@article { ISI:000230685200006, title = {Biphenyl hydrogenation over supported transition metal catalysts under supercritical carbon dioxide solvent}, journal = {Applied Catalysis A - General}, volume = {288}, number = {1-2}, year = {2005}, month = {JUL}, pages = {43-47}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Catalytic hydrogenation of biphenyl to bicyclohexyl, an organic hydrogen storage medium, was examined over supported transition metal catalysts in supercritical carbon dioxide solvent. The yield of bicyclohexyl was almost 100\% over the charcoal-supported rhodium (Rh/C) and ruthenium (Ru/C) catalysts at the temperature of 323 K, which was much lower than that required for biphenyl hydrogenation in organic solvents (573 K). The initial activity was higher over the Rh/C catalyst, while the initial selectivity to bicyclohexyl was higher over the Ru/C catalyst. The conversion of biphenyl increased with increase in hydrogen and carbon dioxide pressures, while the selectivity to bicyclohexyl was independent of hydrogen and carbon dioxide pressures over both catalysts. (c) 2005 Elsevier B.V. All rights reserved.

}, keywords = {bicyclohexyl, biphenyl, charcoal-supported rhodium catalyst, charcoal-supported ruthenium catalyst, Hydrogen storage, Hydrogenation, Supercritical carbon dioxide}, issn = {0926-860X}, doi = {10.1016/j.apcata.2005.04.021}, author = {Hiyoshi, Norihito and Rode, C. V. and Sato, O. and Shirai, M.} } @article { ISI:000227710300073, title = {Enhanced selectivity to decalin in naphthalene hydrogenation under supercritical carbon dioxide}, journal = {Chemistry Letters}, volume = {34}, number = {3}, year = {2005}, month = {MAR}, pages = {424-425}, publisher = {CHEMICAL SOC JAPAN}, type = {Article}, address = {1-5 KANDA-SURUGADAI CHIYODA-KU, TOKYO, 101-8307, JAPAN}, abstract = {

A charcoal-supported rhodium catalyst was highly active and selective to decalin for the hydrogenation of naphthalene at very low temperature (333 K) under supercritical carbon dioxide.

}, issn = {0366-7022}, doi = {10.1246/cl.2005.424}, author = {Hiyoshi, Norihito and Miura, R. and Rode, C. V. and Sato, O. and Shirai, M.} } @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:000230232100019, title = {Partial ring hydrogenation of naphthols over supported metal catalysts in supercritical carbon dioxide solvent}, journal = {Chemistry Letters}, volume = {34}, number = {6}, year = {2005}, month = {JUN}, pages = {782-783}, publisher = {CHEMICAL SOC JAPAN}, type = {Article}, address = {1-5 KANDA-SURUGADAI CHIYODA-KU, TOKYO, 101-8307, JAPAN}, abstract = {

Selective ring hydrogenation of naphthols to tetrahydronaphthols and tetralones proceeded at 323 K over a charcoal supported rhodium catalyst in supercritical carbon dioxide.

}, issn = {0366-7022}, doi = {10.1246/cl.2005.782}, author = {Mine, Eiichi and Haryu, E. and Arai, K. and Sato, T. and Sato, O. and Sasaki, A. and Rode, C. V. and Shirai, M.} } @article { ISI:000233067000013, title = {Preparation and characterization of a copper based Indian traditional drug: tamra bhasma}, journal = {Journal of Pharmaceutical and Biomedical Analysis}, volume = {39}, number = {5}, year = {2005}, month = {OCT}, pages = {951-955}, publisher = {PERGAMON-ELSEVIER SCIENCE LTD}, type = {Article}, address = {THE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, ENGLAND}, abstract = {

The copper based Indian traditional drug {\textquoteleft}tamra bhasma{\textquoteright} is administered for various ailments since long. Its synthesis involves treating metallic copper with plant juices and then repeated calcination in presence of air so that the metallic state is transformed into the corresponding oxide form traditionally known as {\textquoteleft}bhasma{\textquoteright}. In this work, we present a systematic characterization of this traditional drug using various techniques like X-ray diffraction (XRD), scanning electron microscopy (SEM)-energy dispersive X-ray analysis (EDX), X-ray photoelectron spectroscopy (XPS), infrared spectroscopy (IR), thermogravimetry (TG) and surface area measurement. The results obtained were found to match very well with those of a standard copper oxide confirming the composition of the drug sample. In addition, some specific findings were also made which could help in interpreting the therapeutic properties of the traditional drug {\textquoteleft}tamra bhasma{\textquoteright}. (c) 2005 Elsevier B.V. All rights reserved.

}, keywords = {copper oxide, crystallite size, tamra bhasma, traditional medicine, XPS of copper oxide, XRD}, issn = {0731-7085}, doi = {10.1016/j.jpba.2005.06.015}, author = {Wadekar, M. P. and Rode, C. V. and Bendale, Y. N. and Patil, K. R. and Prabhune, Asmita} } @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:000238491100062, title = {Effect of calcination cycles on the preparation of tin oxide based traditional drug: studies on its formation and characterization}, journal = {Journal of Pharmaceutical and Biomedical Analysis}, volume = {41}, number = {4}, year = {2006}, month = {JUN}, pages = {1473-1478}, publisher = {PERGAMON-ELSEVIER SCIENCE LTD}, type = {Article}, address = {THE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, ENGLAND}, abstract = {

The preparation method of metal based Indian traditional drugs involves conversion of a pure metal into its oxide by repeated high temperature calcination cycles. In this work, the effect of number of calcination cycles followed in the preparation of tin oxide based Ayurvedic drug, {\textquoteleft}vanga bhasma{\textquoteright} was studied by a systematic characterization of the drug samples after various calcination stages. It was found that tin was in the form of Sn4+ state and that the formation of SnO2 proceeded step-wise through Sn(OH)(4). (c) 2006 Elsevier B.V. All rights reserved.

