Stable Sulfonic MCM-41 Catalyst for Furfural Production from Renewable Resources in a Biphasic System

An MCM-41-SO3H catalyst with 14 wt% S was successfully synthesized to be used in furfural production from xylose and hemicellulose in a biphasic n-butanol/water system. The precursor MCM-41 and the acid-functionalized MCM-41-SO3H catalyst were characterized by XRD, FTIR, TEM, N-2 physisorption, ICP-MS, TPD-NH3, and XPS. The characterization results indicated that the sulfonic process partially decreased the ordered mesoporous structure and increased the acid strength of the initial MCM-41. The catalytic performance of the xylose conversion was evaluated in a batch-type reactor using different biphasic ecological and renewable n-butanol/water ratios (1:1, 1.5:1, 2:1, and 2.5:1) as dissolvent at 170 & DEG;C. The effect of the dissolvent mixture was clearly seen from the larger initial reaction rate and TOF values for the 1.5:1 ratio. This catalytic behavior indicated that a proper proportion of n-butanol/water dissolvent mixture enhanced the solubility of the substrate in the n-butanol-rich mixture and prevented the deactivation of acidic sulfonated surface groups. To achieve transformation of lignocellulosic raw material to value-added products, the MCM-41-SO3H catalyst was also used for the production of furfural. The recycling evaluation tests indicated that for the recovered catalyst submitted to a sulfonation process, the yield of furfural was closer to the fresh catalyst.

Automated summary

An MCM-41-SO3H catalyst with a sulfonic process was successfully synthesized and characterized for furfural production from xylose and hemicellulose. The catalytic performance was evaluated using different n-butanol/water ratios as dissolvent, and a proper ratio enhanced substrate solubility and prevented deactivation of the catalyst. Recycling evaluation tests showed that the yield of furfural was closer to the fresh catalyst when the recovered catalyst underwent a sulfonation process.