@article { ISI:000252529400025, title = {Incorporation of zirconium in medium-pore aluminophosphate molecular sieves with AEL framework}, journal = {Microporous and Mesoporous Materials}, volume = {108}, number = {1-3}, year = {2008}, month = {FEB}, pages = {223-229}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Zirconium incorporated alurninophosphate molecular sieves ZrAPO-11 was synthesized by hydrothermal method. The samples were characterized by X-ray diffraction (XRD), scanning electron microscopy, thermogravimetric/differential thermal analysis (TGA/DTA), diffuse reflectance UV-visible spectroscopy, magic-angle spinning nuclear magnetic resonance (MAS NMR) spectroscopy (P-31 and Al-27). The acidity of the materials were determined by temperature programmed desorption (TPD) of ammonia. X-ray diffraction and scanning electron microscopy reveals formation of crystalline material in pure phase. Thermal analysis shows higher template content in zirconium containing samples than the corresponding AlPOs. MAS NMR suggests incorporation of zirconium in the framework. TPD reveals that the ZrAPO-11 samples were of higher acidity than AIPO(4)-11 (c) 2007 Elsevier Inc. All rights reserved.

}, keywords = {AlPO4-11, Aluminophosphate, catalysis, Molecular sieve, ZrAPO-11}, issn = {1387-1811}, doi = {10.1016/j.micromeso.2007.03.044}, author = {Ganguli, J. N. and Chakrabortty, Dhruba and Satyanarayana, C. V. V.} } @article { ISI:000284557000009, title = {Incorporation of zirconium in medium-pore aluminophosphate molecular sieves with AFO framework}, journal = {Microporous and Mesoporous Materials}, volume = {137}, number = {1-3}, year = {2011}, month = {JAN}, pages = {65-71}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Zirconium substituted medium pore microporous aluminophosphate molecular sieve ZrAPO-41 was prepared by hydrothermal synthesis under autogenous pressure The formation of the pure phase was confirmed by powder X-ray diffraction (XRD) and scanning electron microscopy (SEM)The thermal behaviour of the material was investigated by carrying out thermogravimetric/differential thermal analysis (TGA/DTA) The zirconium environment was studied by magic-angle spinning nuclear magnetic resonance (MAS NMR) spectroscopy which suggests incorporation of zirconium into the framework UV-Visible diffuse reflectance study also supports the claim The temperature programmed desorption (TPD) of ammonia reveals that the acidity of ZrAPO 41 samples is higher than that of pure AlPO4-41 The catalytic activity of the samples was investigated through phenol hydroxylation reaction The result show hi E her catalytic activity for ZrAPO-41 samples compared to AlPO4-41 (C) 2010 Elsevier Inc All rights reserved

}, keywords = {AFO, Aluminophosphate, catalysis, Molecular sieve, ZrAPO 41}, issn = {1387-1811}, doi = {10.1016/j.micromeso.2010.08.022}, author = {Chakrabortty, Dhruba and Ganguli, J. N. and Satyanarayana, C. V. V.} } @article { ISI:000343715000091, title = {Influence of method of preparation on the activity of La-Ni-Ce mixed oxide catalysts for dry reforming of methane}, journal = {RSC Advances}, volume = {4}, number = {91}, year = {2014}, month = {OCT}, pages = {50226-50232}, publisher = {ROYAL SOC CHEMISTRY}, address = {THOMAS GRAHAM HOUSE, SCIENCE PARK, MILTON RD, CAMBRIDGE CB4 0WF, CAMBS, ENGLAND}, abstract = {

La-Ni-x-Ce1-x mixed oxide catalysts were prepared by a sol-gel method varying the Ni composition (0 \<= x \<= 1). The catalysts were characterized by X-ray diffraction (XRD), inductively coupled plasma optical emission spectroscopy (ICP-OES), BET surface area, X-ray photoelectron spectroscopy (XPS), temperature-programmed reduction (TPR), H-2 chemisorption and Fourier transform infrared spectroscopy (FT-IR) techniques. CO2 reforming of methane was carried out at atmospheric pressure and 800 degrees C, maintaining a reactant CO2/CH4/N-2 ratio of 80/80/80 (total flow rate = 240 ml min(-1), GHSV of 28 800 h(-1)). The catalysts offered higher activity even at lower Ni compositions. LaNi0.4Ce0.6O3. showed the highest conversion of CH4 and CO2. The H-2/CO ratio in the syngas was stable at 0.85 +/- 0.02. The performance of the sol-gel catalysts was compared with that of the hydrothermally prepared catalysts, reported earlier. High surface area and better Ni dispersion were found to be the reasons for superior activity of the sol-gel catalysts.

