纳米CeO2催化剂对柴油机碳烟颗粒和NO降低效果

    Reducing soot and NO emission from diesel engine exhaust catalyzed by nano-CeO2

    • 摘要: 为采取后处理技术同时控制柴油机颗粒(PM)和一氧化氮(NO)排放,该研究采用沉淀法制备了3组纳米二氧化铈(CeO2)催化剂,通过X射线衍射(XRD)法、BET法测比表面积与孔径、氢气程序升温还原法(H2-TPR)对其性能进行表征,并利用碳烟起燃温度和峰值温度以及NO向N2的转化率分别对催化剂进行活性评价。试验结果表明:3组制备的CeO2催化剂平均粒径依次为7、12和20 nm,明显小于商业级CeO2;自制CeO2相较于商业级CeO2具有较大的比表面积,且比表面积越大催化活性越高;自制的CeO2有3个较明显的H2还原峰,依次对应表面吸附氧、表面晶格氧以及体相晶格氧;CeO2对碳烟颗粒催化氧化的效率由高到低依次为20、12和7 nm,这3组CeO2催化剂较未添加催化剂时起燃温度依次降低了124,109,93 ℃,峰值温度依次降低了185,104,102 ℃;CeO2对NO转化率最高可以达到70%,且温度窗口比较宽。研究结果对CeO2在排放后处理领域的应用具有指导意义。

       

      Abstract: Abstract: Nitrogen oxide (NOx) and particulate matter (PM) are the main emissions for diesel engines. Because of their contradictory relationship of generation mechanisms, only using the internal purification technology is very difficult to meet the increasingly stringent diesel emissions regulations. Development and application of after-treatment technology with low cost, high efficiency and high adaptability will be more promising, which should be utilized to control both NOx and PM emissions. Rare-earth-based catalysts have rich electronic structure, and show the unique physical and chemical properties. In existing rare earth oxides, cerium oxide has been paid much attention in the field of catalysis because of its low price, unique crystal structure and reversible transformation of trivalent ion (Ce3+) and tetravalent ion (Ce4+). In the recent years, the application of cerium dioxide (CeO2) in after-treatment technology for diesel engine is a hot research topic. In this study, 3 groups of nano-CeO2 were prepared using the coprecipitation method in order to reduce the PM and NOx emissions from diesel engine through the after-treatment technology. The samples were characterized by X-ray diffraction (XRD), Brunauer-Emmett-Teller (BET), and hydrogen temperature programmed reduction (H2-TPR). What was more, the activity of catalysts was evaluated by ignition temperature and peak temperature of soot combustion as well as conversion ratio from nitric oxide (NO) to nitrogen (N2). The experimental results showed that CeO2 crystal structure had not been changed, and continued to be the cubic fluorite structure. The average particle diameters of the prepared CeO2 were 7, 12 and 20 nm, respectively, which were much smaller than that of commercial CeO2. Compared with commercial CeO2, the prepared CeO2 had larger specific surface area, which indicated that there were more active sites on the surface of CeO2 for the unit mass. Furthermore, there were more opportunities for the catalyst to be exposed to the reactants, which was beneficial for adsorption and activation of the reactant molecules. The prepared CeO2 had 3 obvious H2 reduction peaks, corresponding to the surface absorbed oxygen, surface lattice oxygen and bulk lattice oxygen, respectively. Oxygen species, especially the surface lattice oxygen, had direct relation with catalytic activity. The reduction property of surface oxygen species was stronger, and the catalytic activity was higher. The results of H2-TPR had correspondence with the results of BET. For the efficiency of catalytic oxidation, the order of nano-CeO2 particle size from high to low was 20, 12 and 7 nm, successively. The ignition temperatures of soot combustion were reduced by 124, 109 and 93 ℃, and the peak temperatures were reduced by 185, 104 and 102 ℃ respectively with the 3 groups of CeO2 catalysts. With the increase of temperature, the conversion ratio of NO firstly increased and then decreased. The conversion ratio of NO with 20 nm CeO2 reached the highest value of 70% at 350 ℃. The conversion ratio of the 3 groups of CeO2 catalysts was higher than 68% at 400-520 ℃, which indicated that CeO2 has a wide temperature window. The experimental results can provide a reference for optimum design and application of CeO2 catalyst in the field of diesel exhaust after-treatment system.

       

    /

    返回文章
    返回