An investigation into support cooperativity for the deoxygenation of guaiacol over nanoparticle Ni and Rh2P. Issue 14 (6th June 2017)

• Record Type: Journal Article
• Authors: Griffin, Michael B.; Baddour, Frederick G.; Habas, Susan E.; Nash, Connor P.; Ruddy, Daniel A.; Schaidle, Joshua A.
• Is Part Of: Catalysis science & technology. Volume 7:Issue 14(2017)
• Page Start: 2954
• Page End: 2966
• Publication Date: 2017-06-06
• Subjects: Catalysis -- Periodicals; 541.395
• DOI: 10.1039/c7cy00261k
• Languages: English
• ISSNs: 2044-4753

Abstract

Abstract : For guaiacol deoxygenation under catalytic fast pyrolysis conditions, support acidity increases catalytic activity while support reducibility enhances selectivity to deoxygenated products. Abstract : The production of hydrocarbon fuels from biomass pyrolysis requires the development of effective deoxygenation catalysts, and insight into how the properties of the support influence performance is critical for catalyst design. In this report, nanoparticles of Ni and Rh2 P were synthesized using solution-phase techniques and dispersed on high surface area supports. The supports included a relatively inert material (C), an acidic reducible metal-oxide (TiO2 ), an acidic irreducible metal-oxide (Al2 O3 ), and a basic irreducible metal-oxide (MgO). The eight active phase/support combinations were investigated for the deoxygenation of guaiacol, a pyrolysis vapor model compound, under ex situ catalytic fast pyrolysis conditions (350 °C, 0.44 MPa H2 ). Compared to the baseline performance of the C-supported catalysts, Ni/TiO2 and Rh2 P/TiO2 exhibited higher guaiacol conversion and lower O : C ratios for C5+ products, highlighting the enhanced activity and greater selectivity to deoxygenated products derived from the use of an acidic reducible metal-oxide support. The Al2 O3 -supported catalysts also exhibited higher conversion than the C-supported catalysts and promoted alkylation reactions, which improve carbon efficiency and increase the carbon number of the C5+ products. However, Ni/Al2 O3 and Rh2 P/Al2 O3 were less selective towards deoxygenated products than the C-supported catalysts. The MgO-supported catalyst exhibited lower conversion and decreased yield of deoxygenated products compared to the C-supported catalysts. The results reported here suggest that basic metal-oxide supports may inhibit deoxygenation of phenolics under CFP conditions. Contrastingly, support acidity and reducibility were demonstrated to promote conversion and selectivity to deoxygenated products, respectively.