}, keywords = {calcination cycles, Oxidation, oxidation state of tin, Particle size, tin oxide, vanga bhasma}, issn = {0731-7085}, doi = {10.1016/j.jpba.2006.03.032}, author = {Wadekar, M. P. and Rode, C. V. and Bendale, Y. N. and Patil, K. R. and Gaikwad, A. B. and Prabhune, Asmita} } @article { ISI:000238416100033, title = {Ring hydrogenation of naphthalene and 1-naphthol over supported metal catalysts in supercritical carbon dioxide solvent}, journal = {Catalysis Today}, volume = {115}, number = {1-4}, year = {2006}, note = {8th International Conference on Carbon Dioxide Utilization, Univ Oslo, Oslo, NORWAY, JUN 20-23, 2005}, month = {JUN}, pages = {248-253}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Catalytic ring hydrogenations of naphthalene and 1-naphthol were studied over several supported metal catalysts in supercritical carbon dioxide solvent at low temperature. Higher concentration of hydrogen in supercritical carbon dioxide and lower reaction temperature were responsible for higher catalyst activity and selectivities to the desired partial ring hydrogenated products as compared with those observed in organic solvent for the same catalyst. (c) 2006 Elsevier B.V. All rights reserved.

}, keywords = {1-naphthol, Hydrogenation, Naphthalene, Supercritical carbon dioxide, supported metal catalyst}, issn = {0920-5861}, doi = {10.1016/j.cattod.2006.02.048}, author = {Shirai, M. and Rode, C. V. and Mine, Eiichi and Sasaki, A. and Sato, O. and Hiyoshi, Norihito} } @article { ISI:000243163000025, title = {Bimetallic Pt-Sn/gamma-alumina catalyst for highly selective liquid phase hydrogenation of diethyl succinate to gamma-butyrolactone}, journal = {Catalysis Communications}, volume = {8}, number = {3}, year = {2007}, month = {MAR}, pages = {340-344}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Platinum-tin bimetallic catalyst on gamma-alumina support was prepared by impregnation method and was reduced by sodium borohydride at room temperature. XRD and XPS characterization revealed that platinum was reduced to Pt-0 while, tin was probably partially reduced to Sn2+ due to the low temperature reduction method and Sn-0 was completely absent, avoiding the formation of P-Sn alloy. Pt-Sn/gamma-alumina (Pt 1\%, Sn 9\%) thus prepared was found to give almost complete selectivity to gamma-butyrolactone in liquid phase hydrogenation of diethyl succinate. A plausible reaction pathway is proposed involving Pt-O-Sn state and high selectivity to GBL is due to the Lewis acidity of Sn2+/4+ (c) 2006 Elsevier B.V. All rights reserved.

}, keywords = {bimetallic Pt-Sn catalyst, gamma-butyrolactone selectivity, liquid phase hydrogenation of diethyl maleate, XPS of Pt-Sn, XRD of Pt-Sn}, issn = {1566-7367}, doi = {10.1016/j.catcom.2006.06.026}, author = {Vaidya, S. H. and Rode, C. V. and Chaudhari, Raghunath V.} } @article { ISI:000250026200021, title = {Synthesis of tinidazole by condensation-oxidation sequence using MoO3/SiO2 bifunctional catalyst}, journal = {Catalysis Communications}, volume = {8}, number = {10}, year = {2007}, month = {OCT}, pages = {1550-1555}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Antimicrobial drug, tinidazole has been synthesized by condensation of 2-methyl,5-nitro-imidazole and 2-ethyl-thio-ethanol over MoO3/SiO2 catalyst to obtain 1-(2-ethyl-thio-ethanol)-2-methyl-5-nitro-imidazole which is further oxidized using hydrogen peroxide using the same MoO3/SiO2 catalyst to obtain tinidazole. MoO3/SiO2 catalyst (20\%), synthesized by sol-gel process showed the highest acid strength and was successfully demonstrated to catalyze both condensation and oxidation in the synthesis of tinidazole. Due to the bifunctional activity of the catalyst, the use of acetic acid for condensation step and tungstic acid or ammonium molybdate for oxidation step in the conventional synthesis of tinidazole could be eliminated, thus making it an environmentally benign process. The catalysts could be recycled five times without any appreciable loss in the conversion and selectivity showing the potential for. the use of MoO3/SiO2 as bifunctional catalyst for the production of this industrially important compound. (C) 2007 Elsevier B.V. All rights reserved.

}, keywords = {antimicrobial drug, condensation, MoO3/SiO2, Oxidation, solid acid catalyst, tinidazole}, issn = {1566-7367}, doi = {10.1016/j.catcom.2007.01.001}, author = {Chandorkar, J. G. and Shubhangi B. Umbarkar and Rode, C. V. and Kotwal, V. B. and Dongare, Mohan K.} } @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:000259602400109, title = {Manufacturing of tinidazole by recovering and recycling catalyst}, journal = {Asian Journal of Chemistry}, volume = {20}, number = {4}, year = {2008}, month = {APR}, pages = {3289-3291}, publisher = {ASIAN JOURNAL OF CHEMISTRY}, address = {11/100 RAJENDRA NAGAR, SECTOR 3,, SAHIBABAD 201 005, GHAZIABAD, INDIA}, abstract = {

In this paper, the recycle process of tungstic acid by recovering it from waste during the manufacture of tinidazole is described. The recovered tungstic acid gives desired quality and quantity of tinidazole.

}, keywords = {Recovery, tinidazole, tungstic acid}, issn = {0970-7077}, author = {Dongare, Mohan K. and Chandorkar, J. G. and Rode, C. V.} } @article { ISI:000255455300004, title = {Reaction kinetics of liquid phase air oxidation of p-cresol to p-hydroxybenzaldehyde}, journal = {Applied Catalysis A-General}, volume = {339}, number = {1}, year = {2008}, month = {APR}, pages = {28-35}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The kinetics of liquid phase oxidation of p-cresol to p-hydroxybenzaldehyde has been investigated using insoluble cobalt oxide (CO3O4) catalyst at oxygen partial pressures in the range 0.1-1.5 MPa, reaction temperatures 333-393 K, p-cresol concentrations 0.49-1.53 kmol/m(3) and catalyst loadings 0.38-3.03 kg/m(3). The effects of oxygen partial pressure, reaction temperature, p-cresol concentration and catalyst loading on the initial rate of reaction have been studied. The initial rate varied linearly with catalyst loading up to 1.5 kg/m(3) beyond which it was independent of the catalyst loading while first-order dependence was observed with variation in oxygen partial pressure. A rate expression has been proposed considering Langmuir-Hinshelwood (LH) type mechanism, based on the initial rate data. A batch reactor model was also developed based on the kinetics studied and the concentration time profile predicted by the model was in good agreement with the experimental data. The activation energy for the liquid phase oxidation of p-cresol was found to be 39.6 kJ/mol. (c) 2008 Elsevier B.V. All rights reserved.

