Breadcrumb
- Home
- Publications
- Proceedings
- 2012 AIChE Annual Meeting
- Fuels and Petrochemicals Division
- Catalytic Biofuels Refining
- (264c) Kinetics of High Pressure Catalytic Reaction Pathways for Dihydroeugenol Over Pt/ZrO2
Kinetic data was obtained for the reaction of the lignin-derived compound dihydroeugenol (2-methoxy-4-propylphenol) in hydrogen over a 2%Pt/ZrO2 catalyst in a vapor-phase fixed-bed reactor at 24 atm total pressure. Weight hourly space velocities were varied from 100-1000 g hr-1 g cat-1 to obtain reaction pathways. Reaction orders and activation energies were obtained over a temperature range of 200-400oC, hydrogen partial pressure range of 0-23 atm and dihydroeugenol partial pressure range of 0.4-1.2 atm under differential conditions.
Three main reaction pathways were identified: HDO, transalkylation, and hydrogenation of the aromatic ring. The WHSV studies suggest that the HDO pathway occurs via a series reaction, with methoxy group removal occurring first followed by phenol group removal. Transalkylation occurs via methyl attachment to the aromatic ring. The four isomers of the pure hydrogenation product 2-methoxy-4-propylcyclohexanol have: 1) positive apparent activation energies in the range of 25 to 40 kJ mol-1 in the temperature range 200-240oC and negative apparent activation energies of -10 to -40 kJ mol-1 for temperatures of 280-320oC 2) dihydroeugenol orders of 0.5-0.7 and 3) hydrogen orders of 1.9-2.5 at 300oC. The similarity of these kinetic results to those for benzene hydrogenation suggest that the mechanism of ring hydrogenation for dihydroeugenol is similar to that of other aromatic compounds [2]. At 300oC the aromatic HDO products 4-propyl phenol and propylbenzene have apparent activation energies of 88 and 128 kJ mol-1, dihydroeugenol orders of 0.6 and 0.6, and hydrogen orders of 0.36 and 0.38, respectively. The analogous hydrogenated HDO products 4-propylcyclohexanol and propylcyclohexane have apparent activation energies of 27 and 67 kJ mol-1, dihydroeugenol orders of 0.33 and 0.43, and hydrogen orders of 3.2 and 2.4 respectively. The reaction sequences and rate expressions will be discussed for the three reaction pathways.
References:
1) R. Agrawal, N. R. Singh, Synergistic Routes to Liquid Fuel for a Petroleum Deprived Future, AIChE Journal,55,7,1898-1905, 2009.
2) S. D. Lin, M. A. Vannice, Hydrogenation of Aromatic Hydrocarbons over Supported Pt Catalysts I. Benzene Hydrogenation, Journal of Catalysis, 143, 539-553, 1993.