2020
DOI: 10.1007/s10563-020-09293-6
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Preparations and Characterization on Fe Based Catalyst Supported on Coconut Shell Activated Carbon CS(AC) and SCR of NOx-HC

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Cited by 16 publications
(8 citation statements)
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“…60 In the literature on the preparation and application of Fe/AC, the same results were obtained, where the characteristic peaks of Fe were not detected in the XRD patterns for low Fe loading, but when the loading was large enough, the presence of Fe was detected in the form of Fe 2 O 3 . 69,70 Combined with the XPS characterization results, we concluded that Fe 2 O 3 was predominantly present in our catalyst, along with Fe carbide.…”
Section: Resultssupporting
confidence: 59%
“…60 In the literature on the preparation and application of Fe/AC, the same results were obtained, where the characteristic peaks of Fe were not detected in the XRD patterns for low Fe loading, but when the loading was large enough, the presence of Fe was detected in the form of Fe 2 O 3 . 69,70 Combined with the XPS characterization results, we concluded that Fe 2 O 3 was predominantly present in our catalyst, along with Fe carbide.…”
Section: Resultssupporting
confidence: 59%
“…The peaks located at 1443 and 1601 cm −1 are assigned to pyridine adsorbed on Lewis (L) acid sites, while the peak centered at 1540 cm −1 is associated with pyridine adsorbed on Brønsted (B) acid sites 34 . The other peak at 1490 cm −1 is related to the pyridine co‐adsorbed on both Lewis and Brønsted acid sites 35,36 . For a better comparison, the amount of Brønsted acid sites is computed based on the peak area of 1540 cm −1 and the Lewis acid sites are evaluated based on the peak area of 1443 cm −1 .…”
Section: Resultsmentioning
confidence: 99%
“…34 The other peak at 1490 cm −1 is related to the pyridine co-adsorbed on both Lewis and Brønsted acid sites. 35,36 For a better comparison, the amount of Brønsted acid sites is computed based on the peak area of 1540 cm −1 and the Lewis acid sites are evaluated based on the peak area of 1443 cm −1 . It is found that the B/L ratio at 150 °C is 0.22 and 0.17 for the Fe-Ce (S) and Fe(S)-Ce catalysts, respectively, and the value is 0.28 and 0.18 at 250 °C, indicating that Fe-Ce(S) contains a much higher B/L ratio than Fe(S)-Ce.…”
Section: Py-ir Analysismentioning
confidence: 99%
“…In particular, the valence state of Mn-based catalysts is variable and the redox ability is superb, which display good denitration ability. However, when the flue gas contains SO 2 and H 2 O, the denitration activity of catalysts decreases greatly [31][32][33]. For example, the actual sintering flue gas contains about 10-13% water vapor and 300-1500 mg/Nm 3 SO 2 [34].…”
Section: Introductionmentioning
confidence: 99%