@article { ISI:000233264700006, title = {Influence of alkali metal doping on selectivity behaviour of platinum catalysts for hydrogenation of 2-butyne-1,4-diol}, journal = {Catalysis Communications}, volume = {6}, number = {11}, year = {2005}, month = {NOV}, pages = {725-730}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Hydrogenation of 2-butyne-1,4-diol to 2-butene-1,4-diol (B(2)D) and butane-1,4-diol (B(1)D) using Pt catalysts doped with alkali metals was studied. These catalysts showed higher selectivity to the olefinic diol (B2D) compared to that with monometallic platinum catalyst. Among various alkali metals, Cs-doped catalyst showed highest selectivity (\>99\%) to B(2)D. The selectivity to B(2)D increased (up to 99.9\%) with increase in the concentration of Cs from 0.25\% to 1\%. The increase in the basic strength of alkali doped catalysts measured by CO(2)-TPD, would be responsible for the increase in electron density of Pt hence, faster desorption and higher selectivity to the intermediate olefinic diol (B(2)D). The reaction parameters; such as temperature, H(2) pressure and substrate concentration haye strong influence on the catalyst activity but almost no effect on the selectivity to B(2)D. (c) 2005 Elsevier B.V. All rights reserved.

}, keywords = {2-butene-1, 2-butyne-1, 4-diol, alkali metal doping, platinum catalysts, Selective hydrogenation}, issn = {1566-7367}, doi = {10.1016/j.catcom.2005.07.009}, author = {Telkar, M. M. and Rode, C. V. and Rane, V. H. and Chaudhari, R.} } @article { ISI:000233062500003, title = {Role of a co-metal in bimetallic Ni-Pt catalyst for hydrogenation of m-dinitrobenzene to m-phenylenediamine}, journal = {Applied Catalysis A-General}, volume = {295}, number = {1}, year = {2005}, month = {OCT}, pages = {23-30}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Bimetallic Ni-Pt catalysts supported on carbon were found to give very high turn over frequency numbers and almost complete selectivity to m-phenylenediamine in m-dinitrobenzene hydrogenation as compared to the monometallic nickel catalysts. The XRD and XPS characterization revealed that most of the nickel remains as Ni2+ in a monometallic catalyst while, the addition of platinum leads to the stabilization of Ni-0 state, in case of bimetallic catalysts. (c) 2005 Elsevier B.V. All rights reserved.

}, keywords = {Bimetallic catalyst, Catalytic hydrogenation, m-dinitrobenzene, m-phenylenediamine, Selective hydrogenation, turn over number, XPS and XRD of nickel}, issn = {0926-860X}, doi = {10.1016/j.apcata.2005.07.050}, author = {Telkar, M. M. and Nadgeri, J. M. and Rode, C. V. and Chaudhari, R.} } @article { ISI:000256892200001, title = {Catalytic hydrogenation of 2-butyne-1,4-diol: activity, selectivity and kinetics studies}, journal = {Journal of the Japan Petroleum Institute}, volume = {51}, number = {3}, year = {2008}, month = {MAY}, pages = {119-133}, publisher = {JAPAN PETROLEUM INST}, type = {Article}, address = {YOYU-KANDA BLDG. 4F, 1-8-4 KANDASUDA-CHO, CHIYODA-KU, TOKYO, 108-0041, JAPAN}, abstract = {

The reaction pathway for hydrogenation of 2-butyne-1,4-diol involves parallel and consecutive isomerization as well as hydrogenation reactions forming other side products along with cis-2-butene-1,4-diol and butane-1,4-diol. Hence, achieving the highest selectivity to butene- and/or butanediol is critical from industrial point of view. Hydrogenation of butynediol is also of fundamental significance, due to its adsorption characteristics leading to the formation of active species and their role in determining the product distribution. Studies on designing various catalyst systems including colloidal as well supported palladium nanoparticles for the hydrogenation of butynediol, role of additives, catalyst pretreatment, kinetic studies carried out in our group has been presented in this review. Interestingly, almost complete selectivity to the intermediate olefinic diol was achieved with 1\% Pd/CaCO3-NH3 catalyst system. This could be due to the competitive adsorption of ammonia on the palladium surface along with the substrate 2-butyne-1,4-diol. Studies on catalyst pretreatment and kinetics using palladium catalyst have also been presented here. Nanostructure palladium both colloidal as well as supported catalysts showed a very high catalytic activity (10-40 times more) in the hydrogenation 2-butyne-1,4-diol to cis-2-butene-1,4-diol compared with the corresponding conventional Pd catalysts. For platinum based catalysts, formation of side products was completely eliminated in the hydrogenation of butyne diol. The increase in the basic strength of alkali metal doped Pt catalysts measured by CO2-TPD, led to the increase in electron density of Pt hence, faster desorption and higher selectivity to butenediol. In the case of continuous hydrogenation, the selectivity pattern was completely different from that found in the case of batch slurry reactor and by varying the contact time, the selectivity to both butene- and butanediols could be varied over a wide range of conditions.

