MnOx/ZrO2纳米催化剂的制备及CO-SCR-NO性能研究

以氧氯化锆和硝酸锰为主要原料,采用Sol-Gel-VFD技术制备了MnOx/ZrO2超细粉体材料.用XRD,TG-DSC,TEM和BET等技术对试样进行了表征,用微反应器-气相色谱仪在线研究了试样选择性催化还原NO的活性.结果表明:用Sol-Gel-VFD技术可制得粒子尺寸约为20nm、具有高催化活性的负载型MnOx/ZrO2纳米催化剂,活性组分锰对NO的催化还原起了主要作用.添加铈组分能提高MnOx/ZrO2纳米催化剂催化还原NO的活性.     

钯钌原子比对碳载Pd-Ru催化剂催化H2O2电还原性能影响

利用化学还原法制备了不同原子比的碳载Pd-Ru催化剂,考察了钯钌原子比对碳载Pd-Ru催化剂催化H2O2电还原反应性能的影响。研究结果表明,随着Ru元素的增加,碳载Pd-Ru催化剂的粒径逐渐减小,各催化剂上H2O2电还原反应的起始还原电势稳定在0.82V,电流密度先增大后减小。当Pd∶Ru=1∶1时,PdRu/C催化剂表现了最好的催化性能。     

掺杂不同量Nd2O3对CeO2-ZrO2-Al2O3材料性能的影响

采用共沉淀法制备了一系列Nd2O3含量为0～13wt%的CeO2-ZrO2-A12O3(CZA)复合氧化物,并通过X射线衍射(XRD)、低温N2吸附–脱附、氧脉冲吸附(OSC)、H2–程序升温还原(H2-TPR)及扫描电子显微镜(SEM)等方法对所制备的材料进行了表征.研究结果表明,Nd2O3在CZA固溶体中的溶解限约为10wt%,过量Nd的添加会出现分相形成Nd0.5Ce0.5O1.75氧化物.掺杂适量Nd能有效抑制氧化物晶粒的长大,提高材料的热稳定性和氧化还原性能.Nd2O3的掺杂量为10wt%时,样品的织构稳定性最好,1000℃老化5 h后,比表面积和孔容分别达97.14 m2/g和0.44 mL/g.Nd2O3的掺杂量为7wt%时,样品有高的储氧量,经600℃和1000℃焙烧后储氧量分别为938.01μmol/g和821.72μmol/g;体相氧的移动能力最强,还原性能最佳,老化后还原峰温由465℃升高到483℃.SEM结果表明,所制备的材料均为球形颗粒,Nd2O3的添加可以有效阻止高温焙烧过程中粒子的团聚.     

Zr助剂对富氧条件下Ag/Al2O3选择性催化C3H6还原NO性能的影响

采用浸渍法制备了不同Zr助剂改性的Ag/Al_2O_3的Ag-Zr系列催化剂,在富氧条件下对比其对选择性催化还原NO的影响。采用XRD、H_2-TPR、NH_3-TPD和O_2-TPD技术对催化剂进行了表征。研究结果表明,以硝酸锆为Zr源的先浸渍Zr后浸渍Ag的1.5%Ag/1%Zr/Al_2O_3催化剂具有最好的催化活性,与Ag/Al_2_3催化剂相比,400℃和450℃的NO转化率分别提高了10%和8%。XRD表征表明少量Zr的添加增强了催化剂的体相储氧能力。H_2-TPR表征表明Zr助剂的添加提高了催化剂的低温活性。NH_3-TPD表明Zr助剂的添加可以增加催化剂的弱酸和中等强度酸中心。O_2-TPD表明Zr的添加显著增强了催化剂储氧能力,从而提高其对NO的催化还原性能。     

Fe2O3在氧化铝碳热还原-氯化法炼铝过程中的行为分析

在中真空(15~100 Pa)、993~1723 K下,采用X射线衍射、扫描电镜及能谱仪等分析手段对Fe2O3在氧化铝碳热还原及氯化过程的行为以及Fe2O3的添加量对产物金属铝的直收率的影响进行了研究。结果表明:在碳热还原过程中、不通入氯化铝气体时:当温度低于1273 K,Fe2O3逐渐与C反应生成Fe;当温度处于1273~1473 K之间,Al2O3发生晶型转变;当温度处于1473~1623 K之间,有Fe3C生成;当温度处于1723 K,由于生成的Fe3C与剩余的Fe形成熔体,包裹Al2O3与C,使Al2O3与C反应生成大量的Al3C4及Al4O4C。通入氯化铝发生氯化反应后,此时有金属铝生成,并且在冷凝物中未发现含Fe物质。在1723 K下,物料中添加适量的Fe2O3可以降低氧化铝真空碳热还原反应的温度,提高反应的速率从而提高铝的产率。     