}, keywords = {Co3O4, kinetics, p-cresol oxidation, XPS, XRD}, issn = {0926-860X}, doi = {10.1016/j.apcata.2008.01.006}, author = {Kshirsagar, V. S. and Nadgeri, J. M. and Tayade, P. R. and Rode, C. V.} } @article { ISI:000259602400108, title = {Recovery of ammonical salts from mother liquid of 2-methyl-5-nitroimidazole}, journal = {Asian Journal of Chemistry}, volume = {20}, number = {4}, year = {2008}, month = {APR}, pages = {3287-3288}, publisher = {ASIAN JOURNAL OF CHEMISTRY}, address = {11/100 RAJENDRA NAGAR, SECTOR 3,, SAHIBABAD 201 005, GHAZIABAD, INDIA}, abstract = {

An attempt have been made to recover the ammonical salt (ammonium sulphate and ammonium nitrate) from the mother liquid of 2-methyl-5-nitroimidazole successfully.

}, keywords = {2-methyl-5-nitroimidazole, ammonium nitrate, ammonium sulphate, Recovery}, issn = {0970-7077}, author = {Dongare, Mohan K. and Rode, C. V. and Chandorkar, J. G.} } @article { ISI:000260941700137, title = {Zinc oxide nanoparticles as novel alpha-amylase inhibitors}, journal = {Journal of Applied Physics}, volume = {104}, number = {9}, year = {2008}, month = {NOV}, pages = {094907}, publisher = {AMER INST PHYSICS}, type = {Article}, address = {CIRCULATION \& FULFILLMENT DIV, 2 HUNTINGTON QUADRANGLE, STE 1 N O 1, MELVILLE, NY 11747-4501 USA}, abstract = {

Amylase inhibitors, also known as starch blockers, contain substances that prevent dietary starches from being absorbed by the body via inhibiting breakdown of complex sugars to simpler ones. In this sense, these materials are projected as having potential applications in diabetes control. In this context, we report on zinc oxide nanoparticles as possible alpha-amylase inhibitors. Zinc oxide nanoparticles have been synthesized using soft-chemistry approach and 1-thioglycerol was used as a surfactant to yield polycrystalline nanoparticles of size similar to 18 nm, stabilized in wurtzite structure. Conjugation study and structural characterization have been done using x-ray diffraction technique, Fourier transform infrared spectroscopy, UV-visible spectroscopy, and transmission electron microscopy. Cytotoxicity studies on human fibrosarcoma (HT-1080) and skin carcinoma (A-431) cell lines as well as mouse primary fibroblast cells demonstrate that up to a dose of 20 mu g/ml, ZnO nanoparticles are nontoxic to the cells. We report for the first time the alpha-amylase inhibitory activity of ZnO nanoparticles wherein an optimum dose of 20 mu g/ml was sufficient to exhibit 49\% glucose inhibition at neutral pH and 35 degrees C temperature. This inhibitory activity was similar to that obtained with acarbose (a standard alpha-amylase inhibitor), thereby projecting ZnO nanoparticles as novel alpha-amylase inhibitors. (C) 2008 American Institute of Physics. [DOI: 10.1063/1.3009317]

}, issn = {0021-8979}, doi = {10.1063/1.3009317}, author = {Dhobale, Sandip and Thite, Trupti and Laware, S. L. and Rode, C. V. and Koppikar, Soumya J. and Ghanekar, Ruchika-Kaul and Kale, Sangeeta N.} } @article { ISI:000271982400003, title = {Characterization of clay intercalated cobalt-salen catalysts for the oxidation of p-cresol}, journal = {Applied Catalysis A-General}, volume = {370}, number = {1-2}, year = {2009}, month = {NOV}, pages = {16-23}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The intercalation of cobalt-salen complexes into the interlamelar spaces of montmorillonite clay was investigated by various characterization studies. The {\textquoteleft}{\textquoteleft}neat{\textquoteright}{\textquoteright} cobalt-salen complex showed a weight loss at 368 degrees C while the weight loss for the corresponding intercalated complex was observed at much higher temperature of 492 degrees C due to decomposition of the complex. The thermal stabilization observed was due to the host-guest interaction of clay and metal complex and thus confirmed the intercalation. The XANES spectrum of Co(salen)-mont sample revealed the change of symmetry from the tetrahedral in plane to the octahedral structure having an axial bonding of oxygen to the cobalt, indicating that cobalt atoms in Co(salen)-mont were coordinated axially with the lattice oxygen of montmorillonite. Both XANES and EXAFS results indicated that cobalt atoms in Co(salen)-mont form two additional Co-O bonds with a bond length of 0.199 nm by the intercalation while retaining the Co-salen structure. Co-salen intercalated into the montmorillonite clay showed the highest activity for the air oxidation of p-cresol, giving 88\% selectivity to the oxidation products. Effects of NaOH concentration and various solvents on the conversion and selectivity patterns also have been studied. (C) 2009 Elsevier B.V. All rights reserved.

