کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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61709 | 47600 | 2010 | 8 صفحه PDF | دانلود رایگان |
Catalytic hydrogenation of CO2 to valuable chemicals or liquid fuels is a promising way to recycle and utilize CO2. In the present study, elementary steps leading to the formation of formate and CO, two important intermediates in CO2 hydrogenation on Ni/γ-Al2O3, have been explored using the density functional theory (DFT) slab calculations. Two systems: Ni4 cluster supported on the dry γ-Al2O3(1 1 0) surface, D(Ni4), and on the hydroxylated γ-Al2O3(1 1 0) surface, H(Ni4), have been used to model Ni/γ-Al2O3. On D(Ni4), the reaction energy and activation barrier for formate formation are −0.23 eV and 1.25 eV, respectively, whereas those for CO formation are −0.48 eV and 2.13 eV, respectively. As such, formate formation is preferred kinetically while CO formation is more facile thermodynamically. On H(Ni4), the reaction energy and activation barrier for formate formation are −0.36 eV and 2.32 eV, respectively, whereas those for CO formation are −0.67 eV and 0.69 eV, respectively. Consequently, CO formation becomes more favorable both kinetically and thermodynamically. These results indicate that hydroxylation of the γ-Al2O3 support alters the pathway, and ultimately, the selectivity of CO2 hydrogenation on Ni/γ-Al2O3. This conclusion supports the fact that varying the reaction environment such as water partial pressure is often used to improve the selectivity of a reaction.
Hyroxylation of the γ-Al2O3 support alters the preference of CO2 hydrogenation from formate to CO over the Ni/γ-Al2O3 catalystFigure optionsDownload high-quality image (39 K)Download as PowerPoint slide
Journal: Journal of Catalysis - Volume 272, Issue 2, 15 June 2010, Pages 227–234