Pt/MoO3/ZrO2催化剂的制备及三效催化性能的研究

采用浸渍法制备了MoOz/ZrO2,用低温氮吸附-脱附法和NH3-程序升温脱附法(TPD)分别对其比表面积和酸碱性进行了表征.结果表明,MoO3/ZrO2具有106.8m2/g的比表面积和超强酸的性能.用等体积浸渍法制备了Pt/MoO3/ZrO2催化剂,在汽车尾气模拟气中考察了其对C3H8、CO和NO的催化活性.与传统三效催化剂Pt/La2O3/Al2O3相比较,Pt/MoO3/ZrO2具有更好的低温起燃性能和更宽的空燃比窗口,并显著地改善了C3H8在富氧状态下的转化效率.通过XRD、H2-TPR对催化剂进行了表征,结果表明,Pt在催化剂载体上具有高度的分散性和优异的氧化还原性能.     

Mn-Cu-La/TiO_2低温催化剂催化还原氮氧化物性能研究

采用浸渍法制备了Mn-Cu-La/TiO2催化剂,研究了其组分配比、焙烧温度等制备条件和NO进口浓度、空速、O2含量、NH3/NO摩尔比等操作条件对Mn-Cu-La/TiO2上NH3低温还原NO活性的影响;探讨了H2O、SO2对Mn-Cu-La/TiO2活性的影响.结果表明,该催化剂具有很好的低温SCR活性,空速为10 000h-1,反应温度为150℃下时NO转化率接近99.6%.180℃下同时通SO2、H2O后的360min内,活性始终保持在95%以上;单独通入SO2时,该催化剂较容易中毒;单独通入体积分数10%的H2O对催化剂活性基本没有影响,转化率始终保持在98%以上.     

低温制备纳米α-Al2O3粉体

研究了以Al(NO3)3.9H2O和NH3．H2O溶液为原料,采用高纯氧化铝球磨原位引入晶种和添加ZnF2、AlF3的制备工艺,通过提高凝胶中晶种的均匀性和加速相转变时物质的扩散和传输,可降低过渡型氧化铝向α型氧化铝相转变温度,所制铝凝胶经900－920℃煅烧可获得平均粒径＜50nm的α型纳米氧化铝。     

Fe对Mn/CeO2-TiO2催化剂低温NH3选择性催化还原NO的影响

以锰氧化物为活性组分,CeO2-TiO2为载体制备了Mn/CeO2-TiO2催化剂.考察了Fe的加入对Mn/CeO2-TiO2的低温NH3-SCR活性的影响.并采用BET比表面积,H2程序升温还原(H2-TPR)和X射线光电子能谱(XPS)等手段对催化剂进行了表征.活性结果表明,Fe的引入显著改善了Mn/CeO2-TiO2的NH3-SCR活性,催化剂在113～250℃之间表现出良好的NO去除效率.表征结果表明,Fe的引入促进了锰物种在CeO2-TiO2表面的分散,降低了Mn-Fe/CeO2-TiO2中锰物种的还原温度.XPS分析指出Mn-Fe/CeO2-TiO2表面Mn以+4价存在,而Fe主要以+3价的Fe2O3存在,且Fe与载体表面间存在强相互作用.     

超临界抗溶剂法纳米Al_2O_3-ZrO_2颗粒的制备与表征

以CO2为抗溶剂介质,无水乙醇为溶剂,采用超临界抗溶剂法(SAS)制备了纳米Al2O3-ZrO2复合氧化物颗粒的前驱体—纳米Al(NO3)3-Zr(NO3)4颗粒,系统考察了温度和压力等因素对制备过程的影响,并对前驱体中Al、Zr组分的共抗溶剂效应进行了研究,通过焙烧前驱体Al(NO3)3-Zr(NO3)4制得了纳米Al2O3-ZrO2球形颗粒.采用热重质谱(TG-MS)、X射线衍射(XRD)、X射线光电子能谱(XPS)、场发射透射电镜(FEG-TEM)和程序升温还原(TPR)等技术对所制备的前驱体Al(NO3)3-Zr(NO3)4和Al2O3-ZrO2纳米颗粒的物化性能进行了表征,初步考察了Al2O3-ZrO2纳米颗粒负载Ni催化剂的还原性能.研究发现,该纳米复合氧化物比用浸渍?沉淀法制得的Al2O3-ZrO2载体对活性组分Ni具有更好的分散性能,作为新型催化剂载体材料有良好的应用前景.     

