Selective catalytic reduction of nitric oxide by propane over vanadia-titania aerogels

An investigation has been carried out of the effect of vanadia loading on the activity and selectivity ofV₂O₅TiO₂ aerogel catalysts, prepared by a two-step procedure, for the reduction of NO by propane. The structure of catalysts have been characterized by laser Raman spectroscopy and XRD measurements. At vanadia loading levels below ca. 4.4 wt%, the vanadia is present in the form of coordinated polymeric species, whereas crystallites of V₂O₅ are formed at higher vanadia contents. At this critical level of 4.4 wt% V₂O₅, the kinetic measurements showed also a maximum in the activity per mass of catalyst which very likely indicated that the coordinated polymeric surface species are more active than crystalline V₂O₅. The selectivity towards the formation of dinitrogen decreased as the loading increased, presumably because of the formation of larger polymeric species and V₂O₅ crystallites, below and above the critical loading level, respectively. For the reduction of NO by propane, titania supported vanadia aerogel catalysts are significantly more active, per mass of catalyst, and more selective towards N₂ formation than conventionalV₂O₅TiO₂ and V₂O₅Al₂O₃ aerogel catalysts, at vanadia loading levels below ca. 11 wt%.     

The role of carbon deposition on precious metal catalyst activity during dry reforming of biogas

Gold and palladium were supported on a mesoporous TiO₂ for total oxidation of volatile organic compounds (VOCs). Mesoporous high surface area titania support was synthesised using of Ti(OC₂H₅)₂ in the presence of CTMABr surfactant. After removing the surfactant molecules, 0.5 or 1.5 wt% of palladium and 1 wt% of gold were precipitated on the support by, respectively, wet impregnation and deposition–precipitation methods. The activity for toluene and propene total oxidation of the prereduced samples follows the same order: 0.5%Pd-1%Au/TiO₂ > 1.5%Pd/TiO₂ > 0.5%Pd/TiO₂ > 1%Au-0.5%Pd/TiO₂ > 1%Au/TiO₂ > TiO₂. Moreover, a catalytic comparison with samples based on a conventional TiO₂, shows the catalytic advantage of the mesoporous TiO₂ support. The promotional effect of gold added to palladium could be partly explained by small metallic particles (TEM), but meanly by metallic particles made up of Au-rich core with a Pd-rich shell. Moreover, the hydrogen TPR profile of 0.5%Pd-1%Au/TiO₂ shows only the signal attributed to small PdO particles. Gold also implies a protecting effect of the support under reduction atmosphere. Operando diffuse reflectance infrared fourier transform (DRIFT) spectroscopy was carried on and allowed to follow the VOCs oxidation and the formation of coke molecules, but also a metallic electrodonor effect to the adsorbed molecule which increases in the same order as the activity for oxidation reaction. The presence of coke after test was also shown by DTA–TGA by exothermic signals between 300 and 500 °C and by EPR (g = 2.003).     

臭氧氧化-光催化降解水中的五氯酚

利用臭氧氧化-光催化技术降解水中的有机污染物五氯酚(PCP)。对比了紫外光照射、臭氧氧化、光催化、臭氧氧化-光催化4种方法降解PCP的情况。考察了臭氧氧化-光催化体系中臭氧流量、臭氧产量、PCP初始质量浓度、pH和CO23-等因素对PCP降解率的影响。实验结果表明,臭氧氧化-光催化法比单独使用紫外光照射、臭氧氧化、光催化法更能有效的去除PCP;增加臭氧流量和臭氧产量有利于提高PCP的降解率;降低PCP的初始浓度,PCP的降解率显著提高;pH对PCP的降解效果影响不明显;CO23-的存在显著降低了PCP的降解率。在臭氧氧化-光催化体系中,除臭氧直接氧化降解PCP外,臭氧与TiO2协同作用产生的.OH对PCP的降解也起到了重要作用。     

TiO_2粉体性能对PTC热敏电阻性能的影响

ＴｉＯ_２的纯度、粒度及粒形对ＢａＴｉＯ_３系ＰＴＣＲ的性能影响很大，对所用ＴｉＯ_２加以选择非常重要，国产和日本产ＴｉＯ_２原料在粉体性能上存在差异。     

非平衡等离子体协同作用光催化剂催化降解苯

采用非平衡等离子体与光催化剂相结合,对苯的降解进行了实验研究。考察了以不同吸附能力的玻璃球和γ-Al2O3为载体对苯降解率、碳平衡、CO2选择性、NOx及O3生成量的影响;研究了以γ-Al2O3为载体时,水蒸气含量对苯的降解率、碳平衡、CO2选择性、NOx及O3生成量的影响。实验结果表明,以具有吸附性的γ-Al2O3为载体可提高苯的降解率;当能量密度为618J/L时,苯的降解率可达98%;同时可降低O3的生成量,但NOx生成量增加;以γ-Al2O3为载体时,随水蒸气含量的增加,苯的降解率降低,特别是在低能量密度时,水蒸气对苯降解率的影响更为显著,但水蒸气的加入可抑制O3的生成,同时可提高碳平衡值。     

