to degrade in water, was selected as the target degradation product. When the magnetic field strength is 0.3-0.6 tesla, the above three kinds of magnetic composite catalyst particles are distributed in a gradient in the aqueous solution containing atrazine, and can be uniformly distributed in the upper, middle and lower layers of the aqueous solution. At this time, 900 mL of atrazine aqueous solution was selected, and the weight of Y 2 GaSbO 7 coated on the surface of all magnetic particles was close to 2.4 g. The initial concentration of atrazine aqueous solution was 0.1 mmol L -1 , and the initial pH value was 7. Select a 300W xenon lamp to irradiate the atrazine solution with a cut-off filter (λ>420nm). During the experiment, oxygenation and aeration were also used. The entire light reaction was carried out in a closed and light-tight environment. Finally, the flexible application of static magnetic field and alternating magnetic field can make the photocatalyst coated on the surface of magnetic particles fully contact with organic pollutants and light sources. After 400 minutes of visible light irradiation, the removal rate of atrazine reaches 96.8%, and the photon quantum efficiency The removal rate (mineralization rate) of total organic carbon TOC is 93.2%.
6.采用γ-Fe2O3(铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2YbSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)降解废水中的阿特拉津6. Using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 YbSbO 7 (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 2 YbSbO 7 (photocatalyst shell) and MnO (antiferromagnetic Particle core)-Y 2 YbSbO 7 (photocatalyst shell) for degradation of atrazine in wastewater
利用自制的磁场-光催化反应系统,通过磁场强度可调式交变磁场发生器,磁场强度选取0.3~0.6T(特斯拉)。光源为300W氙灯。采用γ-Fe2O3(铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2YbSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)作为催化剂,上述三种磁性复合光催化材料的体积百分比各占三分之一,选择水中典型难降解的阿特拉津作为目标降解物。当磁场强度为0.3~0.6特斯拉时,上述三种磁性复合催化剂颗粒在含有阿特拉津的水溶液中呈梯度分布,并且可使其均匀分布在水溶液内上、中、下三层。此时选择900mL阿特拉津水溶液,同时所有磁性颗粒表面涂覆的Y2YbSbO7重量接近2.4g,阿特拉津水溶液的初始浓度为0.1mmol L-1,初始pH值为7。选取300W的氙灯照射阿特拉津溶液,配上截止滤光片(λ>420nm)。实验过程中,同样采用充氧曝气。整个光照反应在密闭不透光的环境下进行。最后灵活施加静磁场与交变磁场,可以使磁性颗粒表面包覆的光催化剂能够与有机污染物及光源充分接触,在可见光照射400分钟后,阿特拉津的去除率达到93.5%,光量子效率为0.31%,总有机碳TOC的去除率(矿化率)达90.4%。A self-made magnetic field-photocatalytic reaction system is used, and an alternating magnetic field generator with adjustable magnetic field strength is used, and the magnetic field strength is selected from 0.3 to 0.6T (Tesla). The light source is a 300W xenon lamp. Using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 YbSbO 7 (photocatalytic shell), SiO 2 (paramagnetic particle core)-Y 2 YbSbO 7 (photocatalytic shell) and MnO (antiferromagnetic particle core) )-Y 2 YbSbO 7 (photocatalyst shell) was used as the catalyst, and the volume percentage of the above three magnetic composite photocatalytic materials each accounted for one-third, and atrazine, which is typically difficult to degrade in water, was selected as the target degradation product. When the magnetic field strength is 0.3-0.6 tesla, the above three kinds of magnetic composite catalyst particles are distributed in a gradient in the aqueous solution containing atrazine, and can be uniformly distributed in the upper, middle and lower layers of the aqueous solution. At this time, 900 mL of atrazine aqueous solution was selected, and the weight of Y 2 YbSbO 7 coated on the surface of all magnetic particles was close to 2.4 g. The initial concentration of atrazine aqueous solution was 0.1 mmol L -1 , and the initial pH value was 7. Select a 300W xenon lamp to irradiate the atrazine solution with a cut-off filter (λ>420nm). During the experiment, oxygenation and aeration were also used. The entire light reaction was carried out in a closed and light-tight environment. Finally, the flexible application of static magnetic field and alternating magnetic field can make the photocatalyst coated on the surface of magnetic particles fully contact with organic pollutants and light sources. After 400 minutes of visible light irradiation, the removal rate of atrazine reaches 93.5%, and the photon quantum efficiency is 0.31%, and the removal rate (mineralization rate) of total organic carbon TOC reaches 90.4%.
