4.6 Article

Non-Porous Sulfonic Acid Catalysts Derived from Vacuum Residue Asphaltenes for Glycerol Valorization via Ketalization with Acetone

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CATALYSTS
卷 11, 期 7, 页码 -

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MDPI
DOI: 10.3390/catal11070776

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glycerol; solketal; asphaltenes; sulfonic acid catalyst; ketalization

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A method for preparing heterogeneous acid catalysts based on asphaltenes from vacuum residue was proposed. The sulfonated asphaltenes showed high activity and stability in the ketalization reaction between glycerol and acetone. The most active sample had a lower activation energy compared to other known heterogeneous catalysts and exhibited no acid leaching or loss of activity after multiple cycles.
In this study, an approach for the preparation of heterogeneous acid catalysts based on asphaltenes isolated from vacuum residue is proposed. Varying the conditions for the sulfonation of asphaltenes made it possible to obtain materials with an acid value of 1.16 to 2.76 meq g(-1) and a total sulfur content of 6.4 to 12.3 wt%. The samples obtained were characterized by acid-base titration, nitrogen adsorption, sulfur elemental analysis and transmission electron microscopy techniques, and were studied as potential acid catalysts in the ketalization reaction between glycerol and acetone. Sulfonated asphaltenes (SA) were characterized by a homogeneous distribution of sulfonic groups over the granule surface and an almost complete absence of a porous structure. The ketalization reaction in the presence of SA proceeded without intradiffusion restrictions; as a result of which, their activity was higher than for known heterogeneous catalysts. The most active SA sample (total acid value, 1.16 meq g(-1)) had an apparent activation energy of 18.0 kJ mol(-1), which was lower than the value obtained for the zeolite BEA-40 (29-53 kJ mol(-1)) and the Amberlyst 36 resin (27 kJ mol(-1)), and was close to the value for the homogeneous p-TSA catalyst (14.5 kJ mol(-1)). The SA heterogeneous catalysts did not show any acid leaching and had no loss of activity after five catalytic cycles, with the total turnover number TON = 7247.

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