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Study on Novel SCR Catalysts for Denitration of High Concentrated Nitrogen Oxides and Their Reaction Mechanisms

机译:新型 SCR 催化剂对高浓氮氧化物脱硝及其反应机理的研究

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With the rapid development of industrialization, the emission of nitrogen oxides (NOx) has become a global environmental issue. Uranium is the primary fuel used in nuclear power generation. However, the production of uranium, typically based on the uranyl nitrate method, usually generates large amounts of nitrogen oxides, particularly NO2, with concentrations in the exhaust gas exceeding 10,000 ppm. High concentrations of nitrogen dioxide are also produced during silver electrolysis processing and the treatment of waste electrolyte solutions. Traditional V-W/TiO2 NH3-SCR catalysts typically exhibit high catalytic activity at temperatures ranging from 300 to 400 degrees C, under conditions of low NOx concentrations and high gas hourly space velocity. However, their performance is not satisfying when reducing high concentrations of NO2. This study aims to optimize the traditional V-W/TiO2 catalysts to enhance their catalytic activity under conditions of high NO2 concentrations (10,000 ppm) and a wide temperature range (200-400 degrees C). On the basis of 3 wt Mo/TiO2, various loadings of V(2)O(5 )were selected, and their catalytic activities were tested. Subsequently, the optimal ratios of active component vanadium and additive molybdenum were explored. Simultaneously, doping with WO3 for modification was selected in the V-Mo/TiO2 catalyst, followed by activity testing under the same conditions. The results show that: the NOx conversion rates of all five catalysts increase with temperature at range of 200-400 degrees C. Excessive loading of MoO3 decreased the catalytic performance, with 5 wt being the optimal loading. The addition of WO3 significantly enhanced the low-temperature activity of the catalysts. When the loadings of WO3 and MoO3 were both 3 wt, the catalyst exhibited the best denitrification performance, achieving a NOx conversion rate of 98.8 at 250 degrees C. This catalyst demonstrates excellent catalytic activity in reducing very high concentration (10,000 ppm) NO2, at a wider temperature range, expanding the temperature range by 50 compared to conventional SCR catalysts. Characterization techniques including BET, XRD, XPS, H(2)2-TPR, and NH3-TPD were employed to further study the evolution of the catalyst, and the promotional mechanisms are explored. The results revealed that the proportion of chemisorbed oxygen (O-alpha) increased in the WO3-modified catalyst, exhibiting lower V reduction temperatures, which are favorable for low-temperature denitrification activity. NH3-TPD experiments showed that compared to MoOx species, surface WOx species could provide more acidic sites, resulting in stronger surface acidity of the catalyst.
机译:随着工业化的快速发展,氮氧化物 (NOx) 的排放已成为全球环境问题。铀是核能发电中使用的主要燃料。然而,铀的生产通常基于硝酸铀酰法,通常会产生大量的氮氧化物,特别是 NO2,废气中的浓度超过 10,000 ppm。在银电解加工和废电解质溶液的处理过程中,也会产生高浓度的二氧化氮。传统的 V-W/TiO2 NH3-SCR 催化剂通常在 300 至 400 摄氏度的温度范围内、低 NOx 浓度和高气体每小时空速条件下表现出高催化活性。然而,在减少高浓度的 NO2 时,它们的性能并不令人满意。本研究旨在优化传统的 V-W/TiO2 催化剂,以提高其在高 NO2 浓度 (10,000 ppm) 和宽温度范围 (200-400 °C) 条件下的催化活性。在 3 wt% Mo/TiO2 的基础上,选择了不同负载量的 V(2)O(5 ),并测试了它们的催化活性。随后,探索了活性成分钒和添加钼的最佳比例。同时,在 V-Mo/TiO2 催化剂中选择 WO3 掺杂进行改性,然后在相同条件下进行活性测试。结果表明:在 200-400 °C 范围内,所有 5 种催化剂的 NOx 转化率都随温度的增加而增加,MoO3 的过量负载降低了催化性能,5 wt% 是最佳负载。WO3 的添加显著提高了催化剂的低温活性。当 WO3 和 MoO3 的负载量均为 3 wt% 时,催化剂表现出最佳的脱硝性能,在 250 °C 时实现了 98.8% 的 NOx 转化率。该催化剂在更宽的温度范围内还原极高浓度 (10,000 ppm) 的 NO2 方面表现出优异的催化活性,与传统的 SCR 催化剂相比,温度范围扩大了 50%。采用包括 BET、XRD、XPS、H(2)2-TPR 和 NH3-TPD 在内的表征技术进一步研究催化剂的演变,并探索其促进机制。结果表明,WO3改性催化剂中化学吸附氧(O-α)的比例增加,表现出较低的V还原温度,有利于低温脱硝活性。NH3-TPD 实验表明,与 MoOx 物种相比,表面 WOx 物种可以提供更多的酸性位点,从而导致催化剂的表面酸性更强。

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