4.7 Article

Ni-Based Hydrotalcite (HT)-Derived Cu Catalysts for Catalytic Conversion of Bioethanol to Butanol

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MDPI
DOI: 10.3390/ijms241914859

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Ni-based hydrotalcite; biomass conversion; support effect; selectivity; stability

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The catalytic conversion of biomass-derived ethanol into n-butanol through Guerbet coupling reaction has attracted significant attention. In this study, a series of supported Cu catalysts were prepared and tested, and Cu/NiAlOx showed the best performance in terms of butanol selectivity and catalyst stability.
Catalytic conversion of biomass-derived ethanol into n-butanol through Guerbet coupling reaction has become one of the key reactions in biomass valorization, thus attracting significant attention recently. Herein, a series of supported Cu catalysts derived from Ni-based hydrotalcite (HT) were prepared and performed in the continuous catalytic conversion of ethanol into butanol. Among the prepared catalysts, Cu/NiAlOx shows the best performance in terms of butanol selectivity and catalyst stability, with a sustained ethanol conversion of similar to 35% and butanol selectivity of 25% in a time-on-stream (TOS) of 110 h at 280 C-degrees. While for the Cu/NiFeOx and Cu/NiCoOx, obvious catalyst deactivation and/or low butanol selectivity were obtained. Extensive characterization studies of the fresh and spent catalysts, i.e., X-ray diffraction (XRD), Transmission electron microscopy (TEM), X-ray photoelectron spectroscopy (XPS) and Hydrogen temperature-programmed reduction (H-2-TPR), reveal that the catalysts' deactivation is mainly caused by the support deconstruction during catalysis, which is highly dependent on the reducibility. Additionally, an appropriate acid-base property is pivotal for enhancing the product selectivity, which is beneficial for the key process of aldol-condensation to produce butanol.

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