}, keywords = {Cobalt-oxygen bond, Cobalt-salen, Extended X-ray absorption fine structure, Intercalation, Lattice oxygen, Montmorillonite, X-ray absorption near edge structure}, issn = {0926-860X}, doi = {10.1016/j.apcata.2009.09.003}, author = {Kshirsagar, V. S. and Garade, Ajit C. and Mane, R. B. and Patil, K. R. and Yamaguchi, A. and Shirai, M. and Rode, C. V.} } @article { ISI:000263864900016, title = {Efficient gamma-Fe2O3 catalyst for liquid phase air oxidation of p-hydroxybenzyl alcohol under mild conditions}, journal = {Catalysis Communications}, volume = {10}, number = {5}, year = {2009}, month = {JAN}, pages = {485-489}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

gamma-Fe2O3 (maghemite) particles were synthesized at 5 degrees C (LT, low temperature) and 95 degrees C (HT, high temperature) using a simple chemical protocol. The major reflection in XRD was observed to be of the gamma-Fe2O3 phase which was further supported by the XPS analysis. Fe3+ species were responsible for initiation of the oxidation of p-hydroxybenzyl alcohol. SEM revealed that the morphologies of the catalysts were different for samples prepared at two different temperatures. gamma-Fe2O3 (LT) showed the highest catalyst activity (84\% conversion) for liquid phase air oxidation of p-hydroxybenzyl alcohol with 94\% selectivity to the oxidation products at 370 K and ambient pressure conditions. (C) 2008 Elsevier B.V. All rights reserved.

}, keywords = {Air oxidation, gamma-Fe2O3, p-Hydroxybenzaldehyde, p-Hydroxybenzyl alcohol, scanning electron microscopy}, issn = {1566-7367}, doi = {10.1016/j.catcom.2008.10.044}, author = {Garade, Ajit C. and Bharadwaj, M. and Bhagwat, S. V. and Athawale, A. A. and Rode, C. V.} } @article { ISI:000262658000018, title = {Montmorillonite for selective hydroxyalkylation of p-cresol}, journal = {Applied Clay Science}, volume = {43}, number = {1}, year = {2009}, month = {JAN}, pages = {113-117}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Performances of montmorillonite titanium silicate (TS-1) and dodecatungstophosphoric acid (DTP) were compared for the hydroxyalkylation of p-cresol into dihydroxydiarylmethane (DAM). Ammonia TPD studies of various catalysts showed that an appropriate combination of both strong and weak acid sites of montmorillonite was mainly responsible rather than only the stronger acidity of bulk DTP for its highest catalytic activity for selective hydroxyalkylation of p-cresol to DAM. The selectivity to DAM could be enhanced by adjusting reaction conditions like mole ratio of p-cresol to formaldehyde, reaction temperature, catalyst concentration, solvent and reaction time. (C) 2008 Elsevier B.V. All rights reserved.

}, keywords = {Ammonia TPD, Dihydroxydiarylmethane, Hydroxyalkylation, Montmorillonite, Solid acids}, issn = {0169-1317}, doi = {10.1016/j.clay.2008.07.015}, author = {Garade, Ajit C. and Mate, Vivek R. and Rode, C. V.} } @article { ISI:000263491600023, title = {Selective hydroxyalkylation of phenol to bisphenol F over dodecatungstophosphoric acid (DTP) impregnated on fumed silica}, journal = {Applied Catalysis A-General}, volume = {354}, number = {1-2}, year = {2009}, month = {FEB}, pages = {176-182}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The catalyst activity of various solid acids, such as fumed Silica (SiO(2)) dodecatungstophosphoric acid (DTP), DTP impregnated on SiO(2), amberlyst-15 and montmorillonite KSF/0, was studied for the hydroxyalkylation of phenol to bisphenol F. A well-dispersed DTP on SiO2 catalyst was prepared by the wet impregnation method. The effect of DTP loading on SiO(2) was also compared with bulk DTP and other solid acid catalysts. 20\% DTP/SiO(2) catalyst gave the highest products yield of 34.2\% and selectivity of 90.1\% to bisphenol F, at 353 K and with a phenol-to-formaldehyde mole ratio of 5:1. Ammonia TPD studies of various catalysts showed that an appropriate combination of both strong and weak acid sites of DTP/SiO(2) Was mainly responsible, rather than only the stronger acidity of bulk DTP, for its highest catalytic activity and selectivity. The effect of various reaction parameters like mole ratio, catalyst concentration, temperature and reaction time on product yield and bisphenol F selectivity was also investigated. The catalyst recycle was established by catalyst activity testing. (C) 2008 Elsevier B.V. All rights reserved.

}, keywords = {Bisphenol F, Hydroxyalkylation, NH(3)-TPD, Reaction pathways, solid acid catalysts}, issn = {0926-860X}, doi = {10.1016/j.apcata.2008.11.025}, author = {Garade, Ajit C. and Kshirsagar, V. S. and Rode, C. V.} } @article { ISI:000270338700005, title = {Solid acid catalysts: modification of acid sites and effect on activity and selectivity tuning in various reactions}, journal = {Catalysis Surveys from Asia}, volume = {13}, number = {3}, year = {2009}, month = {SEP}, pages = {205-220}, publisher = {SPRINGER/PLENUM PUBLISHERS}, address = {233 SPRING ST, NEW YORK, NY 10013 USA}, abstract = {

The effects of acidity and variation in concentration of acid sites of dodecatungstophosphoric acid (DTP), supported DTP and montmorillonite-K catalysts were studied for various organic reactions such as the hydroxyalkylation of phenols to bisphenols, intramolecular rearrangement of benzyl phenyl ether (BPE) to 2-benzyl phenol (2-BP) and selective cleavage of tert-butyldimethylsilyl (TBDMS) ether into the corresponding alcohol. Both dodecatungstophosphoric acid (DTP) impregnated on silica (SiO(2)) and montmorillonite catalysts showed the highest catalyst activity with 90-95\% selectivity to bisphenol for the hydroxyalkylation of phenols to give bisphenol. Temperature Programmed Desorption (TPD) of ammonia and activity results of various catalysts showed that an appropriate combination of both strong and weak acidic sites in the catalyst was highly desirable for high bisphenol selectivity. A 10\% DTP/SiO(2) catalyst was found to be highly selective for the cleavage of TBDMS ether into the corresponding alcohol at room temperature giving a high TON of 9.5 x 10(5) even after the 4th recycle. DTP was also found to be a promising solid acid catalyst for the intramolecular rearrangement of BPE giving 2-BP.

