4.7 Article

Highly efficient Pd-doped ferrite spinel catalysts for the selective catalytic reduction of NO with H2 at low temperature

期刊

CHEMICAL ENGINEERING JOURNAL
卷 289, 期 -, 页码 231-238

出版社

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2015.12.085

关键词

NOx; Hydrogen; SCR; Flue gas; Ferrite spinel

资金

  1. National Natural Science Foundation of China [21277045]
  2. Ministry of Environmental Protection [201309021]
  3. Shu Guang Project of the Shanghai Municipal Education Commission
  4. Shanghai Education Development Foundation
  5. Fundamental Research Funds for the Central Universities

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Palladium-doped ferrite spinels with various divalent metals (Co, Cu or Zn) were prepared using the sol-gel auto-ignition method for use in the selective catalytic reduction of NO with hydrogen (H-2-SCR). The activity of the Co-FePd catalyst was greatly enhanced by adding a small amount of palladium and resulted in approximately 96% NO conversion in the 170-250 degrees C range. In TPD and TPR analyses, Co-FePd exhibited a larger peak area and a lower reductive temperature than the other studied materials, indicating that this catalyst possesses stronger reduction ability and larger acidity; these properties were very important for the catalytic performance of Co-FePd, which showed the best SCR activity of the tested materials. The catalytic activities ranked in the following order: Co-FePd > Zn-FePd > Cu-FePd. Adding H2O to the reacting gas mixture slightly decreased NO conversion by the Co-FePd oxide. When the H2O content was increased from 3% to 5%, no further decline of NO conversion occurred. The presence of 100 ppm SO2 in the gas phase decreased the SCR activity of Co-FePd by approximately 19%, but no further deactivation was observed when the concentration was increased to 150 ppm. When SO2 was removed from the feed stream, NO conversion recovered rapidly; however, the conversion was not restored to the original level, indicating that SO2 has both a reversible and an irreversible effect on the H-2-SCR reaction. (C) 2016 Elsevier B.V. All rights reserved.

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