(109a) Economically Competitive Production of Oleo-Furan Sulfonate Detergents from Furfural and Fatty Alcohols
AIChE Annual Meeting
2024
2024 AIChE Annual Meeting
Catalysis and Reaction Engineering Division
Biomass Conversion and Biorefining III: Conversion of Alcohols and Ethers
Monday, October 28, 2024 - 12:30pm to 12:48pm
The first step of this process takes place over hydrotalcite catalysts, in which basic sites catalyze the transfer dehydrogenation and aldol condensation reactions. The liquid-phase batch reaction yields an α,β-unsaturated furanic aldehyde at 70% yield and no significant catalyst degradation over 5 recycles.
In the second synthesis step, the obtained aldehyde undergoes hydrodeoxygenation (HDO) to yield the desired oleo-furan molecules. The synthesis is performed over a ruthenium-based catalyst (a mixture of Ru/C, catalyzing localized hydrogen production, and RuO2 hydrate, catalyzing the reverse Mars-van Krevelen HDO step) at 180°C under both inert nitrogen (N2) and hydrogen gas (H2) conditions. At short reaction times, the oleo-furan yield during H2-HDO is observed to be consistently higher than under N2. Remarkably, however, at longer reaction times, oleo-furans production under an inert atmosphere exceeds that of the H2 atmosphere, providing a promising pathway to achieve high oleo-furan yields via hydrodeoxygenation without involving H2. We attribute this observation to the reduction of the RuO2 catalyst to Ru during reaction, which renders it inactive for the HDO reaction.
The subsequent sulfonation of the oleo-furan intermediates yields oleo-furan sulfonate surfactants with good detergency properties. Importantly, technoeconomic analysis of the oleo-furan sulfonate production process suggests improved economic potential compared to the legacy process.