2022
DOI: 10.1016/j.jcat.2022.05.001
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On the link between CO surface coverage and selectivity to CH4 during CO2 hydrogenation over supported cobalt catalysts

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Cited by 18 publications
(13 citation statements)
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“…One possibility is incomplete reduction of the carbide surface due to ligand retention, which is supported by the low initial activity and long induction period described above. Additionally, the lack of CO* site density but moderate H* site density suggests that another possibility for the high methane selectivity for the OAm-MoC 1– x /C catalyst is a comparatively high H*/CO x * ratio on this catalyst surface after the induction period, leading to complete hydrogenation to methane. In contrast, the t -BuNH 2 –MoC 1– x /C catalyst reduced at 250 °C exhibited greater CO* site density with a H* site density in the same order-of-magnitude, suggesting a lower H*/CO x * ratio, and subsequently, a lower hydrogenation selectivity to CH 4 . Comparing the selectivity for the t -BuNH 2 -MoC 1– x /C catalyst reduced at 250 °C to both catalysts pretreated at 450 °C revealed similar product slates (Figure S8).…”
Section: Resultsmentioning
confidence: 99%
“…One possibility is incomplete reduction of the carbide surface due to ligand retention, which is supported by the low initial activity and long induction period described above. Additionally, the lack of CO* site density but moderate H* site density suggests that another possibility for the high methane selectivity for the OAm-MoC 1– x /C catalyst is a comparatively high H*/CO x * ratio on this catalyst surface after the induction period, leading to complete hydrogenation to methane. In contrast, the t -BuNH 2 –MoC 1– x /C catalyst reduced at 250 °C exhibited greater CO* site density with a H* site density in the same order-of-magnitude, suggesting a lower H*/CO x * ratio, and subsequently, a lower hydrogenation selectivity to CH 4 . Comparing the selectivity for the t -BuNH 2 -MoC 1– x /C catalyst reduced at 250 °C to both catalysts pretreated at 450 °C revealed similar product slates (Figure S8).…”
Section: Resultsmentioning
confidence: 99%
“…Operando DRIFTS experiments were performed on a modified high-temperature DRIFT cell (from Spectra-Tech, Hong Kong) fitted with CaF 2 windows using a Collector II assembly. A description and properties of the cell can be found in earlier references [28][29][30]. The spectrophotometer used was a Nicolet 8700 (ThermoFischer Scientific, Waltham, MA, USA) fitted with a liquid-N 2 cooled MCT detector.…”
Section: Methodsmentioning
confidence: 99%
“…Using operando IR spectroscopy, they found that the selectivity toward methane is related to the CO* coverage. 410 When shifting from a CO-rich to a CO 2 -rich feed, the CO* coverage decreases and methane selectivity increases. A possible explanation for the increased methane yield is the higher H* coverage when CO* coverage decreases.…”
Section: Co-and Ru-based Co 2 -Ftsmentioning
confidence: 99%
“…On cobalt, high CO partial pressures are necessary to induce chain growth, as shown by DFT calculations by the Saeys group and the Iglesia group and experiments by the Meunier group and the Weststrate group. ,,, While the groups of Iglesia and Saeys mainly focused on CO-FT, the group of Meunier investigated the surface of the cobalt catalysts under CO 2 hydrogenation conditions. Using operando IR spectroscopy, they found that the selectivity toward methane is related to the CO* coverage . When shifting from a CO-rich to a CO 2 -rich feed, the CO* coverage decreases and methane selectivity increases.…”
Section: Co2-fts: Revival Of the Century-old Fischer–tropsch Process?mentioning
confidence: 99%