7.采用γ-Fe2O3(铁磁性颗粒核)-Y2GaSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2GaSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2GaSbO7(光催化剂壳)降解废水中的五氯酚7. Using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 GaSbO 7 (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 2 GaSbO 7 (photocatalyst shell) and MnO (antiferromagnetic Particle core)-Y 2 GaSbO 7 (photocatalyst shell) for degradation of pentachlorophenol in wastewater
利用自制的磁场-光催化反应系统,通过磁场强度可调式交变磁场发生器,磁场强度选取0.3~0.6T(特斯拉)。光源为300W氙灯。采用γ-Fe2O3(铁磁性颗粒核)-Y2GaSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2GaSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2GaSbO7(光催化剂壳)作为催化剂,上述三种磁性复合光催化材料的体积百分比各占三分之一,选择水中典型难降解的五氯酚作为目标降解物。当磁场强度为0.3~0.6特斯拉时,上述三种磁性复合催化剂颗粒在含有五氯酚的水溶液中呈梯度分布,并且可使其均匀分布在水溶液内上、中、下三层。此时选择900mL五氯酚水溶液,同时所有磁性颗粒表面涂覆的Y2GaSbO7重量接近2.4g,五氯酚水溶液的初始浓度为0.1mmol L-1,初始pH值为7。选取300W的氙灯照射五氯酚溶液,配上截止滤光片(λ>420nm)。实验过程中,同样采用充氧曝气。整个光照反应在密闭不透光的环境下进行。最后灵活施加静磁场与交变磁场,可以使磁性颗粒表面包覆的光催化剂能够与有机污染物及光源充分接触,在可见光照射400分钟后,五氯酚的去除率达到96.7%,光量子效率为0.35%,总有机碳TOC的去除率(矿化率)达93.4%。A self-made magnetic field-photocatalytic reaction system is used, and an alternating magnetic field generator with adjustable magnetic field strength is used, and the magnetic field strength is selected from 0.3 to 0.6T (Tesla). The light source is a 300W xenon lamp. Using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 GaSbO 7 (photocatalytic shell), SiO 2 (paramagnetic particle core)-Y 2 GaSbO 7 (photocatalytic shell) and MnO (antiferromagnetic particle core) )-Y 2 GaSbO 7 (photocatalyst shell) was used as the catalyst, and the above three magnetic composite photocatalytic materials each accounted for one-third of the volume percentage, and the typical refractory pentachlorophenol in water was selected as the target degradation product. When the magnetic field strength is 0.3-0.6 tesla, the above three kinds of magnetic composite catalyst particles are distributed in a gradient in the aqueous solution containing pentachlorophenol, and can be uniformly distributed in the upper, middle and lower layers of the aqueous solution. At this time, 900mL pentachlorophenol aqueous solution is selected, and the weight of Y 2 GaSbO 7 coated on the surface of all magnetic particles is close to 2.4g. The initial concentration of pentachlorophenol aqueous solution is 0.1mmol L -1 , and the initial pH value is 7. Choose a 300W xenon lamp to irradiate the pentachlorophenol solution, and add a cut-off filter (λ>420nm). During the experiment, oxygenation and aeration were also used. The entire light reaction was carried out in a closed and light-tight environment. Finally, the static magnetic field and alternating magnetic field can be applied flexibly, so that the photocatalyst coated on the surface of the magnetic particles can fully contact with organic pollutants and light sources. After 400 minutes of visible light irradiation, the removal rate of pentachlorophenol reaches 96.7%, and the photon quantum efficiency is 0.35%, the removal rate (mineralization rate) of total organic carbon TOC reaches 93.4%.
