@article { ISI:000283589900009, title = {Chemoselective hydrogenation of cinnamaldehyde over Pd/CeO2-ZrO2 catalysts}, journal = {Catalysis Letters}, volume = {140}, number = {1-2}, year = {2010}, month = {NOV}, pages = {55-64}, publisher = {SPRINGER}, address = {233 SPRING ST, NEW YORK, NY 10013 USA}, abstract = {

Selective hydrogenation of cinnamaldehyde over Pd (2 wt\%) supported on CeO2, ZrO2 and CeO2-ZrO2 catalysts is reported for the first time. In general, the olefinic (C=C) group of cinnamaldehyde is preferentially hydrogenated compared to the carbonyl (C=O) group. This selectivity preference could, however, be altered or reversed by adding alkali additives to the catalyst. The influence of additive on the structure and redox properties of the active sites and correlation of that with selective hydrogenation activity is investigated.

}, keywords = {alpha, beta-Unsaturated aldehyde, Ceria-zirconia, Cinnamaldehyde, Hydrogenation, palladium catalyst}, issn = {1011-372X}, doi = {10.1007/s10562-010-0423-z}, author = {Bhogeswararao, Seemala and Srinivas, D.} } @article { ISI:000315069400009, title = {Catalytic activity of ZIF-8 in the synthesis of styrene carbonate from CO2 and styrene oxide}, journal = {Catalysis Communications}, volume = {32}, year = {2013}, month = {FEB}, pages = {36-40}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The catalytic activity of ZIF-8 in the synthesis of styrene carbonate from carbon dioxide and styrene oxide is presented. ZIF-8 crystals displayed catalytic activity even at temperatures as low as 50 degrees C, with styrene carbonate yields as high as similar to 54\% at 100 degrees C. In contrast to many prior-art catalysts, solvents or co-catalysts were not required. Pyridine and ammonia were used as probe molecules to estimate the type and density of acid sites in fresh and reused ZIF-8 catalysts. DRIFT spectroscopy of adsorbed pyridine revealed the presence of both Bronsted (B) and Lewis (L) acid sites. The B-sites have nearly vanished in the case of recycled ZIF-8 catalysts. The simultaneous presence of both the acid sites and the nitrogen basic moieties from the imidazole linker in ZIF-8 promoted the adsorption of the CO2 on the solid surface and its further conversion to the cyclic carbonate. The ZIF-8 catalysts could be recycled and reused without significant loss in catalytic activity. Published by Elsevier B.V.

}, keywords = {CO2 conversion, cyclic carbonates, Styrene carbonate, Zeolitic imidazolate frameworks, ZIF-8}, issn = {1566-7367}, doi = {10.1016/j.catcom.2012.12.003}, author = {Zhu, Minqi and Srinivas, Darbha and Bhogeswararao, Seemala and Ratnasamy, Paul and Carreon, Moises A.} } @article { ISI:000356739400008, title = {Catalytic conversion of furfural to industrial chemicals over supported Pt and Pd catalysts}, journal = {Journal of Catalysis}, volume = {327}, year = {2015}, month = {JUL}, pages = {65-77}, publisher = {ACADEMIC PRESS INC ELSEVIER SCIENCE}, address = {525 B ST, STE 1900, SAN DIEGO, CA 92101-4495 USA}, abstract = {

Several industrial chemicals were prepared by hydrogenation of furfural over gamma-Al2O3-supported Pt and Pd catalysts. These catalysts were active even at room temperature (25 degrees C). While the Pt catalysts were selective for C=O hydrogenation (yielding furfuryl alcohol), Pd facilitated ring hydrogenation (producing tetrahydrofurfuryl alcohol). At high temperature (240 degrees C), the Pd catalyst exhibited excellent decarbonylation activity forming furan with 85\% yield. The catalyst was reusable even in the absence of external hydrogen. The presence of hydrogen led to ring-opened products. Furan was quantitatively converted at 25 degrees C to tetrahydrofuran. Acidity of the support made a marked influence on the activity and selectivity. Pt on SO4-ZrO2 favored hydrogenolysis yielding 2-methyl furan along with furan with \>75 wt\% selectivity. Particle size, metal dispersion, and solvent influenced catalytic activity. Differences in structure and mode of furfural adsorption were also the causes for variations in selectivity of these supported Pt and Pd catalysts. (C) 2015 Elsevier Inc. All rights reserved.

}, keywords = {Biomass to fuels and chemicals, Decarbonylation, furfural, Hydrogenation, Hydrogenolysis, Supported Pt and Pd catalysts}, issn = {0021-9517}, doi = {10.1016/j.jcat.2015.04.018}, author = {Bhogeswararao, Seemala and Srinivas, D.} }