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The Role of the Hydrogen Source on the Selective Production of γ‐Valerolactone and 2‐Methyltetrahydrofuran from Levulinic Acid
Author(s) -
Obregón Iker,
Gandarias Inaki,
AlShaal Mohammad G.,
Mevissen Christian,
Arias Pedro L.,
Palkovits Regina
Publication year - 2016
Publication title -
chemsuschem
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 2.412
H-Index - 157
eISSN - 1864-564X
pISSN - 1864-5631
DOI - 10.1002/cssc.201600751
Subject(s) - levulinic acid , catalysis , chemistry , solvent , acetone , inert gas , yield (engineering) , hydrogen , inert , hydrogen production , organic chemistry , transfer hydrogenation , inorganic chemistry , ruthenium , materials science , metallurgy
A mechanistic study of the hydrogenation reaction of levulinic acid (LA) to 2‐methyltetrahydrofuyran (MTHF) was performed using three different solvents under reactive H 2 and inert N 2 atmospheres. Under the applied reaction conditions, catalytic transfer hydrogenation and hydrogenation with molecular H 2 were effective at producing high yields of γ‐valerolactone. However, the conversion of this stable intermediate to MTHF required the combination of both hydrogen sources (the solvent and the H 2 atmosphere) to achieve good yields. The reaction system with 2‐propanol as solvent and Ni–Cu/Al 2 O 3 as catalyst allowed full conversion of LA and a MTHF yield of 80 % after 20 h reaction time at 250 °C and 40 bar of H 2 (at room temperature). The system showed the same catalytic activity at LA feed concentrations of 5 and up to 30 wt%, and also when high acetone concentration at the beginning of the reaction were added, which confirmed the potential industrial applications of this solvent/catalyst system.

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