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Levulinic Acid as a Catalyst for the Production of 5‐Hydroxymethylfurfural and Furfural from Lignocellulose Biomass

Bhogeswararao Seemala, Victoria S. Haritos, Akshat Tanksale

Open publisher page 63 citations

Abstract

Abstract Levulinic acid (LA) was used as a catalyst for the first time to produce 5‐hydroxymethylfurfural (5‐HMF) and furfural (FAL) from pinewood and eucalyptus sawdust in a mono‐ or biphasic solvent system. 2‐Methyltetrahydrofuran was used as a co‐solvent with water in different ratios and temperatures (140–200 °C). Highest yields of 5‐HMF and FAL were obtained at 180 °C and 2 h reaction time; however, at 160 °C, high yields of C6 and C5 sugars were obtained. Both hydrolysis and dehydration steps were accelerated in the MTHF/water biphasic system compared to pure aqueous phase. In particular, 1:2 w/w ratio of MTHF/water resulted in the highest yield of 5‐HMF and FAL, whereas 2:1 w/w ratio showed highest yield of C6 and C5 sugars. Increasing the ratio of MTHF/water resulted in a higher fraction of dehydrated products extracted into the organic phase. LA as a catalyst is beneficial because it is miscible in both the phases and the presence of LA favours the equilibrium towards 5‐HMF production.

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What this paper is about

Abstract Levulinic acid (LA) was used as a catalyst for the first time to produce 5‐hydroxymethylfurfural (5‐HMF) and furfural (FAL) from pinewood and eucalyptus sawdust in a mono‐ or biphasic solvent system. 2‐Methyltetrahydrofuran was used as a co‐solvent with water in different ratios and temperatures (140–200 °C). Highest yields of 5‐HMF and FAL were obtained at 180 °C and 2 h reaction time; however, at 160 °C, high yields of C6 and C5 sugars were obtained. Both hydrolysis and dehydration steps were accelerated in the MTHF/water biphasic system compared to pure aqueous phase. In particular, 1:2 w/w ratio of MTHF/water resulted in the highest yield of 5‐HMF and FAL, whereas 2:1 w/w ratio showed highest yield of C6 and C5 sugars. Increasing the ratio of MTHF/water resulted in a higher fraction of dehydrated products extracted into the organic phase. LA as a catalyst is beneficial because it is miscible in both the phases and the presence of LA favours the equilibrium towards 5‐HMF production.

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Available abstract

Abstract Levulinic acid (LA) was used as a catalyst for the first time to produce 5‐hydroxymethylfurfural (5‐HMF) and furfural (FAL) from pinewood and eucalyptus sawdust in a mono‐ or biphasic solvent system. 2‐Methyltetrahydrofuran was used as a co‐solvent with water in different ratios and temperatures (140–200 °C). Highest yields of 5‐HMF and FAL were obtained at 180 °C and 2 h reaction time; however, at 160 °C, high yields of C6 and C5 sugars were obtained. Both hydrolysis and dehydration steps were accelerated in the MTHF/water biphasic system compared to pure aqueous phase. In particular, 1:2 w/w ratio of MTHF/water resulted in the highest yield of 5‐HMF and FAL, whereas 2:1 w/w ratio showed highest yield of C6 and C5 sugars. Increasing the ratio of MTHF/water resulted in a higher fraction of dehydrated products extracted into the organic phase. LA as a catalyst is beneficial because it is miscible in both the phases and the presence of LA favours the equilibrium towards 5‐HMF production.

Key concepts: Levulinic acid, Furfural, Hydroxymethylfurfural, Chemistry, Catalysis, Yield (engineering), Solvent, Hydrolysis

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Levulinic Acid as a Catalyst for the Production of 5‐Hydroxymethylfurfural and Furfural from Lignocellulose Biomass — Research Paper | ScholarLens