}, issn = {2046-2069}, doi = {10.1039/c4ra07098d}, author = {Sagar, T. V. and Sreelatha, N. and Hanmant, G. and Surendar, M. and Lingaiah, N. and Rao, K. S. Rama and Satyanarayana, C. V. V. and Reddy, I. A. K. and Prasad, P. S. Sai} } @article {46725, title = {Influence of cobalt on performance of Cu-CeO2 catalysts for preferential oxidation of CO}, journal = {Journal of Rare Earths}, volume = {38}, year = {2020}, month = {SEP}, pages = {941-950}, type = {Article}, abstract = {

{Copper and cobalt oxides supported on CeO2 were investigated for preferential oxidation of carbon monoxide (CO-PROX) in the presence of excess hydrogen and CO2. (CuO)(1-x)(Co3O4)(x/3)-(CeO2)(2.5) (x = 0, 0.25, 0.50, 0.75, 0.85 and 1) catalysts were prepared by coprecipitation method. These mixed oxide catalysts were characterized by several physicochemical techniques, such as BET surface area (SBET), X-ray diffraction (XRD), high resolution transmission electron microscopy (HRTEM), temperature programmed reduction (TPR) and X-ray photoelectron spectroscopy (XPS). XRD studies show the peaks related to CuO and Co3O4 phases in copper and cobalt containing CeO2 catalysts. The average particle size of the CeO2 crystallites is in the range of 8-10 nm as evaluated from HRTEM studies. XPS studies demonstrate that Cu, Co and Ce in (CuO)(1-x)(Co3O4)(x/3)-(CeO2)(2.5) catalysts are presented in +2 and +1, +3 and +2 and +4 and +3 oxidation states, respectively. The catalyst with x = 0.75 shows better activity and selectivity towards CO-PROX. Though the catalyst with only copper (CuO-CeO2

}, keywords = {CO-PROX, Cu-CeO2, H2O addition, Methanation, XPS, XRD}, issn = {1002-0721}, doi = {10.1016/j.jre.2019.08.001}, author = {Malwadkar, Sachin and Bera, Parthasarathi and Satyanarayana, C. V. V.} } @article {46968, title = {Insights into the catalytic activity of Ru/NaY catalysts for efficient H-2 production through aqueous phase reforming}, journal = {Sustainable Energy \& Fuels}, volume = {4}, year = {2020}, month = {FEB }, pages = {678-690}, type = {Article}, abstract = {

Ruthenium nanoparticles supported on NaY zeolite catalysts were synthesized by a simple ion exchange method. The structural and morphological features of the catalysts were systematically investigated using numerous techniques such as N-2-sorption, XRD, CO2-TPD, H-2-TPR, TEM, SEM, ICP-OES, TGA, CHN analysis, XPS, in situ CO-FTIR and NMR spectroscopy. These novel Ru-NaY catalysts were highly active and selective for H-2 production through aqueous phase reforming (APR) of glycerol and ethylene glycol. Among the various catalysts evaluated for H-2 production, the 3 wt\% Ru-NaY catalyst demonstrated the highest catalytic performance with excellent H-2 selectivity and this catalyst exhibits better activity as compared to many state of the art catalysts reported so far. The superior catalytic activity of 3 wt\% Ru-NaY was attributed to the appropriate Ru metal loading, good metal dispersion, small size of Ru nanoparticles, better metal-support interaction, and higher availability of catalytically active sites (Ru-0) and facilitated water gas shift (WGS) reaction. This catalytic activity result clearly shows that NaY zeolite supported Ru nanoparticles catalysts have excellent potential for H-2 production from biomass-derived compounds.

}, issn = {2398-4902}, doi = {10.1039/c9se00797k}, author = {Gogoi, Pranjal and Nagpure, Atul S. and Kandasamy, Prabu and Satyanarayana, C. V. V. and Raja, Thirumalaiswamy} }