Pd负载型介孔ZrO2-TiO2复合材料的设计合成及其CO催化氧化性能研究

以介孔结构的复合ZrO₂-TiO₂为载体负载活性组分, 制备了具有高CO催化氧化活性的Pd/ZrO₂-TiO₂与PdCu/ZrO₂-TiO₂负载型催化剂。XRD、TEM研究结果表明: 活性组分Pd、Cu物种可均匀分散于介孔载体中。系统考察了不同的催化剂载体、制备方法和助催化剂等对该介孔复合材料CO催化氧化性能的影响, 结果表明: 以ZrO₂-TiO₂为载体的催化剂其CO催化氧化活性明显优于以介孔Al₂O₃或介孔SBA-15为载体的催化剂; 一步法制备的介孔Pd/ZrO₂-TiO₂催化剂其CO催化氧化的低温活性较浸渍法制备的Pd/ZrO₂-TiO₂有很大提高; 并且Pd和Cu物种共负载的介孔ZrO₂-TiO₂复合催化剂具有最优的CO催化氧化活性, 其CO的完全催化氧化温度可降至170℃, O₂-TPD分析说明Pd和Cu之间的相互作用使得PdCu/ZT催化剂在更低温度具有氧化还原活性。     

Decolorization of molasses fermentation wastewater by SnO(2)-catalyzed ozonation

In the presence of O(3), the oxidative decolorization reaction on molasses fermentation wastewater with SnO(2) as a catalyst was studied. The results showed that SnO(2) accelerated the ozone oxidation reaction and the oxidative decolorization of molasses fermentation wastewater was accelerated. Influences on SnO(2) catalytic ozonation activity by precipitants and the calcination temperature were studied by XRD, IR and TG-DSC. SnO(2) prepared by ammonia as the precipitant had higher catalytic activity and a stronger dehydroxylation. The IR spectra of adsorbed pyridine showed that there were Lewis acid sites on the surface of this SnO(2) catalyst. The main factors influencing molasses fermentation wastewater oxidative decolorization were the wastewater concentration, the O(3) concentration, the pH value and the catalyst dosage. The decolorization of wastewater was improved with the increase of the wastewater dilution ratio, the ozone concentration and the catalyst dosage. High activity *OH was found to be existing with less amount and low concentration in the process of SnO(2) catalyzed ozonation decolorization.     

Influence of physicochemical treatments on iron-based spent catalyst for catalytic oxidation of toluene

The catalytic oxidation of toluene was studied over an iron-based spent and regenerated catalysts. Air, hydrogen, or four different acid solutions (oxalic acid (C2H2O4), citric acid (C6H8O7), acetic acid (CH3COOH), and nitric acid (HNO3)) were employed to regenerate the spent catalyst. The properties of pretreated spent catalyst were characterized by the Brunauer Emmett Teller (BET), inductively coupled plasma (ICP), temperature programmed reduction (TPR), and X-ray diffraction (XRD) analyses. The air pretreatment significantly enhanced the catalytic activity of the spent catalyst in the pretreatment temperature range of 200-400 degrees C, but its catalytic activity diminished at the pretreatment temperature of 600 degrees C. The catalytic activity sequence with respect to the air pretreatment temperatures was 400 degrees C>200 degrees C>parent>600 degrees C. The TPR results indicated that the catalytic activity was correlated with both the oxygen mobility and the amount of available oxygen on the catalyst. In contrast, the hydrogen pretreatment had a negative effect on the catalytic activity, and toluene conversion decreased with increasing pretreatment temperatures (200-600 degrees C). The XRD and TPR results confirmed the formation of metallic iron which had a negative effect on the catalytic activity with increasing pretreatment temperature. The acid pretreatment improved the catalytic activity of the spent catalyst. The catalytic activity sequence with respect to different acids pretreatment was found to be oxalic acid>citric acid>acetic acid>or=nitric acid>parent. The TPR results of acid pretreated samples showed an increased amount of available oxygen which gave a positive effect on the catalytic activity. Accordingly, air or acid pretreatments were more promising methods of regenerating the iron-based spent catalyst. In particular, the oxalic acid pretreatment was found to be most effective in the formation of FeC2O4 species which contributed highly to the catalytic combustion of toluene.     

Effect of palladium precursor and preparation method on the catalytic performance of Pd/SiO2 catalysts for benzene hydrogenation

Supported Pd catalysts on silica were prepared by different synthesis methods using Pd(Ac)₂ and PdCl₂ as salts precursors. The obtained materials were characterized by X-Ray Diffraction (XRD), H₂ chemisorption, and temperature programmed desorption of hydrogen (H₂-TPD). The catalytic performances of these catalysts have been evaluated in the hydrogenation of benzene. The obtained results show that metal dispersion and catalytic activity are strongly dependent on the salts precursor and the method of preparation of the catalyst. The catalysts prepared by hydrazine reduction exhibit higher activity in benzene hydrogenation than that by the polyol reduction method. Moreover, the catalyst prepared with palladium acetate showed higher catalytic activity than those prepared with palladium chloride. The superior catalytic performance of this catalyst in the hydrogenation of benzene was ascribed to a significantly better dispersion of Pd particles on the silica support.     

