4.7 Article

Selective hydrogenation of furfural to tetrahydrofurfuryl alcohol in 2-butanol over an equimolar Ni-Cu-Al catalyst prepared by the co-precipitation method

期刊

ENERGY CONVERSION AND MANAGEMENT
卷 265, 期 -, 页码 -

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.enconman.2022.115736

关键词

Biomass; bimetallic NiCu-Al catalysts; Hydrogenation of furfural; Tetrahydrofurfuryl alcohol

资金

  1. JICA IITH-FRIENDSHIP, Japan [D1956755]
  2. Strategic International Research Cooperative Program, Japan Science and Technology Agency (JST)

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Synthesizing suitable non-precious bimetallic catalysts is of great significance for upgrading biomass-derived chemicals. The study found that Ni-Cu alloy catalysts exhibited high activity, and the equimolar catalysts could achieve high yields of tetrahydrofurfuryl alcohol under appropriate conditions. Reaction pressure, temperature, and solvent selection have a significant impact on product yield and selectivity.
In order to upgrade biomass-derived platform chemicals to high value-added chemicals and liquid fuels, it is highly advantageous and desirable to synthesize suitable non-precious bimetallic catalysts that are efficient and versatile in chemical reactions. Equal moles of Ni and Cu were dispersed on varying mole ratios of Al by the co-precipitation method to synthesize Ni-Cu alloy particles to obtain a maximum yield of tetrahydrofurfuryl alcohol (THFA) by the liquid phase hydrogenation of furfural. The nickel species were active for both the furan ring (C=C) and carbonyl group (C=O) of furfural molecule, while Cu species were highly active for only the carbonyl group of furfural molecule. Systematic characterization of the prepared catalysts by XRD, TPR, STEM-EDS, and XPS analysis revealed the formation of highly active Ni-Cu alloys and near-equal Ni/Cu surface contents were achieved for the equimolar catalyst, which showcased a maximum of 98 mol% yield of THFA at 140 ?C, 30 bar, 4 h. The reaction pressure and temperature showed a substantial effect on the product yield. The solvent selection also influenced the product selectivity, particularly with 2-butanol, which promoted the reaction with its hydrogen donor capacity and supported the ring hydrogenation of FAL to THFA. Moreover, the reduced Ni1Cu1-Al1 catalyst displayed good recyclability for three runs and an equal activity to that of a fresh catalyst after the regeneration.

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