Monday, November 9, 2015: 2:10 PM
355C (Salt Palace Convention Center)
In this presentation, we describe a multi-step catalytic approach for conversion of cellulose into 1,6-hexanediol (C6 α,ω-diol) which is a high-volume (130,000 tons/year), high value ($4,600/ton) commodity chemical. Cellulose is first converted to levoglucosan which is then dehydrated into levoglucosenone (LGO) in the condensed phase with dilute acid (5-20 mM acid concentration) using a polar, aprotic solvent. The product selectivity is a function of the water concentration, the solvent type and the cellulose loading. Increasing the water content leads to the production of 5-hydroxymethylfurfural. The LGO is then hydrogenated into dihydrolevoglucosenone, levoglucosanol, and tetrahydropyran-2-methanol (THPM). The THPM then undergoes selective C-O-C hydrogenolysis to produce 1,6-hexanediol using a bifunctional (reducible metal with an oxophilic promoter) catalyst with > 90% selectivity to the desired α,ω-diol. We will discuss how the catalytic properties change the reaction pathways in these various steps and how further improvements in catalyst design could be used to produce these high value commodity chemicals from biomass.
See more of this Session: Catalytic Processing of Fossil and Biorenewable Feedstocks: Chemicals & Fuels II
See more of this Group/Topical: Catalysis and Reaction Engineering Division
See more of this Group/Topical: Catalysis and Reaction Engineering Division