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<dc:title>The Study and Optimization of the AlCl3/SnCl2 Catalyst System in the Subcritical Water Production of Lactic Acid from Corn Stover</dc:title>
<dc:creator>Candela Gil, Helena</dc:creator>
<dc:creator>Illera Gigante, Alba Ester</dc:creator>
<dc:creator>Barea Gómez, Pedro</dc:creator>
<dc:creator>Beltrán Calvo, Sagrario</dc:creator>
<dc:creator>Sanz Díez, Mª Teresa</dc:creator>
<dc:subject>Al(III)/Sn(II)</dc:subject>
<dc:subject>Lactic acid</dc:subject>
<dc:subject>Corn stover</dc:subject>
<dc:subject>Subcritical water</dc:subject>
<dc:subject>Organic acids</dc:subject>
<dc:description>The lactic acid (LA) production from corn stover using Lewis acid catalysts was&#xd;
optimized. Initially, an equimolar mixture of Al(III)/Sn(II) was used as a catalytic system&#xd;
at 190 ◦C with 5 wt% biomass. Increasing the catalyst concentration led to higher LA&#xd;
production, showing the optimal results at 16 mM. A low catalyst concentration mainly&#xd;
produced furfural and HMF, dehydration products from the corn stover sugars. Higher&#xd;
catalyst concentration increased LA yield but also produced the degradation of the glucose&#xd;
dehydration products into levulinic and formic acids, reducing LA selectivity. Al(III)&#xd;
was essential for LA formation, while Sn(II) was less effective due to its lower solubility,&#xd;
shown by the presence of Sn(II) in the solid residue after treatments. A total of 16 mM&#xd;
Al(III) yielded the highest LA levels at 190 ◦C, 7.4 g/L, and 20.7% yield. Increasing the&#xd;
temperature to 210 ◦C accelerated the LA production while also achieving the lowest energy&#xd;
consumption, which was 0.47 kWh/g LA at the highest LA production point. However,&#xd;
longer treatments at this temperature caused LA degradation. AlCl3 has been identified as&#xd;
an ideal catalyst for biomass conversion to LA, being inexpensive and low in toxicity.</dc:description>
<dc:date>2025-10-02T09:44:18Z</dc:date>
<dc:date>2025-10-02T09:44:18Z</dc:date>
<dc:date>2025-06</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>https://hdl.handle.net/10259/10917</dc:identifier>
<dc:identifier>10.3390/catal15060539</dc:identifier>
<dc:identifier>2073-4344</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>Catalysts. 2025, V. 15, n. 6, 539</dc:relation>
<dc:relation>https://doi.org/10.3390/catal15060539</dc:relation>
<dc:rights>http://creativecommons.org/licenses/by/4.0/</dc:rights>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>Atribución 4.0 Internacional</dc:rights>
<dc:publisher>MDPI</dc:publisher>
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