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The influence of Mg/Al molar ratio on the performance of CuMgAl-x catalysts for CO2 hydrogenation to methanol
The CuMgAl-x catalysts derived from hydrotalcite precursors with different Mg/Al molar ratios were synthesized and applied to CO 2 hydrogenation to methanol reaction. In this study, the effects of Mg/Al molar ratio on the structure and surface properties of CuMgAl-x catalysts were investigated by XR...
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Published in: | Frontiers in chemistry 2024-03, Vol.12, p.1361930-1361930 |
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Main Authors: | , , , , , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites |
Online Access: | Get full text |
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Summary: | The CuMgAl-x catalysts derived from hydrotalcite precursors with different Mg/Al molar ratios were synthesized and applied to CO
2
hydrogenation to methanol reaction. In this study, the effects of Mg/Al molar ratio on the structure and surface properties of CuMgAl-x catalysts were investigated by XRD, N
2
adsorption-desorption, SEM, TEM, H
2
-TPR, CO
2
-TPD, XPS, and
in situ
DRIFTS characterization methods. The results showed that an appropriate Mg/Al molar ratio can enhance the Cu-MgO interaction, increasing the basic sites and obtaining suitable acid sites. The dispersion of active Cu on the CuMgAl-x catalysts can be improved by strong Cu-MgO interaction, which enhances the adsorption capacity of CO
2
and makes H
2
activation easier, accelerates the conversion of intermediate species CO
3
*
and HCO
3
*
to HCOO
*
, and facilitates further conversion to CH
3
O
*
and CH
3
OH. The strong interaction between Cu and MgO was conducive to the formation of Cu
+
, which can inhibit the desorption of CO in the reverse water gas shift reaction. The CuMgAl-3 catalyst showed the highest CO
2
Conversion rate (14.3%), methanol selectivity (94.5%), and STY of methanol (419.3 g⋅kg
cat.
−1
⋅h
−1
) at 240°C and 2.5 MPa. The results obtained in this paper can provide a new idea for the design of high-performance catalysts for CO
2
hydrogenation to methanol. |
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ISSN: | 2296-2646 2296-2646 |
DOI: | 10.3389/fchem.2024.1361930 |