2015
DOI: 10.1002/cssc.201403392
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In Situ Catalytic Hydrogenation of Biomass‐Derived Methyl Levulinate to γ‐Valerolactone in Methanol

Abstract: In this work, the hydrocyclization of methyl levulinate (ML) to γ-valerolactone (GVL) was performed in MeOH over an in situ prepared nanocopper catalyst without external H2 . This nanocopper catalyst served as a dual-functional catalyst for both hydrogen production by MeOH reforming and hydrogenation of ML. Nearly quantitative ML conversion with a GVL selectivity of 87.6 % was achieved at 240 °C in 1 h in MeOH under a nitrogen atmosphere. ML in the methanolysis products of cellulose also could be hydrogenated … Show more

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Cited by 61 publications
(41 citation statements)
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“…When the reaction was conducted at 200°C for 1 h, a X ML of only 10.2% with a S GVL of 96.5% was obtained (Table , entry 4). The low X ML is mainly ascribed to insufficient H 2 supply by MeOH reforming and/or inferior ML hydrogenation at a relatively low temperature . Moreover, almost no by‐products from the hydrocarboxylation of GVL were detected in this case.…”
Section: Resultsmentioning
confidence: 78%
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“…When the reaction was conducted at 200°C for 1 h, a X ML of only 10.2% with a S GVL of 96.5% was obtained (Table , entry 4). The low X ML is mainly ascribed to insufficient H 2 supply by MeOH reforming and/or inferior ML hydrogenation at a relatively low temperature . Moreover, almost no by‐products from the hydrocarboxylation of GVL were detected in this case.…”
Section: Resultsmentioning
confidence: 78%
“…However, no detectable MHP intermediate could be observed, indicating that the reduction of ML to MHP is the rate‐determing step and the intramolecular transesterification of MHP to GVL is a fast step under the conditions applied in this study . Besides the main product GVL, small amount of by‐products could form through the hydrocarboxylation/alkoxycarbonylation of GVL with CO 2 in MeOH followed by hydrogenation (Scheme ) …”
Section: Resultsmentioning
confidence: 86%
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“…2.5‐15 MPa), followed by acid/base‐mediated lactonization can afford GVL with reduced oxygen content . To increase the economic benefit of the catalytic process, some efforts have been made on the development of non‐noble metal particles (e. g., Ni, Cu and Co) and even transition metal oxides (e. g., ZrO 2 , ZrNi, TiZr, and ZrFeO x ) for the selective conversion of levulinates to GVL in good yields by using formic acid or alcohol as hydrogen‐donor (H‐donor) . The synergistic effect of Lewis acid‐base pair sites is verified to be responsible for achieving the high efficiency in the production of GVL from alkyl levulinates in alcohol via cascade Meerwein‐Ponndorf‐Verley (MPV) reduction and lactonization ,.…”
Section: Introductionmentioning
confidence: 99%
“…For example, diphenolic acid, synthesized by the condensation of LA with phenols, has been envisaged as a desirable substitute for 4,4′‐(propane‐2,2‐diyl)diphenol in the polycarbonate and epoxy‐resin industries . Similarly, methyl levulinate (ML) has found application in the synthesis of γ‐valerolactone, which is used as a solvent and an alternative fuel additive . Furthermore, ethyl levulinate (EL) is considered as a new biobased diluent for biodiesel owing to its high saturated fatty acid content …”
Section: Introductionmentioning
confidence: 99%