}, keywords = {Acidity tuning, Catalytic cleavage, Hydroxyalkylation, Intramolecular rearrangement, solid acid catalysts}, issn = {1571-1013}, doi = {10.1007/s10563-009-9078-4}, author = {Rode, C. V. and Garade, Ajit C. and Chikate, Rajeev C.} } @article { ISI:000276010700025, title = {Acidity tuning of montmorillonite K10 by impregnation with dodecatungstophosphoric acid and hydroxyalkylation of phenol}, journal = {Applied Clay Science}, volume = {48}, number = {1-2, SI}, year = {2010}, month = {MAR}, pages = {164-170}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Acidity tuning of montmorillonite K10 (mont K10) was achieved by impregnating with dodecatungstophosphoric acid (DTP). The effect on the hydroxyalkylation of phenol was studied at 353 K with phenol to formaldehyde molar ratio of 5. The nature and strength of acid sites were determined by NH(3)-TPD measurement while the distribution of Brensted and Lewis acid sites expressed as B/L ratio, was determined by pyridine IR technique. Among various loadings of DTP (5-60\%) studied for the hydroxyalkylation of phenol, 20\% DTP/mont K10 showed the highest catalyst activity (90\% selectivity to bisphenol F with 28\% conversion of phenol). Both total concentration of acid sites and the distribution of acid sites in a high temperature region were required for the high bisphenol F selectivity. Our catalyst (20\% DTP/Mont K10) could be recycled three times. (C) 2009 Elsevier B.V. All rights reserved.

}, keywords = {Acidity tuning, Dodecatungstophosphoric acid/Montmorillonite K10, Hydroxyalkylation, Impregnation, Temperature programmed desorption}, issn = {0169-1317}, doi = {10.1016/j.clay.2009.11.042}, author = {Garade, Ajit C. and Kshirsagar, V. S. and Mane, R. B. and Ghalwadkar, Ajay A. and Joshi, U. D. and Rode, C. V.} } @article { ISI:000279333000002, title = {Structure-activity studies of dodecatungstophosphoric acid impregnated bentonite clay catalyst in hydroxyalkylation of p-cresol}, journal = {Catalysis Communications}, volume = {11}, number = {11}, year = {2010}, month = {JUN}, pages = {942-945}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Bentonite clay impregnated with dodecatungstophosphoric acid (20\% DTP/BNT) showed an excellent activity, selectivity and stability [95\% product yield with 94\% selectivity to 2, 2{\textquoteright}-methylenebis (4-methylphenol), DAM] for the hydroxyalkylation of p-cresol with formaldehyde at 353 K and for a mole ratio of 5. Ammonia-TPD results showed that an increase in total concentration of acid sites from 4.9 of parent bentonite to 11.6 micromoles per surface area NH(3) (mu molS(-1) NH(3)) of 20\% DTP/BNT was due to a strong interaction of protons of bulk DTP with surface hydroxyl groups of BNT as evidenced by (31)P NMR studies. (C) 2010 Elsevier B.V. All rights reserved.

}, keywords = {(31)P CPMAS NMR, Bentonite, Hydroxyalkylation, p-Cresol, surface modification}, issn = {1566-7367}, doi = {10.1016/j.catcom.2010.04.008}, author = {Garade, Ajit C. and Kshirsagar, V. S. and Jha, Ajay and Rode, C. V.} } @article { ISI:000289716300080, title = {Role of promoters in copper chromite catalysts for hydrogenolysis of glycerol}, journal = {Catalysis Today}, volume = {164}, number = {1}, year = {2011}, note = {1st Joint International Conference of the 8th Tokyo Conference on Advanced Catalytic Science and Technology/5th Asia Pacific Congress on Catalysis, Sapporo, JAPAN, JUL 18-23, 2010}, month = {APR}, pages = {447-450}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Various copper chromite catalysts with and without promoters were prepared by simultaneous co-precipitation and digestion technique and the role of promoters (Al, Ba and Zn) was investigated for hydrogenolysis of glycerol to 1,2-propylene glycol (1,2-PG) in both batch and continuous operations. Among various promoters studied, copper chromite catalyst with Ba as a promoter showed the highest activity and selectivity of 85\% to 1,2-PG. This catalyst was found to be active for more than 800 h in a continuous operation also. Ammonia TPD results showed that barium promoted copper chromite catalyst had the highest acidity which facilitates the dehydration of glycerol to acetol which is the first step in hydrogenolysis of glycerol to 1,2-PG. The effect of barium content and variation in the promoters combination was also studied. (C) 2010 Elsevier B.V. All rights reserved.

}, keywords = {1, 2-Propylene glycol, Acetol, Ammonia TPD, Glycerol hydrogenolysis, Surface acidity}, issn = {0920-5861}, doi = {10.1016/j.cattod.2010.10.032}, author = {Mane, R. B. and Ghalwadkar, Ajay A. and Hengne, Amol M. and Suryawanshi, Y. R. and Rode, C. V.} } @article { ISI:000306358100005, title = {Copper modified waste fly ash as a promising catalyst for glycerol hydrogenolysis}, journal = {Catalysis Today}, volume = {190}, number = {1}, year = {2012}, month = {AUG}, pages = {31-37}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Several catalyst formulations using waste fly ash along with Cu were prepared and characterised by XRD, BET and TEM. These catalysts were also evaluated for the first time for hydrogenolysis of glycerol to 1,2 propanediol (1,2-PDO) in a batch reactor under 52 bar H-2 pressure in the temperature range of 473-513 K conditions. The fly ash pretreated by alkali using the fusion method and impregnated with Cu showed higher activity and stability for glycerol hydrogenolysis. Due to pretreatment with alkali at high temperature, transformation of alpha-quartz to the tridymite phase of SiO2 occurred. More importantly, use of alkali either during the pretreatment or the Cu loading step resulted in a high dispersion on the surface which was responsible for higher glycerol conversion and 1,2-PDO selectivity. The effects of temperature, Cu loading and solvent on glycerol conversion and product selectivities were also studied in this work. (C) 2011 Elsevier B.V. All rights reserved.