8.采用γ-Fe2O3(铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2YbSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)降解废水中的五氯酚8. Using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 YbSbO 7 (photocatalyst shell), SiO 2 (paramagnetic particle core)-Y 2 YbSbO 7 (photocatalyst shell) and MnO (antiferromagnetic Particle core)-Y 2 YbSbO 7 (photocatalyst shell) for degradation of pentachlorophenol in wastewater
利用自制的磁场-光催化反应系统,通过磁场强度可调式交变磁场发生器,磁场强度选取0.3~0.6T(特斯拉)。光源为300W氙灯。采用γ-Fe2O3(铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)、SiO2(顺磁性颗粒核)-Y2YbSbO7(光催化剂壳)和MnO(反铁磁性颗粒核)-Y2YbSbO7(光催化剂壳)作为催化剂,上述三种磁性复合光催化材料的体积百分比各占三分之一,选择水中典型难降解的五氯酚作为目标降解物。当磁场强度为0.3~0.6特斯拉时,上述三种磁性复合催化剂颗粒在含有五氯酚的水溶液中呈梯度分布,并且可使其均匀分布在水溶液内上、中、下三层。此时选择900mL五氯酚水溶液,同时所有磁性颗粒表面涂覆的Y2YbSbO7重量接近2.4g,五氯酚水溶液的初始浓度为0.1mmol L-1,初始pH值为7。选取300W的氙灯照射五氯酚溶液,配上截止滤光片(λ>420nm)。实验过程中,同样采用充氧曝气。整个光照反应在密闭不透光的环境下进行。最后灵活施加静磁场与交变磁场,可以使磁性颗粒表面包覆的光催化剂能够与有机污染物及光源充分接触,在可见光照射400分钟后,五氯酚的去除率达到94.3%,光量子效率为0.32%,总有机碳TOC的去除率(矿化率)达91.5%。A self-made magnetic field-photocatalytic reaction system is used, and an alternating magnetic field generator with adjustable magnetic field strength is used, and the magnetic field strength is selected from 0.3 to 0.6T (Tesla). The light source is a 300W xenon lamp. Using γ-Fe 2 O 3 (ferromagnetic particle core)-Y 2 YbSbO 7 (photocatalytic shell), SiO 2 (paramagnetic particle core)-Y 2 YbSbO 7 (photocatalytic shell) and MnO (antiferromagnetic particle core) )-Y 2 YbSbO 7 (photocatalyst shell) was used as the catalyst, and the volume percentage of the above three magnetic composite photocatalytic materials each accounted for one-third, and the typical refractory pentachlorophenol in water was selected as the target degradation product. When the magnetic field strength is 0.3-0.6 tesla, the above three kinds of magnetic composite catalyst particles are distributed in a gradient in the aqueous solution containing pentachlorophenol, and can be uniformly distributed in the upper, middle and lower layers of the aqueous solution. At this time, 900 mL of pentachlorophenol aqueous solution was selected, and the weight of Y 2 YbSbO 7 coated on the surface of all magnetic particles was close to 2.4 g. The initial concentration of pentachlorophenol aqueous solution was 0.1 mmol L -1 , and the initial pH value was 7. Choose a 300W xenon lamp to irradiate the pentachlorophenol solution, and add a cut-off filter (λ>420nm). During the experiment, oxygenation and aeration were also used. The entire light reaction was carried out in a closed and light-tight environment. Finally, the flexible application of static and alternating magnetic fields can make the photocatalyst coated on the surface of the magnetic particles fully contact with organic pollutants and light sources. After 400 minutes of visible light irradiation, the removal rate of pentachlorophenol reaches 94.3%, and the photon quantum efficiency is 0.32%, the removal rate (mineralization rate) of total organic carbon TOC reaches 91.5%.
9.采用Y2GaSbO7分解水制取氢气9. Using Y 2 GaSbO 7 to decompose water to produce hydrogen
在密闭的由多个阀门控制的玻璃管路内部照明反应器内进行分解水制取氢气实验,照射光源采用300W的氙灯(入射光通量为4.513×10-6Einstein L-1s-1,420nm截止滤光片)或400W(入射光通量为6.013×10-6Einstein L-1s-1,390nm截止滤光片)的高压汞灯,在300mL纯水中放入Y2GaSbO7粉末0.8g。溢出的氢气产率采用带有TCD的气相色谱-质谱联用仪测定,该气相色谱-质谱联用仪和密闭环路内部照明反应器相连。在反应之前密闭环路内部照明反应器内各种气体被去除,氩气被充入该反应器,直到反应器内的氧气和氮气被完全去除。在氙灯照射下24小时后,氢气的产量为762.4微摩尔,氧气的产量为378.5微摩尔;在高压汞灯照射下24小时后,氢气的产量为2148.8微摩尔,氧气的产量为1069.2微摩尔。The experiment of producing hydrogen by splitting water was carried out in a closed glass tube internal lighting reactor controlled by multiple valves. The light source used was a 300W xenon lamp (incident luminous flux: 4.513×10 -6 Einstein L -1 s -1 , cut-off at 420nm filter) or a 400W (incident luminous flux: 6.013×10 -6 Einstein L -1 s -1 , 390nm cut-off filter) high-pressure mercury lamp, put 0.8g of Y 2 GaSbO 7 powder in 300mL pure water. The overflow hydrogen yield was determined using a gas chromatograph-mass spectrometer with a TCD connected to a closed-loop internally illuminated reactor. Before the reaction, various gases in the closed-loop internal lighting reactor were removed, and argon was charged into the reactor until the oxygen and nitrogen in the reactor were completely removed. After 24 hours under the irradiation of a xenon lamp, the production of hydrogen was 762.4 micromoles, and the production of oxygen was 378.5 micromoles; after 24 hours under the irradiation of a high-pressure mercury lamp, the production of hydrogen was 2148.8 micromoles, and the production of oxygen was 1069.2 micromoles.
