2022
DOI: 10.1016/j.cej.2022.134946
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Kinetic modelling of the methanol synthesis from CO2 and H2 over a CuO/CeO2/ZrO2 catalyst: The role of CO2 and CO hydrogenation

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Cited by 48 publications
(18 citation statements)
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“…Subsequently, the formed CO could be transferred to the Cu + species and be further hydrogenated to methanol. Their results indicated that both the CO2-to-methanol and RWGS reactions were catalyzed by the Cu 0 species, and this is also confirmed by Kunkes et al [86] Moreover, Poto et al [87] reported that the reaction conditions could affect the reaction mechanism. Particularly, the mechanism via CO* was more favorable with high reaction temperature and high H2/CO2 ratio.…”
Section: Reaction Mechanismmentioning
confidence: 57%
“…Subsequently, the formed CO could be transferred to the Cu + species and be further hydrogenated to methanol. Their results indicated that both the CO2-to-methanol and RWGS reactions were catalyzed by the Cu 0 species, and this is also confirmed by Kunkes et al [86] Moreover, Poto et al [87] reported that the reaction conditions could affect the reaction mechanism. Particularly, the mechanism via CO* was more favorable with high reaction temperature and high H2/CO2 ratio.…”
Section: Reaction Mechanismmentioning
confidence: 57%
“…Although there was good agreement with their experiments, the authors emphasized that more studies were required [6] . Similarly, kinetic models have been widely implemented for studying other chemical processes [7–10] …”
Section: Introductionmentioning
confidence: 89%
“…80 In fact, even when processing a pure feed mixture of H 2 /CO 2 , there is no consensus in the scientific community regarding the main pathway towards methanol, as it seems that CO production can occur in the catalyst bed and be found in the outlet gas. 93 Thus, in practical plants, it is sensible to assume that CO 2 direct hydrogenation (R1) will have some local competition with the RWGS (R2) and CO hydrogenation (R3), which will be heavily influenced by the catalyst characteristics, such as available active sites. 30,80 The CO present in the outlet gas can be recycled back to the reactor inlet, consequently improving the synthesis efficiency, and this needs to be optimized according to the desired feed stoichiometric ratios.…”
Section: E-methanol From Co 2 Capture and Transformation (P1)mentioning
confidence: 99%