}, keywords = {1, 2-Propanediol, Alkali fusion, Cu loading, Fly ash, Glycerol hydrogenolysis}, issn = {0920-5861}, doi = {10.1016/j.cattod.2011.11.038}, author = {Rode, C. V. and Mane, R. B. and Potdar, A. S. and Patil, P. B. and Niphadkar, P. S. and Joshi, P. N.} } @article { ISI:000311350000043, title = {Effect of preparation parameters of Cu catalysts on their physico-chemical properties and activities for glycerol hydrogenolysis}, journal = {Catalysis Today}, volume = {198}, number = {1, SI}, year = {2012}, month = {DEC}, pages = {321-329}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Cu based catalysts were prepared by co-precipitation, alkali fusion followed by precipitation and direct solid state fusion methods. The changes in the phase formation, morphology, crystallite size, extent of aggregation, strength and nature of acid sites were observed due to variations in precipitating agents and also their order of addition. The catalyst prepared by co-precipitation using Na2CO3 showed the predominant presence of metallic Cu phase with a crystallite size of 5 nm, well segregated spherical morphology and highest acidity in the activated sample. These intrinsic properties contributed to achieve the highest glycerol conversion of 62\% and 1,2-PDO selectivity of 88\% in glycerol hydrogenolysis. (C) 2012 Elsevier B.V. All rights reserved.

}, keywords = {Co-precipitation, Cu catalysts, Glycerol hydrogenolysis, Physico-chemical properties, Solid state fusion}, issn = {0920-5861}, doi = {10.1016/j.cattod.2012.05.051}, author = {Mane, R. B. and Kondawar, S. E. and Niphadkar, P. S. and Joshi, P. N. and Patil, K. R. and Rode, C. V.} } @article { ISI:000317945100020, title = {Metal cation-exchanged montmorillonite clay as catalysts for hydroxyalkylation reaction}, journal = {Applied Clay Science}, volume = {74}, number = {SI}, year = {2013}, month = {APR}, pages = {141-146}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Several solid acid catalysts were prepared by exchanging metal cations such as Zn2+, Fe3+ and Al3+ with montmorillonite clay. Among these, Al-montmorillonite showed the highest acidity determined by the pyridine-IR as well as NH3-TPD methods. A systematic comparison of the performance of these catalysts along with parent montmorillonite was carried out for the hydroxyalkylation of p-cresol with formaldehyde to give 2, 2{\textquoteright}-methylenebis (4-methyl phenol) (DAM). It was found that the activity of these catalysts was in accordance with the increase in acidity of parent montmorillonite after the exchange of cations in the order of Zn2+, Fe3+ and Al3+. The selectivity pattern was also influenced by the exchanged cations. Since Al-montmorillonite showed the highest conversion of 51\% with 98\% selectivity to DAM, the effects of various reaction parameters, namely, mole ratio, catalyst concentration, temperature, reaction time on conversion and selectivity pattern were also studied using the same catalyst This catalyst also showed an excellent stability as evidenced by its eight times reuse. (C) 2012 Published by Elsevier B.V.

}, keywords = {Cations-exchanged clay, Montmorillonite, NH3-TPD, Pyridine-IR}, issn = {0169-1317}, doi = {10.1016/j.clay.2012.10.005}, author = {Jha, Ajay and Garade, Ajit C. and Shirai, M. and Rode, C. V.} } @article { ISI:000345479000014, title = {Effect of preparation parameters on characterization and activity of Co3O4 catalyst in liquid phase oxidation of lignin model substrates}, journal = {Applied Catalysis A-General}, volume = {487}, year = {2014}, month = {OCT}, pages = {130-138}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The nano structured spinel cobalt oxide (Co3O4) was prepared via simple co-precipitation method and its catalytic activity was evaluated for the liquid phase aerobic oxidation of lignin sub structure compounds such as veratryl alcohol. Catalyst preparation parameters influenced its morphology eventually affecting its oxidation activity. Thus, nano rod shaped CO3O4 catalyst showed 75\% and 38\% conversion of veratryl alcohol with complete selectivity to veratryl aldehyde in toluene and water, respectively, under base free condition. The influence of reaction conditions, such as temperature, oxygen pressure and catalyst loading was studied to obtain the optimum product yield and selectivity to the desired product. Furthermore, oxidation of various sub-structures of lignin model compounds was also studied over the same catalyst which was found to be in the following order: secondary alcohol \>di-substituted \> tri-substituted \> monosubstituted \> non-substitution. The stability of the catalyst was confirmed by its successful recycle for three times. (c) 2014 Elsevier B.V. All rights reserved.

}, keywords = {Coniferyl alcohol, Nano Co3O4, Sinapyl alcohol, TPR, Veratryl alcohol}, issn = {0926-860X}, doi = {10.1016/j.apcata.2014.08.023}, author = {Mate, Vivek R. and Jha, Ajay and Joshi, U. D. and Patil, K. R. and Shirai, M. and Rode, C. V.} } @article { ISI:000328665300008, title = {Effect of SnO2/Al2O3 ratio of Si-based MFI on its acidity and hydrophobicity: application in selective hydroxyalkylation of p-cresol}, journal = {Catalysis Communications}, volume = {44}, number = {SI}, year = {2014}, month = {JAN}, pages = {29-34}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Silica based MR type molecular sieves with various SnO2/Al2O3 ratios were synthesized from gels having molar compositions SiO2:xSnO(2):yAl(2)O(3):0.23(TPA)(2)O:35H(2)O where 0 \<= x \<= 0.02 and 0 \<= y \<= 0.01. Recyclable, Al-free Sn-MFI catalyst showed 31\% conversion of formaldehyde with 100\% selectivity to 2,2{\textquoteright}-methylenebis(4-methylphenol) in hydroxyalkylation of p-cresol with formaldehyde on account of moderate acidity and higher hydrophobicity. (C) 2013 Elsevier B.A. All rights reserved.

