烧结烟气条件下微波催化直接分解 NO 脱硝试验
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易钰涵(1998—),男,硕士研究生,从事微波催化脱硝的研究。

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TQ46.4;X701.7;O643.36+1

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中国中长石研究发展基金资助项目(2020)CJ02);国家自然科学基金面上项目(22178295)


Research on direct decomposition of NO by microwave catalysis under condition of sintering flue gas
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    摘要:

    复杂烧结烟气条件下,实现低温高效直接分解 NO 具有极大挑战性。在低温过量 O2 且含 SO2 和 CO2 气氛下,本文通过研制 GeO2/MgCo2O4-40% BaCO3 催化剂用于微波催化高效直接分解 NO,并考察该催化剂的脱硝和抗硫性能;通过 XRD 和 TEM 表征分析催化剂失活以及改性后活性得到改善的原因。结果表明:当进气气体中 CO2 体积分数为 5% 时,该微波催化剂的脱硝率几乎保持不变;引入 GeO2 后,该微波催化剂的抗硫性能明显提升,在 SO2 体积分数为 0.1% 气氛下,当反应温度仅为 250 ℃时,该微波催化剂可实现 99.9% 的 NO 转化率和 99.9% 的 N2 选择性;TEM 结果表明,反应前后,该催化剂的形貌特征无明显差异。本文建立的微波催化直接分解 NO 的脱硝新方法,可为复杂烧结烟气条件下绿色深度脱硝提供新途径。

    Abstract:

    It is a great challenge to realize direct decomposition of NO at low temperature and high efficiency under complex sintering flue gas conditions. A GeO2/MgCo2O4 - 40% BaCO3 catalyst is developed for the efficient direct decomposition of NO in microwave catalysis under the condition of low temperature with excess O2 and some SO2 and CO2, and then the denitration performance and sulfur resistance of the catalyst are investigated. XRD and TEM characterization are used to analyze the catalyst deactivation and the reason for the improvement of the deactivation after modification. The results show that the denitrification rate of the microwave catalyst is almost stable when the volume fraction of CO2 in the inlet gas is 5%. After GeO2 is introduced, the sulfur resistance of the microwave catalyst is obviously improved. Under the atmosphere of 0.1% SO2 volume fraction and the reaction temperature is only 250 ℃, the microwave catalyst can achieve 99.9% NO conversion and 99.9% N? selectivity. TEM results show that there is no obvious difference in the topography features of the catalyst before and after the reaction. The new denitration method of direct decomposition of NO by microwave catalysis established in this paper can provide a new way for green deep denitration under complex flue gas condition.

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易钰涵,康建刚,余春沐,杨本涛,魏进超,周继承,徐文涛.烧结烟气条件下微波催化直接分解 NO 脱硝试验[J].烧结球团,2024,(2):99-106

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  • 最后修改日期:2023-02-10
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  • 在线发布日期: 2026-08-24
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