以Y2GaSbO7粉末为催化剂,分别负载Pt,NiO和RuO2辅助催化剂分解水制取氢气,入射光主波长为λ=360nm,催化剂0.8g,纯水300mL,50mL CH3OH,光源为400W高压汞灯,以0.2wt%-Pt/Y2GaSbO7为复合催化剂,24小时后氢气的产量为5.46mmol;以1.0wt%-NiO/Y2GaSbO7为复合催化剂,24小时后氢气的产量为4.12mmol;以1.0wt%-RuO2/Y2GaSbO7为复合催化剂,24小时后氢气的产量为3.18mmol。Use Y 2 GaSbO 7 powder as catalyst, load Pt respectively, NiO and RuO 2 assist catalyst to decompose water to produce hydrogen, the main wavelength of incident light is λ=360nm, catalyst 0.8g, pure water 300mL, 50mL CH 3 OH, light source 400W High-pressure mercury lamp, with 0.2wt%-Pt/Y 2 GaSbO 7 as the composite catalyst, the hydrogen production after 24 hours is 5.46mmol; with 1.0wt%-NiO/Y 2 GaSbO 7 as the composite catalyst, the hydrogen production after 24 hours 4.12mmol; with 1.0wt%-RuO 2 /Y 2 GaSbO 7 as the composite catalyst, the hydrogen production after 24 hours was 3.18mmol.
10.采用Y2YbSbO7分解水制取氢气10. Using Y 2 YbSbO 7 to decompose water to produce hydrogen
在密闭的由多个阀门控制的玻璃管路内部照明反应器内进行分解水制取氢气实验,照射光源采用300W的氙灯(入射光通量为4.513×10-6Einstein L-1s-1,420nm截止滤光片)或400W(入射光通量为6.013×10-6Einstein L-1s-1,390nm截止滤光片)的高压汞灯,在300mL纯水中放入Y2YbSbO7粉末0.8g。溢出的氢气产率采用带有TCD的气相色谱-质谱联用仪测定,该气相色谱-质谱联用仪和密闭环路内部照明反应器相连。在反应之前密闭环路内部照明反应器内各种气体被去除,氩气被充入该反应器,直到反应器内的氧气和氮气被完全去除。在氙灯照射下24小时后,氢气的产量为658.6微摩尔,氧气的产量为326.1微摩尔;在高压汞灯照射下24小时后,氢气的产量为1836.5微摩尔,氧气的产量为915.8微摩尔。The experiment of producing hydrogen by splitting water was carried out in a closed glass tube internal lighting reactor controlled by multiple valves. The light source used was a 300W xenon lamp (incident luminous flux: 4.513×10 -6 Einstein L -1 s -1 , cut-off at 420nm filter) or a 400W (incident luminous flux: 6.013×10 -6 Einstein L -1 s -1 , 390nm cut-off filter) high-pressure mercury lamp, put 0.8g of Y 2 YbSbO 7 powder in 300mL pure water. The overflow hydrogen yield was determined using a gas chromatograph-mass spectrometer with a TCD connected to a closed-loop internally illuminated reactor. Before the reaction, various gases in the closed-loop internal lighting reactor were removed, and argon was charged into the reactor until the oxygen and nitrogen in the reactor were completely removed. After 24 hours under the irradiation of a xenon lamp, the production of hydrogen was 658.6 micromoles, and the production of oxygen was 326.1 micromoles; after 24 hours under the irradiation of a high-pressure mercury lamp, the production of hydrogen was 1836.5 micromoles, and the production of oxygen was 915.8 micromoles.
以Y2YbSbO7粉末为催化剂,分别负载Pt,NiO和RuO2辅助催化剂分解水制取氢气,入射光主波长为λ=360nm,催化剂0.8g,纯水300mL,50mL CH3OH,光源为400W高压汞灯,以0.2wt%-Pt/Y2YbSbO7为复合催化剂,24小时后氢气的产量为4.72mmol;以1.0wt%-NiO/Y2YbSbO7为复合催化剂,24小时后氢气的产量为3.89mmol;以1.0wt%-RuO2/Y2YbSbO7为复合催化剂,24小时后氢气的产量为2.63mmol。Use Y 2 YbSbO 7 powder as a catalyst, load Pt, NiO and RuO 2 to assist the catalyst to decompose water to produce hydrogen, the main wavelength of the incident light is λ=360nm, the catalyst is 0.8g, pure water is 300mL, CH 3 OH is 50mL, and the light source is 400W High-pressure mercury lamp, with 0.2wt % -Pt/ Y2YbSbO 7 as the composite catalyst, the hydrogen production after 24 hours is 4.72mmol; with 1.0wt%-NiO/ Y2YbSbO7 as the composite catalyst, the hydrogen production after 24 hours 3.89mmol; with 1.0wt%-RuO 2 /Y 2 YbSbO 7 as the composite catalyst, the hydrogen production after 24 hours was 2.63mmol.
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