TY - JOUR
T1 - Pd-promoted selective gas phase hydrogenation of p-chloronitrobenzene over alumina supported Au
AU - Cardenas-Lizana, Fernando
AU - Gómez-Quero, Santiago
AU - Hugon, Antoine
AU - Delannoy, Laurent
AU - Louis, Catherine
AU - Keane, Mark A.
PY - 2009/3/10
Y1 - 2009/3/10
N2 - The gas phase hydrogenation of p-chloronitrobenzene has been investigated over alumina supported Au (ca. 1%, w/w) prepared by deposition-precipitation with urea (DP) and impregnation in excess solvent (IMP). Both catalysts were 100% selective in terms of -NO2 group reduction, resulting in the sole formation of p-chloroaniline. Au-DP exhibited a smaller mean Au size (2.9 nm) compared with Au-IMP (4.5 nm) and delivered a higher (by a factor of 14) specific hydrogenation rate. Bimetallic Pd-Au/Al2O3 catalysts have also been prepared by DP and IMP with Au/Pd mol/mol = 8, 20 and 88. Catalyst activation by temperature programmed reduction has been monitored and the activated catalysts characterized in terms of H2 chemisorption, TEM analysis and DRIFTS. DRIFTS measurements using CO as a probe molecule suggest the presence of bimetallic particles and surface Au-Pd interaction. A significant increase (by up to a factor of 3) in activity was observed for Pd-Au/Al2O3 (Au/Pd = 20) compared with Au/Al2O3 where the exclusive conversion of p-chloronitrobenzene to p-chloroaniline was maintained. At a lower ratio (Au/Pd = 8), nitrobenzene was produced as a result of a Pd catalyzed hydrodechlorination step. Under the same reaction conditions, Au/Al2O3 + Pd/Al2O3 physical mixtures (Au/Pd = 20) delivered higher reaction rates but with the formation of nitrobenzene and aniline, i.e. products of hydrodechlorination and hydrogenation. We attribute the enhanced and exclusive production of p-chloroaniline over the supported bimetallics to a surface Pd-Au synergism. Our results establish the viability of Pd-promotion in the selective continuous gas phase catalytic hydrogenation of p-chloronitrobenzene over supported Au. © 2008 Elsevier Inc. All rights reserved.
AB - The gas phase hydrogenation of p-chloronitrobenzene has been investigated over alumina supported Au (ca. 1%, w/w) prepared by deposition-precipitation with urea (DP) and impregnation in excess solvent (IMP). Both catalysts were 100% selective in terms of -NO2 group reduction, resulting in the sole formation of p-chloroaniline. Au-DP exhibited a smaller mean Au size (2.9 nm) compared with Au-IMP (4.5 nm) and delivered a higher (by a factor of 14) specific hydrogenation rate. Bimetallic Pd-Au/Al2O3 catalysts have also been prepared by DP and IMP with Au/Pd mol/mol = 8, 20 and 88. Catalyst activation by temperature programmed reduction has been monitored and the activated catalysts characterized in terms of H2 chemisorption, TEM analysis and DRIFTS. DRIFTS measurements using CO as a probe molecule suggest the presence of bimetallic particles and surface Au-Pd interaction. A significant increase (by up to a factor of 3) in activity was observed for Pd-Au/Al2O3 (Au/Pd = 20) compared with Au/Al2O3 where the exclusive conversion of p-chloronitrobenzene to p-chloroaniline was maintained. At a lower ratio (Au/Pd = 8), nitrobenzene was produced as a result of a Pd catalyzed hydrodechlorination step. Under the same reaction conditions, Au/Al2O3 + Pd/Al2O3 physical mixtures (Au/Pd = 20) delivered higher reaction rates but with the formation of nitrobenzene and aniline, i.e. products of hydrodechlorination and hydrogenation. We attribute the enhanced and exclusive production of p-chloroaniline over the supported bimetallics to a surface Pd-Au synergism. Our results establish the viability of Pd-promotion in the selective continuous gas phase catalytic hydrogenation of p-chloronitrobenzene over supported Au. © 2008 Elsevier Inc. All rights reserved.
KW - Au/Al 2 O 3
KW - DRIFTS analysis
KW - H 2 chemisorption
KW - p-Chloroaniline
KW - p-Chloronitrobenzene
KW - Pd-Au/Al 2 O 3
KW - Selective hydrogenation
KW - TPR
UR - http://www.scopus.com/inward/record.url?scp=60649103557&partnerID=8YFLogxK
U2 - 10.1016/j.jcat.2008.12.019
DO - 10.1016/j.jcat.2008.12.019
M3 - Article
SN - 0021-9517
VL - 262
SP - 235
EP - 243
JO - Journal of Catalysis
JF - Journal of Catalysis
IS - 2
ER -