The conversion of glycerol into lactic acid in alkaline medium using heterogeneous catalysts has been highlighted and has proved to be an e cient alternative to the conventional fermentative route. This work investigated the production of lactic acid from glycerol in alkaline medium using copper catalysts obtained from hydrotalcite-like precursors in a continuous ow reaction system and the effect of different copper loading on catalytic behaviors in terms of yield and selectivity to lactic acid. The catalysts were synthesized by the coprecipitation method and characterized by XRF, XRD, N 2 adsorption-desorption, H 2 -TPR, CO 2 -TPD, and the copper dispersion was determined by N 2 O oxidation. The reaction was performed for 30 h at 240°C, 35 atm, using space velocity (WHSV) of 2 h − 1 , solution of 10 vol% glycerol, and NaOH/glycerol molar ratio of 0.75. Although the 30CuHT catalyst presented higher BET surface areas, Cu dispersion, and basicity than the 20CuHT catalyst, the best results in terms of glycerol conversion (96.5%) and yield (64%) to lactic acid were obtained in the catalytic test performed with the 20CuHT catalyst. This result may be related to the reaction steps that occur in the liquid phase in the presence of the hydroxyl group (OH -). Furthermore, the high content of Cu may favor the hydrogenation of the reaction intermediates (2-hydroxypropenal and pyruvaldehyde), increasing the formation of 1,2-propanediol and consequently reducing the yield of lactic acid. Finally, the catalytic activity of the reduced and nonreduced catalysts was investigated, and the results showed that copper oxide also has catalytic activity.However, the reduction of copper oxide provides better results. Statement Of NoveltyThis study is a new contribution to green chemistry production from biomass-derived products, focusing on the production of lactic acid from glycerol in an alkaline medium using copper catalysts obtained from hydrotalcite-like precursors in a continuous ow reaction system. The motivation for this study is the lack of works that evaluate the effect of the copper loading on the catalysts used in transforming glycerol into lactic acid. In addition, no studies were found in the literature that used hydrotalcite-type precursors for this reaction. Some researchers have evaluated the use of copper oxide as a catalyst.However, in this study, it was observed that for higher yields in the conversion of glycerol into lactic acid, it is necessary to use reduced copper (Cu°) catalysts.
RESUMO -A demanda crescente por biodiesel tem gerado um enorme excedente de glicerol no mercado nacional e mundial e isto tem impulsionando diversas pesquisas visando a transformação do glicerol em produtos de maior importância industrial. O ácido lático possui vasta aplicação na indústria, e a transformação hidrotérmica do glicerol a ácido lático apresentase como uma alternativa ao processo convencional de produção, assim como uma alternativa para o uso do glicerol. Neste trabalho foi investigado a produção de ácido lático a partir do glicerol em meio básico, utilizando catalisador de Cu suportado em MgO, Al2O3 e ZnO em sistema reacional de fluxo contínuo. As condições reacionais empregadas foram de 240 ºC, 35 atm, WHSV de 2 h -1 , solução 10 vol.% de glicerol e razão molar de NaOH/glicerol de 1, 0,75 e 0,5. Os resultados apresentaram elevada conversão do glicerol (95 %) com rendimento e seletividade a ácido lático acima dos 80 e 90 %, respectivamente, utilizando o catalisador Cu/MgO.
The conversion of glycerol into lactic acid in alkaline medium using heterogeneous catalysts has been highlighted and has proved to be an efficient alternative to the conventional fermentative route. This work investigated the production of lactic acid from glycerol in alkaline medium using copper catalysts obtained from hydrotalcite-like precursors in a continuous flow reaction system and the effect of different copper loading on catalytic behaviors in terms of yield and selectivity to lactic acid. The catalysts were synthesized by the coprecipitation method and characterized by XRF, XRD, N2 adsorption-desorption, H2-TPR, CO2-TPD, and the copper dispersion was determined by N2O oxidation. The reaction was performed for 30 h at 240°C, 35 atm, using space velocity (WHSV) of 2 h− 1, solution of 10 vol% glycerol, and NaOH/glycerol molar ratio of 0.75. Although the 30CuHT catalyst presented higher BET surface areas, Cu dispersion, and basicity than the 20CuHT catalyst, the best results in terms of glycerol conversion (96.5%) and yield (64%) to lactic acid were obtained in the catalytic test performed with the 20CuHT catalyst. This result may be related to the reaction steps that occur in the liquid phase in the presence of the hydroxyl group (OH-). Furthermore, the high content of Cu may favor the hydrogenation of the reaction intermediates (2-hydroxypropenal and pyruvaldehyde), increasing the formation of 1,2-propanediol and consequently reducing the yield of lactic acid. Finally, the catalytic activity of the reduced and non-reduced catalysts was investigated, and the results showed that copper oxide also has catalytic activity. However, the reduction of copper oxide provides better results.
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