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Selective Catalytic Reduction of Nitric Oxide with Hydrogen over Pd Based Catalysts

机译:基于Pd基催化剂的氢气选择性催化还原一氧化氮

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Catalytic reduction of NO with hydrogen in the presence of excess oxygen was studied using Pd-based catalysts. High steady-state conversion of NO ( > 80%) is achieved, using 1%Pd/TiO_2/Al_2O_3 as the catalyst and at temperatures ranging from 140°C to 180°C. The addition of V_2O_5 to this catalyst not only increases the NO conversion, but also widens the reaction temperature window to 250°C. The effects of CO, O_2 and H_2 concentrations on the NO conversion were also investigated. It was found that the reaction order is nearly 1st-order with respect to NO, 0.6 with respect to H_2 and -0.18 with respect to CO. Increasing the O_2 concentration from 2% to 10% gave only a slight decrease in NO conversion. FTIR studies showed that a significant amount of NH_4~+ was formed over the V_2O_5-containing catalyst, during the reaction, at temperatures > 200°C, as compared to almost no NH_4~+ formation over the V_2O_5-free sample. The higher activity of 1%Pd-5%V_2O_5/TiO_2-Al_2O_3 is partly attributed to the in-situ formation of NH_4~+.
机译:使用Pd基催化剂研究了在过量氧存在下氢气的催化还原。使用1%Pd / TiO_2 / Al_2O_3作为催化剂,在140℃至180℃范围内的温度下实现高稳态转化的NO(> 80%)。添加V_2O_5至该催化剂不仅增加了不转化,而且将反应温度窗加宽至250℃。还研究了CO,O_2和H_2浓度对NO转化的影响。发现反应顺序相对于CO的H_2和-0.18相对于NO,0.6几乎是1-10s。增加O_2浓度从2%至10%的浓度没有略微减少,没有转化。 FTIR研究表明,在反应过程中,在温度> 200℃下,在含V_2O_5的催化剂上形成大量的NH_4〜+,与在无V_2O_5的样品上几乎没有NH_4〜+形成。 1%PD-5%V_2O_5 / TiO_2-AL_2O_3的较高活性部分归因于NH_4〜+的原位形成。

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