2021
DOI: 10.1039/d0nj05296e
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The selective conversion of furfuryl alcohol to ethyl levulinate over Zr-modified tungstophosphoric acid supported on β-zeolites

Abstract: Catalysts of zirconium-exchanged proton-containing tungstophosphoric acid (TPA) supported on β-zeolites were prepared by an impregnation method for the selective alcoholysis of furfuryl alcohol into ethyl levulinate.

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Cited by 20 publications
(13 citation statements)
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“…Possible reaction mechanisms for hydrogenation of furfural over metallic sites in the presence of molecular hydrogen as well as hydrogen sacrificial agent, e.g., ethanol, have been proposed earlier. , Similarly, the possible reaction mechanism for the conversion of FA to EL in liquid ethanol is also reported and few reaction pathways through formation of various intermediates were suggested. , Recently, the role of hydrotalcite originated basic sites in the adsorption and activation of the carbonyl group of furfural is reported. The surface basic sites of hydrotalcite-derived mixed oxide in close proximity with active metal sites are capable of having interaction with the π* acceptor orbital of carbonyl group, which consequently leads to the enhanced reactivity of the carbonyl group .…”
Section: Resultsmentioning
confidence: 97%
“…Possible reaction mechanisms for hydrogenation of furfural over metallic sites in the presence of molecular hydrogen as well as hydrogen sacrificial agent, e.g., ethanol, have been proposed earlier. , Similarly, the possible reaction mechanism for the conversion of FA to EL in liquid ethanol is also reported and few reaction pathways through formation of various intermediates were suggested. , Recently, the role of hydrotalcite originated basic sites in the adsorption and activation of the carbonyl group of furfural is reported. The surface basic sites of hydrotalcite-derived mixed oxide in close proximity with active metal sites are capable of having interaction with the π* acceptor orbital of carbonyl group, which consequently leads to the enhanced reactivity of the carbonyl group .…”
Section: Resultsmentioning
confidence: 97%
“…which is characteristic of a Keggin structure. [50][51][52][53][54][55][56][57] The sharp and well-defined nature of the peaks indicates the high crystallinity of the sample. FTIR spectra (Fig.…”
Section: Catalyst Characterisationmentioning
confidence: 99%
“…[15] Acidic mesoporous MIL-101(Cr)À SO 3 H (MMSs) catalyst was also explored for FA ethanolization which results in 83 % EL yield with complete FA conversion at 160°C in 2 h. [16] Hu and coworkers studied effects of the Brønsted and Lewis acid sites of different crystal facets of WO 3 on the catalytic conversion of FA to EL. They achieved highest catalytic activity using (110) faceted strong Brønsted acidic WO 3 catalyst forming 93.3 % of EL at 170°C in 2 h. [17] 20 % Zr0.75TPA/β-zeolite was found to be active for the alcoholysis of FA which gave 96 % yield of EL at 130°C in 5 h. [18] Gu et al developed α, α'-dichloro-p-xylene derived hyper-cross-linked organic carbocatalyst for EL production from FA results in 70.3 % EL yield at 150°C in 2 h. [19] Glucose derived carbon-based solid acid was also tested for EL production to give a yield of 67 % at 110°C. [20] Tian et al prepared sulfonated attapulgite catalyst which yields up to 95.4 % of EL from FA at 160°C in 2 h. [21] AQUIVIONs perfluorosulfonic acid resin yields 82 mol % butyl levulinate from FA.…”
Section: Introductionmentioning
confidence: 98%
“…They achieved highest catalytic activity using (110) faceted strong Brønsted acidic WO 3 catalyst forming 93.3 % of EL at 170 °C in 2 h [17] . 20 % Zr0.75TPA/β‐zeolite was found to be active for the alcoholysis of FA which gave 96 % yield of EL at 130 °C in 5 h [18] . Gu et al.…”
Section: Introductionmentioning
confidence: 99%