2018
DOI: 10.1016/j.cattod.2017.07.028
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Dynamic chemical state conversion of nickel species supported on silica under CO–NO reaction conditions

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Cited by 3 publications
(3 citation statements)
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“…Meanwhile, N 2 selectivity was calculated and is shown in Figure b. The formation of N 2 O from the side reaction (CO + 2NO → N 2 O + CO 2 ) has been identified for the CO–NO reaction in the absence of O 2 . At 250–300 °C, it was noted that higher N 2 selectivity was achieved over CoCeO x -TA and CoCeO x -SS catalysts than over the CoCeO x -SA catalyst.…”
Section: Resultsmentioning
confidence: 96%
See 1 more Smart Citation
“…Meanwhile, N 2 selectivity was calculated and is shown in Figure b. The formation of N 2 O from the side reaction (CO + 2NO → N 2 O + CO 2 ) has been identified for the CO–NO reaction in the absence of O 2 . At 250–300 °C, it was noted that higher N 2 selectivity was achieved over CoCeO x -TA and CoCeO x -SS catalysts than over the CoCeO x -SA catalyst.…”
Section: Resultsmentioning
confidence: 96%
“…The formation of N 2 O from the side reaction (CO + 2NO → N 2 O + CO 2 ) has been identified for the CO−NO reaction in the absence of O 2 . 22 At 250−300 °C, it was noted that higher N 2 selectivity was achieved over CoCeO x -TA and CoCeO x -SS catalysts than over the CoCeO x -SA catalyst. Because limited NO x conversion was observed over CoCeO x -SA and CoCeO x -OA catalysts, N 2 selectivity was not calculated at 150−200 and 350−400 °C.…”
Section: Resultsmentioning
confidence: 99%
“…Liu et al [190] prepared Cu 0.1 La 0.1 Ce 0.8 O catalyst, which had good water resistance and catalytic stability in CO-SCR process. Yamashita et al [199] studied the CO-SCR reaction of nickel species supported on silica. Yao et al [200] discussed the mechanism of CeO 2 modified MnO x catalyst at low temperature (Figure 12a).…”
Section: Co-scrmentioning
confidence: 99%