1 research outputs found
Efficient Conversions of Macroalgae-Derived Anhydrosugars to 5‑Hydroxymethylfurfural and Levulinic Acid: The Remarkable Case of 3,6-Anhydro‑d‑galactose
Macroalgae or seaweed is considered a renewable and sustainable
resource to produce biobased fuels, polymers, and chemicals due to
its high content of polysaccharides. Various studies have reported
the obtained 5-hydroxymethylfurfural (HMF) and levulinic acid (LA)
from seaweeds. However, the source of the saccharides that is responsible
for HMF formation, accurate yield data (often only HMF concentrations
are given instead of yields on feed), and the reaction pathways (including
byproducts) is not well understood. We here report a kinetic study
on the conversion of 3,6-anhydro-d-galactose (D-AHG), one
of the main building blocks of the polysaccharides in seaweed, to
HMF and LA in water using sulfuric acid as a catalyst with the aim
to rationalize and optimize the production of HMF and LA from seaweeds.
The experiments were carried out in batch at temperatures between
160 and 200 °C using various initial concentrations of D-AHG
(0.006–0.06 M) and sulfuric acid (0.0025–0.05 M) as
the catalyst. The highest experimental yield of HMF within this range
of experimental conditions was remarkably high (61 mol %) and obtained
at 160 °C, with a low initial D-AHG concentration (0.006 M) and
a low acid concentration (0.0025 M). These findings imply that D-AHG
is a very good precursor for the HMF synthesis. Additional experiments
outside the experimental window gave an even higher HMF yield of 67
mol %. The highest LA yields were 51 mol % [160 °C, low initial
D-AHG concentration (0.006 M), and high acid concentration (0.05 M)].
The experimental data were modeled using a power law approach, and
the kinetic model was used to determine reactor configurations giving
the maximum yield of HMF and LA. The result showed that a plug flow
reactor is favorable to achieve the highest yield of HMF, whereas
a continuously ideally stirred tank reactor is the preferable reactor
configuration to obtain the highest yield of LA