}, keywords = {Al-27 MAS NMR, Hydroxyalkylation, Molecular sieves, p-Cresol, Stannosilicate}, issn = {1566-7367}, doi = {10.1016/j.catcom.2013.08.002}, author = {Garade, Ajit C. and Malwadkar, A. V. and Niphadkar, P. S. and Jha, Ratnesh Kumar and Joshi, P. N. and Rode, C. V.} } @article {45929, title = {Solvent-free carbonylation of glycerol with urea using metal loaded MCM-41 catalysts}, journal = {RSC Advances}, volume = {5}, year = {2015}, month = {JAN}, pages = {16452-16460}, type = {Article}, abstract = {

Reacting glycerol with urea is the most attractive option for the production of glycerol carbonate (GC) as it utilizes two inexpensive chemicals readily available in the chemical cycle. The overall result is the chemical fixation of carbon dioxide. A Zn/MCM-41(im) catalyst prepared by a wet impregnation method exhibited excellent activity for the reaction of glycerol and urea with 75\% glycerol conversion and 98\% selectivity to GC. Such excellent activity of the catalyst is explained based on the presence of both basic and acidic sites on the same catalyst which activates the glycerol and urea molecules, respectively.

}, issn = {2046-2069}, doi = {10.1039/c4ra11590b}, author = {Kondawar, S. E. and Potdar, A. S. and Rode, C. V.} } @article {43921, title = {Carbonylation of glycerol with urea to glycerol carbonate over supported Zn catalysts}, journal = {Applied Petrochemical Research}, volume = {7}, year = {2017}, month = {APR}, chapter = {41-53}, abstract = {

Glycerol carbonylation with urea is a very feasible option to produce glycerol carbonate with a net result of CO2 fixation through urea synthesis. The prerequisite of an efficient catalyst for this reaction is to possess both acid and basic sites together. Several acidic supports were screened for ZnO catalyst in this work and Zn/MCM-41 was found to exhibit the best activity and almost complete selectivity to glycerol carbonate (GC). Although, non-catalytic glycerol carbonylation resulted in GC formation but glycerol conversion achieved was twice with Zn/MCM-41 as a catalyst. Further to that increase in Zn loading from 2 to 5\% resulted in increase in glycerol conversion from 63 to 82\%. The prepared catalysts were characterized by XRD, NH3 and CO2-TPD and effects of reaction parameters such as catalyst loading, glycerol to urea mole ratio and temperature on glycerol conversion and GC selectivity in batch mode of operation were also studied. Time on stream activity of 5\% Zn/MCM-41 catalyst for continuous carbonylation of glycerol was also studied for ~100 h with an average conversion of ~55\% and complete selectivity to GC. This indicated five times lower productivity of GC per h due to lower residence time than that in a batch operation as compared to that of a continuous operation. Activation energy estimated from the Arrhenius plot was found to be 39.82 kJ mol-1 suggesting that the reaction is kinetically controlled. A reaction pathway mediated by acid and basic sites of the Zn/MCM-41 catalyst is also proposed.

}, keywords = {Acid{\textendash}base ratio, Continuous process, Glycerol carbonate, Glycerol-urea carbonylation, reaction pathway, Supported Zn, Zn loading}, issn = {2190-5533}, doi = {10.1007/s13203-017-0177-2}, author = {Kondawar, S. E. and Mane, R. B. and Vasishta, A. and More, S. B. and Dhengale, S. D. and Rode, C. V.} } @article {45697, title = {Effect of reduction protocol of Pd catalysts on product distribution in furfural hydrogenation}, journal = {ChemistrySelect}, volume = {2}, year = {2017}, month = {JAN}, pages = {24-32}, type = {Article}, abstract = {Single step conversion of furfural to ring hydrogenation and decarbonylation products, 2-methyltetrahydrofuran (2-MeTHF) and tetrahydrofuran (THF) in high selectivity was achieved by controlling the particle size of Pd/C catalyst. The particle size variation of Pd/C catalysts in the range of 3.8 to 22 nm could be achieved by employing different reducing agents. Of particular interest was the NaBH4 reduced catalyst (Pd-B/C), which gave the lowest crystallite size of 4.8 nm due to incorporation of B into the inner lattices of Pd-Pd. This phase was evidenced by a characteristic XRD peak of Pd-B at 2q=38.85 degrees as well as a shift of (111) peak (40.07 degrees) of Pd towards the lower value (39.8 degrees). As compared to formaldehyde reduced catalyst (Pd-F/C), Pd-B/C catalyst completely suppressed the formation of furfuryl alcohol to give > 65\% selectivity to 2-MeTHF and THF. At 180 degrees C, almost equal distribution of side chain hydrogenation and ring opening products, 2-MF (45\%) and PeDO (37 \%), respectively, was observed while, higher temperature clearly favoured ring hydrogenation and decarbonylation reactions to give 2-MeTHF and THF.}, doi = {10.1002/slct.201601790}, author = {Date, N. S. and Biradar, N. S. and Chikate, R. C. and Rode, C. V.} } @article {45746, title = {Tandem synthesis of glycidol via transesterification of glycerol with DMC over Ba-mixed metal oxide catalysts}, journal = {ACS Sustainable Chemistry \& Engineering}, volume = {5}, year = {2017}, month = {FEB}, pages = {1763-1774}, type = {Article}, abstract = {Glycerol carbonate (GC) and glycidol (GD) are commercial products possible from glycerol transformation, which has become a subject of great importance. Among several basic catalysts screened in this work, BaO showed the highest glycerol conversion of 71\% with almost complete selectivity to GC. A tandem synthesis of GD with a selectivity as high as 80\% with 98\% glycerol conversion could be achieved with mixed oxides of Ba and lanthanides (La and Ce) prepared by the coprecipitation method. Although BaO alone showed the highest basicity as measured by CO2 TPD, tuning of basicity by incorporation of CeO2 resulted in the formation of GD. Incorporation of Ba into the ceria matrix induced oxygen vacancies in the cerium oxide material. The presence of u"/v" doublets at 888.7 and 903.2 eV, respectively, in XPS of the Ba-Ce sample also confirmed the oxygen vacancies in the lattice. In this tandem approach to GD, the subsequent decarboxylation of initially formed GC was due to the presence of a CeO2 lattice with defects, which is known to be the best for CO2 adsorption. Increase in both catalyst loading and temperature showed a dramatic enhancement in GD selectivity. A plausible reaction pathway for the transesterification of glycerol with DMC to give GC followed by its decarboxylation to GD is also proposed based on the structural characterization and activity studies.}, doi = {10.1021/acssuschemeng.6b02520}, author = {Kondawar, S. E. and Patil, C. R. and Rode, C. V.} } @article {44149, title = {Two-phase system for the clean and high yield synthesis of furylmethane derivatives over- SO3H functionalized ionic liquids}, journal = {Green Chemistry}, volume = {19}, year = {2017}, month = {OCT}, pages = {4804-4810}, type = {Article}, abstract = {A new and effective unique two-phase reaction system is investigated for the high yield production of tri(furyl) methane from furfural and furan. This strategy includes the use of an acidic aqueous phase (water + -SO3H functionalized IL) and furan phase, which significantly suppresses polymer formation, thereby increasing the yield of tri(furyl) methane. Furan serves as a reactant as well as an extraction solvent for the recovery of the condensation products. For comparison, different -SO3H functionalized ionic liquids are prepared and their performances evaluated for the condensation of furan and furfural. The ionic liquids with alkyl chain linkers are found to be more effective and acidic than those with imidazolium linked N-sulfonic acids. In addition, an increase in carbon chain length between imidazole/tri-ethylamine/pyridine and -SO3H, increases the catalytic activity of the respective ionic liquids. Among the several prepared ionic liquids, the strongly acidic imidazolium based butylsulfonic acid 6 shows the best activity with a maximum condensation product yield of 84\%. This strategy offers a significantly high yield of the condensation products of furan and furfural compared to the traditional mineral acid route. The activity and stability of the -SO3H functionalized 6 is confirmed from seven successful recycles, in which there is no reduction in its activity. Finally, this new strategy is successfully extended for the condensation of furan derivatives (e. g. furan and 2-methylfuran) with several different aldehydes, ketones and alcohols.}, doi = {10.1039/c7gc01654a}, author = {Shinde, S. H. and Rode, C. V.} } @article {44428, title = {Cascade dehydrative amination of glycerol to oxazoline}, journal = {Catalysis Science \& Technology}, volume = {8}, year = {2018}, month = {JUL}, pages = {2954-2965}, abstract = {Transformation of biomass into valuable nitrogen-containing compounds is highly desired, yet less explored. Here, we report a simple and efficient method for the direct conversion of bioglycerol to oxazoline involving glycerol dehydration to acetol followed by its amination using an aqueous solution of ammonia. For the two-step strategy a non-noble metal Cu-Zr catalyst was developed, giving a glycerol to acetol conversion of 78\% followed by amination separately with 95\% selectivity to oxazoline. Moreover, we have demonstrated a single-pot oxazoline synthesis using Ru/C as the most stable catalyst to achieve 95\% selectivity to oxazoline without any leaching. XPS studies revealed the co-existence of multivalent Ru species in different percentages depending on the nature and structure of the support. These multivalent species (RuO2 and RuO3) have a synergistic effect on the activation of the carbonyl group, whereas Ru-0 is an active site for ammonia dissociation. NH3-TPD and Py-IR spectroscopy results also suggest that the presence of relatively moderate acid sites and a higher BrOnsted/Lewis acid ratio in the catalyst promote the selective production of oxazoline. The reaction pathway involves first glycerol dehydration to acetol. In the subsequent step, NH3 is dissociatively adsorbed on the catalyst surface and the imine thus formed is condensed with a second molecule of acetol to obtain oxazoline. The studied catalyst could be recycled successfully without any significant loss of catalytic activity.}, doi = {10.1039/c8cy00185e}, author = {Pandya, R. and Mane, R. and Rode, C. V.} } @article {45607, title = {Selective hydrogenolysis of 5-(hydroxymethyl)furfural over Pd/C catalyst to 2,5-dimethylfuran}, journal = {Journal of Saudi Chemical Society}, volume = {23}, year = {2019}, month = {MAY}, pages = {439-451}, type = {Article}, abstract = {

