کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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55739 | 47063 | 2011 | 6 صفحه PDF | دانلود رایگان |
The selective catalytic oxidation of hydrogen sulfide to elemental sulfur in a continuous-flow fixed-bed reactor was studied over V2O5-supported Fe-pillared clay (V/Fe-PILC) catalysts. The synthesized catalysts were characterized by X-ray diffraction (XRD), surface area–pore volume measurements, chemical analysis, X-ray photoelectron spectroscopy (XPS), temperature-programmed desorption of ammonia (NH3-TPD), and thermogravimetric (TG) analysis. The reaction tests were conducted at temperatures ranging from 220 to 300 °C. The V/Fe-PILC catalysts exhibited very good catalytic performance toward H2S oxidation at 220–300 °C without much SO2 emission. The H2S conversion over V/Fe-PILC increased with increasing vanadia content up to 7 wt.%. This superior catalytic performance might be related to the uniform dispersion of vanadia species on the Fe-PILC support.
The catalytic performance of vanadia-supported Fe-pillared clay (V/Fe-PILC) catalysts was studied for the selective oxidation of H2S.Figure optionsDownload high-quality image (146 K)Download as PowerPoint slideHighlights
► Development of efficient vanadia-supported Fe-pillared clay (V/Fe-PILC) catalyst for the selective catalytic oxidation of H2S.
► Characterization of the catalysts using various techniques.
► V/Fe-PILC catalysts showed very good catalytic performance toward H2S oxidation at 220–300 °C.
► High selectivity for elemental sulfur.
Journal: Catalysis Today - Volume 175, Issue 1, 25 October 2011, Pages 183–188