| Aqueous-Phase Hydrogenation Of Organic Acids On Monometallic Supported Catalysts: A Combined Experimental And Theoretical Study | ||
| Ye Xu, Center for Nanophase Materials Sciences, and Chemical Sciences Division, Oak Ridge National Laboratory, P.O. Box 2008, MS-6493, Oak Ridge, TN 37831-6493, Hakan O. Olcay, Department of Chemical Engineering, University of Massachusetts, Amherst, Goessmann Laboratory, N. Pleasant Street, Amherst, MA 01003 and George Huber, Chemical Engineering, University of Massachusetts-Amherst, 159 Goessmann Lab, 686 North Pleasant St., Amherst, MA 01003
Depletion of fossil fuel combined with environmental and
political concerns with fossil fuels have accelerated research on technologies
to convert biomass into liquid fuels, i.e biofuels. Aqueous-phase hydrogenation
(APH) reactions are crucial for biofuel production including: ethanol
production by hydrogenation of fermentation products (organic acids) [1], gasoline production by hydrogenation of pyrolysis-oils [2], and alkane production by
aqueous-phase dehydration/hydrogenation of carbohydrates [3]. APH reactions
involve hydrogenating a range of functionalities, including acids (C-OOH
bonds), sugars (C-O-C bonds), alkenes (C=C bonds) and aldehydes (C=O bonds).
The objective of this project is to develop a fundamental understanding for
aqueous-phase hydrogenations of organic acids by a combined theoretical and
experimental approach.
We are in the process of measuring the catalytic activity for aqueous-phase hydrogenation of acetic acid with supported monometallic Ru, Pt, Pd, Ni and Cu based catalysts in a fixed bed reactor. The Ru catalyst is significantly more active than Pt. The reaction is first order with respect to H2 for Ru/Carbon with an apparent activation energy of 31 kJ/mol. The reaction is 0.6 order with respect to H2 for Pt-based catalysts with an apparent activation energy of 33 kJ/mol.
These experimental data are combined with density functional theory (DFT) calculations to offer us insight into why some monometallic catalysts are more active. We have calculated the energetics and kinetics of probable elementary steps for acetic acid hydrogenation on Ru(0001). The results are compared with previous DFT calculations for hydrogenation of acetic acid on Pt, Pd and Cu [4-6]. With the additional information afforded by theory we are attempting to identify the physical origin of the difference in the activities of these monometallic catalysts. This study will provide valuable insight for designing a more versatile APH catalyst in the future, which will probably be bi-metallic.
[1] T. Eggeman, D. Verser, Recovery of organic acids from fermentation broths, Appl. Biochem. Biotechnol. 2005, 121-124, 605. [2] G. W. Huber, S. Iborra, A. Corma, Synthesis of transportation fuels from biomass: chemistry, catalysts and engineering, Chem. Rev. 2006, 106, 4044. [3] G. W. Huber, J. A. Dumesic, An overview of aqueous-phase catalytic processes for production of hydrogen and alkanes in a biorefinery, Catal. Today 2006, 111, 119. [4] R. Alcala, J. W. Shabaker, G. W. Huber, M. A. Sanchez-Castillo, J. A. Dumesic, Experimental and DFT studies of the conversion of ethanol and acetic acid on PtSn-based catalysts, J. Phys. Chem. B 2005, 109, 2074. [5] V. Pallassana, M. Neurock, Reaction paths in the hydrogenolysis of acetic acid to ethanol over Pd(111), Re(0001), and PdRe alloys, J. Catal. 2002, 209, 289. [6] M. A. Natal Santiago, M. A. Sanchez-Castillo, R. D. Cortright, J. A. Dumesic, Catalytic reduction of acetic acid, methyl acetate, and ethyl acetate over silica-supported copper, J. Catal. 2000, 193, 16. Extended Abstract Status: Not Uploaded | ||