(513f) Sustainable Solid Acid Carbon Catalysts from Renewable Biomass for Fine and Specialty Chemical Synthesis | AIChE

(513f) Sustainable Solid Acid Carbon Catalysts from Renewable Biomass for Fine and Specialty Chemical Synthesis

Authors 

Sripada, S. - Presenter, University of Georgia
Kastner, J., University of Georgia
Organic acid esterification reactions yield products that find a wide range of applications in the pharmaceutical, cosmetic and polymer sectors. Industrially, these reactions employ homogeneous liquid acid catalysts such as sulfuric acid, posing limitations including reactor corrosion, requirement of additional purification steps and non-reusability. The large amount of acidic waste generated is also a major environmental concern. Sulfonated carbon has emerged as an efficient, heterogeneous solid acid catalyst for esterification reactions, primarily in biodiesel synthesis. Apart from being easy to recover and regenerate, these catalysts are also stable in aqueous environments. Traditionally, these catalysts are synthesized by the hydrothermal sulfonation of carbon with concentrated H2SO4 at temperatures above 200ËšC, or by treatment with toxic gaseous SO3.

With the intent of incorporating sustainability into our catalyst preparation methods, activated carbon derived from woody biomass, in its granular and monolith forms was used to synthesize sulfonated carbon. Activated carbon monolith (ACM) confers the advantage of continuous processing with lower pressure drop and higher mass transfer rates over the granular activated carbon(GAC). We propose a new method where dilute H2SO4 can replace concentrated acid as the sulfonating agent. Innovations in green catalyst design have suggested that plasma technology could be a valuable tool for catalyst synthesis. This technology permits the synthesis of carbon catalysts at low temperatures and pressures, besides reducing the time required for catalyst preparation. Using plasma with different carrier gases, we demonstrate the functionalization of sulfonic acid on activated carbon in granular and monolith forms. The catalytic activity of the hydrothermal and plasma sulfonated carbon catalysts (GAC and crushed ACM) will be compared to a petroleum-derived, industrial benchmark catalyst, Amberlyst-15 in batch esterification reactions of 2-hydroxyisobutyric acid (2HIBA). This research could have potential implications in the catalytic upgrading of fermentation derived organic acids.