everal metal supported catalysts were prepared and evaluated for 5-(hydroxymethyl)furfural (5-HMF) hydrogenolysis to 2,5-dimethylfuran (2,5-DMF) which is a renewable potential fuel additive. Among the prepared catalysts, 3\%Pd/C showed excellent performance in terms of complete conversion of 5-HMF along with the highest selectivity of 99\% to 2,5-DMF. Detailed physico-chemical characterisation was done in order to understand structure-activity correlation. Uniformly dispersed Pd nanoparticles on activated carbon provided the adsorption surface to enhance the hydrogenation of 5-HMF. Reaction was well optimised and established by extensive study of different reaction parameters like temperature, pressure, reaction time, stirring effect, substrate loading and metal loading.

}, keywords = {Biomass, Fuel additive, heterogeneous catalysis, Hydrogenolysis, Palladium}, issn = {1319-6103}, doi = {10.1016/j.jscs.2018.08.009}, author = {Solanki, B. S. and Rode, C. V.} } @article {45624, title = {Stereoselective aromatic ring hydrogenation over supported rhodium catalysts in supercritical carbon dioxide solvent}, journal = {Chemical Record}, year = {2019}, month = {JAN}, type = {Article}, abstract = {The combination of supported rhodium metal catalysts and supercritical carbon dioxide solvent was effective for the stereoselective ring hydrogenations of aromatic compounds at low temperature. Higher solubility of hydrogen in supercritical carbon dioxide provides higher concentration of hydrogen on the rhodium surface, but lower that of the intermediate on rhodium surface, which suppresses the flipping of surface intermediate, leading to higher catalyst activities and cis selectivities to the corresponding ring-hydrogenated products as compared with those in organic solvents.}, doi = {10.1002/tcr.201800128}, author = {Shirai, M. and Hiyoshi, N. and Rode, C. V.} } @article {46682, title = {Cascade dehydrative amination of glycerol to oxazoline (vol 8, pg 2954, 2018)}, journal = {Catalysis Science \& Technology}, volume = {10}, year = {2020}, month = {OCT }, pages = {6740}, type = {Correction}, abstract = {

Correction for {\textquoteleft}Cascade dehydrative amination of glycerol to oxazoline{\textquoteright} by R. Pandyaet al.,Catal. Sci. Technol., 2018,8, 2954-2965, DOI: ;10.1039/C8CY00185E.

}, issn = {2044-4753}, doi = {10.1039/d0cy90089c}, author = {Pandya, R. and Mane, R. and Rode, C. V.} }