TiO2纳米棒光催化降解甲基橙的研究

本文以甲基橙为目标降解物考察了催化剂的添加量、甲基橙溶液的pH值、晶化时间、热处理温度等因素对用"软模板"制备的TiO2纳米棒光催化活性的影响.研究表明:当催化剂添加量为0.08g、甲基橙溶液的pH=4、晶化时间为24h、热处理温度为500℃时,TiO2光催化剂的催化效果最佳,达到了85.96%.     

1,2 -二氯乙烷在担载铈钛复合氧化物的蜂窝陶瓷催化净化——催化组分颗粒大小的影响

采用溶胶-凝胶法制备担载 TiO2 和 CeTiOx 复合氧化物涂层的堇青石蜂窝陶瓷整体式催化剂,并考察 1,2-二氯乙烷(DCE)在上述催化剂上的催化效果。结果表明:TiO2 和 CeTiOx 复合氧化物涂层材料对DCE 的催化燃烧均具有很好的催化活性, 前者在 400 ℃时,DCE 的转化率为 93.1%,后者已达 98.5%,可见,CeTiOx 可以更有效地催化燃烧处理 DCE。譬如,在 300 ℃时,在 CeTiOx 涂覆的催化剂上 DCE 的转化率为 85.6%。但随着催化剂处理温度的升高,CeTiOx 催化活性组分的颗粒变大,导致 CeTiOx 蜂窝陶瓷催化剂对于 DCE 的催化活性降低。     

活性炭负载CaCl2催化五氯乙烷脱HCl的研究

筛选出了催化性能较好的活性炭负载氯化钙(CaCl2/AC)催化剂用于五氯乙烷脱HCl制备四氯乙烯。考察了反应温度、空速、CaCl2负载量对CaCl2/AC催化剂催化性能的影响及催化剂的稳定性。实验结果表明最佳反应条件:反应温度为240℃,空速为3.4h-1,CaCl2负载量为0.3mmol/g,在此反应条件下五氯乙烷的转化率可达99%以上,四氯乙烯的收率达95%以上,催化剂催化性能重现性良好。采用X射线衍射(XRD)、氮气吸附-脱附对催化剂进行了表征。结果表明CaCl2在活性炭表面分散良好;随着CaCl2负载量的增加,CaCl2/AC催化剂的BET比表面及孔容逐渐减小。     

共聚法负载茂钛催化剂的合成及催化苯乙烯配位聚合

通过将带有不饱和双键的茂化合物(对-(1-环戊二烯甲基)-苯乙烯)与苯乙烯、二乙烯基苯共聚,再与乙基锂反应,最后与钛酸四丁酯络合的方法合成负载茂钛催化剂。将此催化剂与格氏试剂(RMgBr)组成催化体系．考察了催化反应温度、催化体系的组成,催化剂浓度和Mg／Ti摩尔比等因素对苯乙烯聚合的影响。结果表明,负载化可减少活性中心的偶联衰减,提高催化活性。催化活性与负栽催化剂的结构、反应条件等因素密切相关。     

Efficient mineralization of dimethyl phthalate by catalytic ozonation using TiO2/Al2O3 catalyst

The removal of dimethyl phthalate (DMP), which is a pollutant of concern in water environments, was carried out by catalytic ozonation with TiO₂/Al₂O₃ catalysts. The heterogeneous catalytic ozonation was an ozonation process combined with the catalytic and adsorptive properties of the TiO₂/Al₂O₃ catalysts to significantly accelerate the mineralization efficiency. Semi-batch ozonation was performed under various experimental conditions including the fed ozone concentration, catalyst type, catalyst dosage, and ultraviolet radiation on the degradation of DMP. The complete removal of DMP was efficiently achieved by both sole and catalytic ozonation; meanwhile, the presence of the catalysts slightly accelerated the elimination rate of DMP. On the other hand, the mineralization efficiency, in terms of total organic carbon (TOC) removal, was substantially enhanced by employing the TiO₂/Al₂O₃ catalyst. The mineralization efficiency using the TiO₂/Al₂O₃ catalyst was the highest, followed in decreasing order by the Al₂O₃ catalyst, the TiO₂ catalyst, and sole ozonation. In addition, the use of the TiO₂/Al₂O₃ catalyst would increase the utilization efficiency of the fed ozone, especially in the late ozonation period. Furthermore, the decrease in the catalytic activity of the TiO₂/Al₂O₃ catalyst after multi-run experiments can be mostly recovered by an incineration process at a high temperature.