Au/CeO2/Y和Au-MFe2O4催化剂用于有氧条件下CH4还原NOx的研究

以CeO2／Y分子筛和MFe2O4(M=Ni,Co，Zn)为载体，制备Au／CeO2／Y和Au-MFe2O4负载型金催化剂．用CH4做还原剂，考察了它们在有氧条件下催化还原NOχ的活性．结果表明：在Au-Y中引人助剂Ce，使得Au／CeO2／Y的催化活性高于Au／Y；Au-CoFe2O4的催化活性高于Au-Fe2O3，反应温度为300℃时，NOχ在Au-CoFe2O4上的转化率达到39．70%．     

V2O5-WO3/TiO2催化剂氨法SCR脱硝反应动力学研究

In this work, a kinetic study of the selective catalytic reduction of NO with NH3 has been carried out. After proving the operating condition that the effect of intraphase diffusion and interphase mass-transfer processes can be ignored, the selective catalytic reduction of NO with NH3 on the catalytic activity of V2O5-WO3/TiO2 has been carried out with fixing the feed gas flow rate and composition （ NO, NH3, O2 ） while varying the catalyst loading. Based on the experimental results of NO removal efficiency, the empirical catalytic reaction rate equation of NO with NH3 has been obtained using differential analysis. The experimental result is further proved by the graphic integral method at the temperature from 320℃to 400 ℃ The reaction order is 1 to NO and zero to NH3. The reaction follows the Eley-Rideal mechanism model.     

富氧条件下乙炔选择催化还原NOx

Acetylene as a reducing agent of metal exchanged HY catalysts, for selective catalytic reduction of NO in the reaction system of 0.16% NO, 0 （C2H2-SCR） was investigated over a series 08% C2H2, and 9.95% O2 （volume percent） in He. 75% of NO conversion to N2 with hydrocarbon efficiency about 1.5 was achieved over a Ce-HY catalyst around 300 ℃. The NO removal level was comparable with that of selective catalytic reduction of NOx by C3H6 reported in literatures, although only one third of the reducing agent in carbon moles was used in the C2H2-SCR of NO. The protons in zeolite were crucial to the C2H2-SCR of NO, and the performance of HY in the reaction was significantly promoted by cerium incorporation into the zeolite. NO2 was proposed to be the intermediate of NO reduction to N2, and the oxidation of NO to NO2 was rate-determining step of the C2H2-SCR of NO over Ce-HY. The suggestion was well supported by the results of the NO oxidation with O2, and the C2H2 consumption under the conditions in the presence or absence of NO.     

焙烧温度对CuO/γ-Al2O3和CeO2-CuO/γ-Al2O3催化剂NO还原活性的影响

用浸渍法制备了CuO/γ-Al2O3催化剂和CeO2改性的CeO2-CuO/γ-Al2O3催化剂,考察了焙烧温度对CuO/γ-Al2O3和CeO2-CuO/γ-Al2O3催化剂C3H6还原NO反应活性的影响,以及CeO2的添加量对CeO2-CuO/γ-Al2O3催化剂C3H6还原NO反应活性的影响。结果表明,在200 ℃～500 ℃的焙烧温度范围内,焙烧温度对CuO/γ-Al2O3催化剂的活性影响很小；在500 ℃～800 ℃的焙烧温度范围内,随着焙烧温度的升高CuO/γ-Al2O3催化剂的活性急剧下降,由XRD物相测定结果可知,归因于对反应表现惰性的尖晶石CuAl2O4相的生成。当焙烧温度为500 ℃时,CeO2的添加对CuO/γ-Al2O3催化剂的活性影响很小；当焙烧温度为800 ℃时,CeO2的添加对CuO/γ-Al2O3催化剂有明显的助催化作用,当Ce和Cu的摩尔比为1∶10时,NO转化率较为理想。     

CrOx-CeO2二元氧化物表面NO的NH3催化还原反应机理

利用原位漫反射红外光谱法研究了473 K下在CrOx-CeO₂二元氧化物表面NO的NH₃催化还原反应的机理。研究了CrO-CeO₂二元氧化物表面在反应过程中的表面吸附物种。为了更加清晰的了解反应过程, 在SCR反应过程中分别切断NH₃和NO的气流, 并采集了所生成的原位漫反射红外光谱图, 通过研究以上结果得出结论:当前状态下的SCR反应过程可能服从E-R机理。     

铁铈复合氧化物催化剂SCR脱硝的改性研究

利用共沉淀法制备了铁铈催化剂,考察添加钛、锆、钨和钼对其SCR脱硝的改性规律。结果表明,钨和钼的添加提高了铁铈催化剂高温脱硝性能,却使其低温活性有所降低;钛的添加对铁铈催化剂脱硝性能具有促进作用,尤其提高了其低温活性,并拓宽了其完全转化温度窗口,为最佳改性物。当钛的物质的量比逐渐由0.10增至0.40,铁铈钛催化剂低温脱硝效率先增大后减小,但其高温脱硝效率逐渐增大至100%,钛的最佳物质的量比为0.15。XRD和N₂吸附分析结果表明,钛能优化铁铈催化剂的孔隙结构,增大其比表面积和比孔容,细化其孔径,并与催化剂中铁、铈氧化物形成良好的固溶体,从而提高了铁铈催化剂的SCR脱硝性能。Fe_0.8Ce_0.05Ti_0.15O_z催化剂在150～400℃取得了高于90%的NO_x转化率。     

用于柴油车尾气消除反应(NH3-SCR)的八元环沸石分子筛研究进展

系统总结了作为柴油车尾气消除反应(NH₃-SCR)催化材料的八元环沸石分子筛(CHA, AEI, RTH)的研究进展, 讨论了不同方法合成的八元环沸石分子筛在NH₃-SCR反应中的性能差异, 并对未来八元环分子筛的发展趋势进行了展望.     

凹凸棒石在烟气SCR脱硝催化反应中的应用研究进展

选择性催化还原脱硝技术作为当前去除NOx的主要手段,该手段的最主要部分为催化剂。在诸多催化剂载体中,凹凸棒石以其独特的天然一维结构、丰富的表面官能团、热稳定性及成型性好等优势脱颖而出。我们综述了近年来以凹凸棒石为载体在SCR脱硝催化剂制备中的应用,并且论述了影响催化剂SCR脱硝性能的主要因素,同时分析了使此类催化剂失活的原因以及失活催化剂的再生方法,并揭示了此类催化剂可能遵循的SCR反应机理,最后对催化剂未来的研究方向进行了展望.     

基于时序逻辑和SCR方法的需求分析方法

以定义事件驱动型系统需求的ＳＣＲ（Ｓｏｆｔｗａｒｅ ＣｏｓｔＲｅｄｕｃｅ）方法和时序逻辑为基础,提出了一种能够根据ＳＣＲ方法与时序逻辑之间的语义联系和时序逻辑的推理能力有效地检查用ＳＣＲ方法定义的事件驱动型系统的需求分析方法．为便于理解,还给出了一个简单的例子来介绍如何分析和检查用ＳＣＲ方法定义的需求的有效性．     

SW-Ⅱ型数显温控XL-Ⅰ箱形高温炉的故障及维修方法

运用电学的基本原理,对数显温控高温炉的故障进行了分析,在实践中总结出各种故障的发生原因、特征现象及解决方法。