Study on the preparation of Cu/ZnO catalyst by sol–gel auto-combustion method and its application for low-temperature methanol synthesis
[Display omitted] ► For the first time, a novel sol–gel auto-combustion method was proposed to prepare the metal and metallic oxide catalyst (Cu/ZnO) without additional reduction. ► Cu particle size was strongly influenced by the initial M/CA molar ratio. ► More carbon residues were left with the in...
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Veröffentlicht in: | Applied catalysis. A, General General, 2011-07, Vol.401 (1), p.46-55 |
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Sprache: | eng |
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► For the first time, a novel sol–gel auto-combustion method was proposed to prepare the metal and metallic oxide catalyst (Cu/ZnO) without additional reduction. ► Cu particle size was strongly influenced by the initial M/CA molar ratio. ► More carbon residues were left with the increased citric acid amount. ► The methanol selectivity increased with the decreased Cu particle size.
A series of the as-burnt and the burnt Cu/ZnO catalysts were prepared by a sol–gel auto-combustion method using metal nitrates with the mole ratio of Cu/Zn
=
1/1 (noted as M, M
=
Cu
+
Zn) and citric acid (noted as CA). When the xerogels were burnt in the argon atmosphere, H
2 and CH
4 which were came from the decomposition of the citric acid, were the reducing agents and were used in the redox process for synthesizing metallic Cu from Cu
2+ in the chelated compound. The XRD patterns revealed that all the as-burnt catalysts with different M/CA molar ratios were converted into pure Cu and ZnO species. TPR analysis of the as-burnt catalyst illustrated that almost no hydrogen was consumed. It proved that Cu
2+ in the chelated compound was absolutely reduced to metallic Cu in the as-burnt catalyst. The effects of M/CA molar ratio on the properties of catalysts were studied by TG-DTA, FT-IR, Raman spectrum, XRD, SEM-EDS, BET, and N
2O chemisorption techniques. The activity of the as-burnt catalysts without reduction was investigated for low-temperature methanol synthesis from syngas containing CO
2 using ethanol as a promoter at 443
K and 5.0
MPa for 12
h. The total carbon conversion increased with increasing the content of citric acid and reached a maximum for the as-burnt Cu/ZnO catalyst C
0.8 with M/CA
=
1/0.8, and then decreased. The variation trend was in accordance with that of the copper (Cu
0) surface area. Comparing with the burnt catalyst C
0.8-air after reduction, the methanol selectivity of the as-burnt Cu/ZnO catalyst was much lower owing to lower hydrogenation activity of the ethyl formate. The as-burnt catalyst C
0.8 was also used in continuous low-temperature methanol synthesis at 443
K and 5.0
MPa for 40
h. The total carbon conversion was stable after 15
h and no obvious deactivation during 40
h reaction, but the methanol selectivity was still not high. |
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ISSN: | 0926-860X 1873-3875 |
DOI: | 10.1016/j.apcata.2011.04.043 |