<div class="csl-bib-body">
<div class="csl-entry">Sringam, S., Witoon, T., Wattanakit, C., Donphai, W., Chareonpanich, M., Rupprechter, G., & Seubsai, A. (2025). Effect of calcination temperature on the performance of K-Co/Al₂O₃ catalyst for oxidative coupling of methane. <i>Carbon Resources Conversion</i>, <i>8</i>(2), Article 100261. https://doi.org/10.1016/j.crcon.2024.100261</div>
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dc.identifier.uri
http://hdl.handle.net/20.500.12708/216575
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dc.description.abstract
The oxidative coupling of methane (OCM) involves directly converting methane to C2+ hydrocarbons (such as ethylene and ethane) via a reaction with oxygen. This study elucidated the effect of the calcination temperature on the structure and catalytic performance of potassium-doped-cobalt oxide supported on an alumina (K-Co/Al2O3) catalyst for the OCM reaction. The catalyst was highly active at relatively low reactor temperatures (500–640 °C). Four calcination temperatures (400, 500, 600, and 700 °C) were investigated, with the results showing that the calcination temperature strongly affected catalytic properties, such as the crystalline phases, elemental distribution, physical properties, and catalytic basicity, leading to a wide range in catalytic performances. The catalyst calcined at 400 °C was superior among the catalysts, with 8.3 % C2+ yield, 24.8 % C2+ selectivity, and 33.6 % CH4 conversion at 640 °C. Furthermore, the catalyst was robust over 24 h of testing.
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dc.language.iso
en
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dc.publisher
KeAi Communications Co.
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dc.relation.ispartof
Carbon Resources Conversion
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dc.subject
Alumina support
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dc.subject
Calcination temperature
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dc.subject
Cobalt catalyst
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dc.subject
Methane conversion
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dc.subject
Oxidative coupling of methane
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dc.title
Effect of calcination temperature on the performance of K-Co/Al₂O₃ catalyst for oxidative coupling of methane