过渡金属对Au-Pd/TiO_2-Al_2O_3催化剂加氢脱硫性能的影响

研究了掺杂过渡金属Ru,Ni,Co对Au-Pd/TiO2-Al2O3催化剂催化噻吩加氢脱硫活性的影响,并采用X射线衍射、电感耦合等离子发射光谱、程序升温还原和程序升温脱附等方法对TiO2-Al2O3复合载体、Au-Pd/TiO2-Al2O3和Au-Pd-TM/TiO2-Al2O3(TM表示过渡金属)催化剂进行了表征。实验结果表明,掺杂过渡金属未改变Au-Pd/TiO2-Al2O3催化剂的结构;掺杂Ru或Ni增强了Au-Pd/TiO2-Al2O3催化剂的活性组分与TiO2-Al2O3复合载体的相互作用,降低了反应活化能,提高了催化剂活性组分的分散度和活性比表面积,改善了Au-Pd/TiO2-Al2O催化剂的吸附性能,从而提高了Au-Pd/TiO2-Al2O3催化剂催化噻吩加氢脱硫的活性;而掺杂Co的效果则与之相反。     

Preparations of nanosized TiO2 in reverse microemulsion and their photocatalytic activity

Nanosized titania sol has been produced by the controlled hydrolysis of titanium tetraisopropoxide (TTIP) in sodium bis(2-ethylhexyl)sulfosuccinate (AOT) reverse micelles. The physical properties, such as surface area, crystallite size and crystallinity according to R and W₀ ratio, have been investigated by TEM, XRD, BET, FT–IR, TGA and DTA. In addition, the photocatalytic decomposition of p-nitrophenol has been studied by using a batch reactor in the presence of UV light in order to compare the photocatalytic activity of prepared nanosized titania. It is shown that the anatase structure appears in the 300–600 °C calcination temperature range and the transformation of anatase into rutile starts above 700 °C. The crystallite size increases with increasing R and W₀ ratio but W₀ ratio shows a stronger effect on the crystallite size than R ratio. In the photocatalytic decomposition of p-nitrophenol, the photocatalytic activity is mainly determined by the crystallinity of titania. In addition, the titania calcined at 500 °C shows the highest activity on the photocatalytic decomposition of p-nitrophenol() and the pure anatase structure.     

铈和锰掺杂纳米TiO2的溶胶-凝胶法制备及其光催化性能

采用溶胶-凝胶法制备了TiO₂、Mn⁴⁺/TiO₂、Ce⁴⁺/TiO₂和Mn⁴⁺-Ce⁴⁺/TiO₂光催化剂。通过考察掺杂离子的种类和用量对所得催化剂用于紫外光催化降解甲基橙性能的影响，表明Ce⁴⁺/TiO₂中Ce⁴⁺的适宜掺杂量为1.0%，Ce⁴⁺-Mn⁴⁺/TiO₂中，当Mn4+的掺杂量为25.0%时，Ce⁴⁺的适宜掺杂量为0.50%，相应的脱色效率为92.39%和99.41%。当掺杂量适当时，四种催化剂用于紫外光催化降解甲基橙的活性次序为：Mn⁴⁺-Ce⁴⁺/TiO₂ > TiO₂>Ce⁴⁺/TiO₂> Mn⁴⁺/TiO₂。XRD分析结果表明，所得光催化剂均为锐钛矿型纳米粒子。     

磁化水配料对TiO2压敏陶瓷电性能和微观结构的影响

研究了使用磁化水配料对TiO2压敏陶瓷电性能和微观结构的影响。电性能测量及SEM和XRD微观结构分析结果表明：磁化水配料制备的TiO2压敏电阻具有较低的压敏电压和较高的非线性指数α。材料的主晶相为金红石相，由Ce,Si,Ti组成的Perrierite第二相均匀分布在晶界区域。因此，采用磁化水配料可以改善材料的工艺性能和陶瓷烧结体的微观结构，从而提高元件的电性能。     

TiO_2薄膜光催化降解甲基橙反应动力学研究

以甲基橙为模型污染物、TiO2薄膜为光催化剂,在自制的光催化反应器上进行了光催化降解反应实验,主要研究了甲基橙初始浓度(c0)和紫外光光照强度(I)对其光催化降解反应的影响。结果表明,该降解反应可用一级反应动力学方程进行描述,反应速率常数(k)与c0及光强I的关系分别为:k∝c0-1 4和k∝I0.65。