}, keywords = {2-butene-1, 2-butyne-1, 4-diol, alkali metal doping, catalyst pretreatment, nano palladium catalyst, Selective hydrogenation}, issn = {1346-8804}, doi = {10.1627/jpi.51.119}, author = {Rode, Chandrashekhar V.} } @article { ISI:000252293400023, title = {Hydrogenation activity and selectivity behavior of supported palladium nanoparticles}, journal = {Catalysis Communications}, volume = {9}, number = {3}, year = {2008}, month = {MAR}, pages = {441-446}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Enhancement in activity and selectivity of catalytic hydrogenation using supported nanosize palladium catalyst has been investigated. Pd/C catalyst prepared in the presence of polyvinyl pyrrolidone (PVP) as a stabilizer gave Pd particle size in a narrow range of 3-5 nm. While, evaluating for hydrogenation of 2-butyne-1,4-diol, the rate enhancement was found to be 10 times higher as compared to the conventional (bulk) Pd catalysts. A proper choice of stabilizer (PVP) giving small particle size as well as highly dispersed nature of nano particles were the major factors for such a dramatic enhancement of activity. (c) 2007 Elsevier B.V. All rights reserved.

}, keywords = {butynediol, Catalytic hydrogenation, nanosize palladium, Selective hydrogenation, SEM-EDX analysis, size distribution, supported Pd nanoparticles}, issn = {1566-7367}, doi = {10.1016/j.catcom.2007.07.023}, author = {Nadgeri, J. M. and Telkar, M. M. and Rode, C. V.} } @article { ISI:000291421400015, title = {Selective hydrogenation of chloronitrobenzenes with an MCM-41 supported platinum allyl complex derived catalyst}, journal = {Applied Catalysis A-General}, volume = {399}, number = {1-2}, year = {2011}, month = {MAY}, pages = {117-125}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

A platinuin precatalyst (1) has been prepared by reacting [(eta(3)-C3H5)(4)Pt4Cl4] with surface functionalized MCM-41 with pendant -(CH2)(3)NH(CH2)(2)NH2 groups. For the hydrogenation of o-, m- and p-chloronitrobenzenes to the corresponding chloroanilines, 1 is found to be a highly active catalyst with good selectivities for them-and p-isomers. Its performance is superior to that of its palladium analogue and far superior to that of commercial (5\%) Pt/C or (5\%) Pt/Al2O3. Comparison of solid state and solution NMR data and other evidences indicate that on treatment with the functionalized MCM-41 support; [(eta(3)-C3H5)(4)Pt4Cl4] loses the ally! ligand. XPS data show that in the fresh catalyst Pt is present in the 2+ oxidation state. Based on these and analytical data, co-ordination by surface diamine and hydroxo groups to Pt2+ in 1 is suggested. In the used catalyst both Pt2+ and Pt are present but the amount of metallic platinum is similar to 16\% of the total. (C) 2011 Elsevier B.V. All rights reserved.

