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Cu/SAPO-34催化剂的NH3-SCO活性及抗水热性能研究

夏福婷 张金辉 杨云汉 杨翠翠 李相华 宋忠贤 张秋林 彭金辉

夏福婷, 张金辉, 杨云汉, 杨翠翠, 李相华, 宋忠贤, 张秋林, 彭金辉. Cu/SAPO-34催化剂的NH3-SCO活性及抗水热性能研究[J]. 燃料化学学报(中英文), 2018, 46(3): 328-336.
引用本文: 夏福婷, 张金辉, 杨云汉, 杨翠翠, 李相华, 宋忠贤, 张秋林, 彭金辉. Cu/SAPO-34催化剂的NH3-SCO活性及抗水热性能研究[J]. 燃料化学学报(中英文), 2018, 46(3): 328-336.
XIA Fu-ting, ZHANG Jin-hui, YANG Yun-han, YANG Cui-cui, LI Xiang-hua, SONG Zhong-xian, ZHANG Qiu-lin, PENG Jin-hui. Catalytic performance and hydrothermal stability of Cu/SAPO-34 catalyst in the selective catalytic oxidation of NH3[J]. Journal of Fuel Chemistry and Technology, 2018, 46(3): 328-336.
Citation: XIA Fu-ting, ZHANG Jin-hui, YANG Yun-han, YANG Cui-cui, LI Xiang-hua, SONG Zhong-xian, ZHANG Qiu-lin, PENG Jin-hui. Catalytic performance and hydrothermal stability of Cu/SAPO-34 catalyst in the selective catalytic oxidation of NH3[J]. Journal of Fuel Chemistry and Technology, 2018, 46(3): 328-336.

Cu/SAPO-34催化剂的NH3-SCO活性及抗水热性能研究

基金项目: 

国家自然科学基金 21567030

  11447191

国家重点基础研究发展规划 973 program

国家重点基础研究发展规划 2014CB643404

云南省科技厅应用基础研究计划青年项目 2013FD033

详细信息
    通讯作者:

    ZHANG Qiu-lin, E-mail: qiulinzhang_kmust@163.com

    PENG Jin-hui, E-mail:jhpeng@kmust.edu.cn

  • 中图分类号: O643.32+2

Catalytic performance and hydrothermal stability of Cu/SAPO-34 catalyst in the selective catalytic oxidation of NH3

Funds: 

The project was supported by the National Natural Science Foundation of China 21567030

The project was supported by the National Natural Science Foundation of China 11447191

the National Program on Key Basic Research Project of China 973 program

the National Program on Key Basic Research Project of China 2014CB643404

Natural Science Fund Item of Yunnan Province 2013FD033

  • 摘要: 采用浸渍法制备了一系列不同铜含量的Cu/SAPO-34催化剂,考察了该系列催化剂上NH3选择性催化氧化反应性能(NH3-SCO)。实验结果表明,10%-Cu/SAPO-34催化剂在300 ℃温度下具有100%的NH3去除率,且其氮气选择性大于90%。与此同时,通过XRD、BET、UV-vis、H2-TPR和XPS等表征分析结果表明,高度分散的CuO是Cu/SAPO-34催化剂的主要活性组分。对10%-Cu/SAPO-34催化剂进行水热处理后,催化剂低温活性明显提高,催化剂的N2选择性在325 ℃急剧下降。这是由于水热处理导致一定数量的铜物种发生迁移并且形成了更稳定的铜物种引起。SAPO-34的骨架结构遭到一定程度的破坏。
  • 图  1  不同催化剂的NH3转化率(a),NO生成量(b), NO2生成量(c),N2O生成量(d)和N2选择性(e)

    Figure  1  NH3 conversion (a), NOproduction (b), NO2production (c), N2Oproduction (d) and N2 selectivity (e) of different catalysts

    图  2  不同催化剂的XRD谱图

    Figure  2  XRD patterns of different catalysts

    图  3  不同催化剂的UV-vis谱图

    Figure  3  UV-vis results of different catalysts

    图  4  不同催化剂的H2-TPR谱图

    Figure  4  H2-TPR profiles of different catalysts

    图  5  新鲜和老化催化剂的NH3转化率、NOx生成量和N2选择性

    Figure  5  NH3 conversion, NOx production and N2 selectivity of catalysts before and after aging

    图  6  水热处理前后催化剂的XRD谱图

    Figure  6  XRD patterns of the catalysts before and after aging

    图  7  水热处理前后Cu/SAPO-34催化剂的Cu 2p XPS

    Figure  7  Cu 2p XPS of Cu/SAPO-34 catalysts before and after hydrothermal aging

    图  8  水热处理前后催化剂的UV-vis谱图

    Figure  8  UV-vis results of the catalysts before and after hydrothermal aging

    图  9  水热处理前后催化剂的H2-TPR谱图

    Figure  9  H2-TPR profiles of the catalysts before and after hydrothermal aging

    表  1  不同催化剂的比表面积和孔容

    Table  1  BET surface area and pore volume of different catalysts

    Sample ABET/(m2·g-1) Pore volume v/(cm3·g-1)
    SAPO-34 210 0.1121
    5%-Cu/SAPO-34 186 0.1437
    10%-Cu/SAPO-34 166 0.1423
    15%-Cu/SAPO-34 158 0.1464
    20%-Cu/SAPO-34 141 0.1135
    25%-Cu/SAPO-34 117 0.1074
    30%-Cu/SAPO-34 128 0.1028
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  • 收稿日期:  2017-09-13
  • 修回日期:  2018-01-19
  • 网络出版日期:  2021-01-23
  • 刊出日期:  2018-03-10

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