2022
DOI: 10.1016/j.fuel.2022.124455
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Analytical review of the catalytic cracking of methane

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Cited by 22 publications
(15 citation statements)
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“…The viability of the regeneration step can be observed by analyzing the turnover frequencies of CH 2 CH 2 formation, as shown in Figure c, from which the TOF of ethene is roughly the same order of magnitude than the H 2 TOF at the entire temperature range on N-EDNC and P-EDNC. However, the high temperatures of over 1000 K in which the CMD process is conducted make the catalyst susceptible to coke deposition, leading to the deactivation of the reactive sites. ,,,,, Therefore, we investigated the resistance to coking of the active sites on the EDNCs by evaluating the dehydrogenation from CH 2 * to CH*, as it was shown to be the rate-determining step of the methane decomposition in previous works ,, and is being applied for investigations of carbon formation on the catalysts. Furthermore, the selectivity between CH* and CH 2 * is pointed as crucial for determining the efficiency of the catalytic formation of C2 products .…”
Section: Resultsmentioning
confidence: 99%
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“…The viability of the regeneration step can be observed by analyzing the turnover frequencies of CH 2 CH 2 formation, as shown in Figure c, from which the TOF of ethene is roughly the same order of magnitude than the H 2 TOF at the entire temperature range on N-EDNC and P-EDNC. However, the high temperatures of over 1000 K in which the CMD process is conducted make the catalyst susceptible to coke deposition, leading to the deactivation of the reactive sites. ,,,,, Therefore, we investigated the resistance to coking of the active sites on the EDNCs by evaluating the dehydrogenation from CH 2 * to CH*, as it was shown to be the rate-determining step of the methane decomposition in previous works ,, and is being applied for investigations of carbon formation on the catalysts. Furthermore, the selectivity between CH* and CH 2 * is pointed as crucial for determining the efficiency of the catalytic formation of C2 products .…”
Section: Resultsmentioning
confidence: 99%
“…Metal-based catalysts are the most commonly employed for the CMD process, with nickel- and iron-based catalysts being the most economically viable and possessing high selectivity for hydrogen production. ,,, Carbon-based materials are expected to overcome the rapid deactivation due to coke deposition, which is common among metallic catalysts. ,,, The decomposition of methane at the gas–solid interface can be largely improved by the presence of different surface configurations on the carbon catalyst, such as defects, vacancies and low-coordination sites . In fact, the amount of defects present in the carbon surface is directly correlated to the catalytic activity for CMD, especially in the initial stages of the process .…”
Section: Introductionmentioning
confidence: 99%
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