}, keywords = {Chloronitrobenzenes, Dehydrohalogenation, heterogeneous catalyst, MCM-41, Selective hydrogenation}, issn = {0926-860X}, doi = {10.1016/j.apcata.2011.03.044}, author = {Indra, Arindam and Rajamohanan, Pattuparambil R. and Gopinath, Chinnakonda S. and Bhaduri, Sumit and Lahiri, Goutam Kumar} } @article { ISI:000311180800010, title = {Effect of particle size on selective hydrogenation of cinnamaldehyde by Pt encapsulated in mesoporous silica}, journal = {Catalysis Communications}, volume = {28}, year = {2012}, month = {NOV}, pages = {42-46}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Pt nanoparticles of various sizes, viz. 8. 4.9, 3.6 and 1.8 nm were encapsulated in 2D hexagonal mesoporous silica by in-situ synthesis as well as post synthetic modifications so that the final catalyst composition was \<= 1 wt.\% Pt/SiO2. A kinetic analysis of the effect of particle size on selective hydrogenation of cinnamaldehyde was carried out on these catalysts. It was found that the materials, even at such low loading of Pt, were very active for the hydrogenation and selective for the desired product, cinnamyl alcohol. Among the different particle sizes, selectivity was found to be the highest on 8 nm particles. Kinetic analysis shows that the reaction follows a consecutive reaction pathway. (C) 2012 Elsevier B.V. All rights reserved.

}, keywords = {alpha, beta-Unsaturated aldehydes, Cinnamaldehyde hydrogenation, Kinetic analysis, Mesoporous silica, Pt nanoparticles, Selective hydrogenation}, issn = {1566-7367}, doi = {10.1016/j.catcom.2012.08.017}, author = {Prashar, Atul K. and Mayadevi, S. and Devi, R. Nandini} } @article { ISI:000327481200002, title = {Noble metal promoted CeO2-ZrO2-supported ni catalysts for liquid-phase hydrogenation of cinnamaldehyde}, journal = {Catalysis Letters}, volume = {143}, number = {12}, year = {2013}, month = {DEC}, pages = {1266-1276}, publisher = {SPRINGER}, address = {233 SPRING ST, NEW YORK, NY 10013 USA}, abstract = {

Pd or Pt promoted CeO2-ZrO2-supported Ni catalysts exhibited superior catalytic activity to the hitherto known Ni catalysts for liquid-phase hydrogenation of cinnamaldehyde at moderate conditions. Under similar experimental conditions, the unpromoted catalyst was selective for hydrocinnamaldehyde product (C=C hydrogenation) whereas the promoted catalyst yielded 3-phenyl propanol (C=C and C=O hydrogenation product). Enhanced dispersion of Ni was the cause for higher activity of the promoted Ni catalysts.

}, keywords = {Ceria-zirconia, Cinnamaldehyde, Noble metal promoted catalyst, Selective hydrogenation, Supported Ni catalyst}, issn = {1011-372X}, doi = {10.1007/s10562-013-1064-9}, author = {Bhogeswararao, Seemala and Kumar, V. Pavan and Chary, K. V. R. and Srinivas, D.} } @article {48031, title = {Highly efficient chemoselective hydrogenation of 5-HMF to BHMF over reusable bimetallic Pd-Ir/C catalyst}, journal = {ChemistrySelect}, volume = {7}, year = {2022}, month = {JUN}, pages = {e202200456}, type = {Article}, abstract = {

Catalytic synergism was observed for a bimetallic Pd-Ir catalyst supported on activated carbon for chemoselective hydrogenation of 5-hydroxymetahyl furfural (5-HMF) to 2, 5-(bishydroxymethyl) furan (BHMF) with complete conversion and 97 \% selectivity under very mild reaction conditions. The structural characterization like XRD, N-2 sorption, FE-SEM and TEM suggested formation of fine nanoparticles (1.95-3.08 nm) having very higher surface area, uniform distribution and mesoporous nature of the material. XPS spectra and Pyridine-IR spectroscopy revealed formation of Pd-PdO and Ir/IrO2/IrO3 interface on the catalytic surface along with strong Bronsted acidic sites which were responsible for high efficiency of catalyst at 80 degrees C, 100 psig H-2 pressure at 5-HMF/Catalyst=20 and within 2.5 h of reaction time. A plausible reaction mechanism is also elucidated based on structure activity correlation.

}, keywords = {5-HMF, Carbon, Catalytic synergism, Selective hydrogenation, Valorization}, issn = {2365-6549}, doi = {10.1002/slct.202200456}, author = {Ratrey, Geetanjali and Solanki, Bhanupratap S. and Kamble, Sanjay P. and Rode, V. Chandrashekhar} }