4.6 Article

Catalysts Derived from Nickel-Containing Layered Double Hydroxides for Aqueous-Phase Furfural Hydrogenation

Journal

CATALYSTS
Volume 12, Issue 6, Pages -

Publisher

MDPI
DOI: 10.3390/catal12060598

Keywords

nickel catalysts; layered double hydroxides; furfural hydrogenation

Funding

  1. Ministry of Science and Higher Education of the Russian Federation [AAAA-A21-121011490008-3]
  2. Nikolaev Institute of Inorganic Chemistry SB RAS [121031700313-8]

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The changes in the properties and state of nickel in the synthesis of nickel catalysts using NiAl-layered double hydroxides were investigated. It was found that the use of NiAl LDH as the catalyst precursor allows for the obtaining of active dispersed nickel particles, and higher catalyst reduction temperature leads to increased catalyst activity and conversion rate.
Changes in the structural and textural properties of NiAl-layered double hydroxides (LDHs) (with 2-4 molar ratios of metals) and state of nickel that occur in different steps of the synthesis of nickel catalysts were studied using XRD, thermal analysis, TPR, low-temperature nitrogen adsorption, XANES, EXAFS, and electron microscopy methods. Relations between nickel content, catalyst reduction conditions, state of nickel, and its catalytic properties were revealed. It was shown that the use of NiAl LDH as the catalyst precursor even at a high content of active metal allows for the obtaining of the dispersed particles of supported nickel that are active in the aqueous-phase hydrogenation of furfural. The catalyst activity and conversion of furfural were found to increase with elevation of the catalyst reduction temperature and the corresponding growth of the fraction of reduced nickel. However, a lower reduction temperature (500 degrees C) makes it possible to form smaller nickel particles with the size of 4-6 nm, and a high Ni content (Ni:Al = 4) can be used to obtain the active Ni@NiAlOx catalyst. Under mild reaction conditions (90 degrees C, 2.0 MPa), the furfural conversion reached 93%, and furfuryl alcohol was formed with the selectivity of 70%. Under more severe reaction conditions (150 degrees C, 3.0 MPa), complete conversion of furfural was achieved, and cyclopentanol and tetrahydrofurfuryl alcohol were the main hydrogenation products.

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