01415nas a2200169   4500008004100000022001400041245012500055210006900180260008100249300001400330490000700344520070200351100002001053700002201073700001801095856013201113       2005                        eng d  a0002-782000aConversion of fly ash - an environmentally detrimental waste to zeolite beta (BEA) for commercial catalytic applications0 aConversion of fly ash an environmentally detrimental waste to ze  a9600 GARSINGTON RD, OXFORD OX4 2DQ, OXON, ENGLANDbBLACKWELL PUBLISHINGcNOV  a3260-32630 v883 a<p>Zeolite beta (BEA) was synthesized hydrothermally using fly ash as a combined source of alumina and silica. The overall crystallization period required to obtain pure crystalline BEA zeolite was found to be slightly longer when fly ash was used. The physicochemical properties of BEA phases obtained using fly ash (FLBEA) and conventional source materials (CONBEA) were compared. The H/FLBEA catalyst has exhibited excellent catalytic performance in commercially important benzene isopropylation process. These results have demonstrated that converting fly ash into BEA zeolite not only alleviates the disposal problem but also turns an otherwise waste material into a marketable commodity.</p>1 aKasture, M., W.1 aBokade, Vijay, V.1 aJoshi, P., N.  uhttps://library.ncl.res.in/content/conversion-fly-ash-environmentally-detrimental-waste-zeolite-beta-bea-commercial-catalytic-001572nas a2200229   4500008004100000022001400041245012400055210006900179260007300248300001200321490000800333520073000341653001801071653002701089653002601116653001101142653000801153100002201161700001801183700001801201856012301219       2011                        eng d  a1387-181100aCharacterization of surface acid sites in tin-silicalite-1 (Sn-MFI) molecular sieve by X-ray photoelectron spectroscopy0 aCharacterization of surface acid sites in tinsilicalite1 SnMFI m  aPO BOX 211, 1000 AE AMSTERDAM, NETHERLANDSbELSEVIER SCIENCE BVcMAY  a236-2400 v1413 a<p>The nature, strength and density of surface acid sites in Sn-MFI molecular sieves with different Sn-content were characterized by N 1s high resolution photoelectron peak of chemisorbed pyridine in combination with pyridine-IR and TPAD. Two peaks emerged at 399.5 +/- 0.2 and 401.5 +/- 0.2 eV by deconvoluting composite N is peak were assigned to chemisorbed pyridine on weak and relatively strong Lewis acid sites, respectively. The relative percentage of strong Lewis acid sites was found to increase with the decrease of framework Sn content. A close agreement was observed between the ratios of weak Lewis acid sites to strong Lewis acid sites obtained from XPS and TPAD. (C) 2010 Elsevier Inc. All rights reserved.</p>10aLewis acidity10aPyridine chemisorption10aSiO2/SnO2 molar ratio10aSn-MFI10aXPS1 aNiphadkar, P., S.1 aPatil, K., R.1 aJoshi, P., N.  uhttps://library.ncl.res.in/content/characterization-surface-acid-sites-tin-silicalite-1-sn-mfi-molecular-sieve-x-ray-001896nas a2200277   4500008004100000022001400041245008600055210006900141260007300210300001000283490000800293520099500301653000601296653001801302653001801320653001501338653001201353653002801365100001701393700001701410700001901427700001801446700002201464700001801486856011401504       2012                        eng d  a0920-586100aCopper modified waste fly ash as a promising catalyst for glycerol hydrogenolysis0 aCopper modified waste fly ash as a promising catalyst for glycer  aPO BOX 211, 1000 AE AMSTERDAM, NETHERLANDSbELSEVIER SCIENCE BVcAUG  a31-370 v1903 a<p>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.</p>10a110a2-Propanediol10aAlkali fusion10aCu loading10aFly ash10aGlycerol hydrogenolysis1 aRode, C., V.1 aMane, R., B.1 aPotdar, A., S.1 aPatil, P., B.1 aNiphadkar, P., S.1 aJoshi, P., N.  uhttps://library.ncl.res.in/content/copper-modified-waste-fly-ash-promising-catalyst-glycerol-hydrogenolysis-002213nas a2200241   4500008004100000022001400041245010500055210006900160260007300229300001000302490000800312520137700320653002001697653000801717653001301725653001501738653001101753100002201764700002001786700001801806700001801824856012901842       2013                        eng d  a1387-181100aCrystallization kinetics of Sn-MFI molecular sieve formation by dry gel cross mark conversion method0 aCrystallization kinetics of SnMFI molecular sieve formation by d  aPO BOX 211, 1000 AE AMSTERDAM, NETHERLANDSbELSEVIER SCIENCE BVcDEC  a73-800 v1823 a<p>The conversion of amorphous stannosilicate dry gel into crystalline molecular sieve with MFI structure (Sn-MFI) was achieved by dry gel conversion (DGC) method at 413, 443 and 473 K. For comparison purpose, Sn-MFI molecular sieve with similar SiO2/SnO2 mole ratio was also obtained by hydrothermal crystallization route. Crystallization curves were established by conducting time dependant studies on progressive crystallization processes for both the systems. The values of activation energy of nucleation (E-n), activation energy of crystallization (E-c), and their pre-exponential factors (InA(n), InA(c) respectively) were calculated from Arrhenius plots. Compared to the hydrothermal method, shorter induction period was observed when DGC method was employed. Both the E-n (49.70 kJ/mol) and E-c (52.82 kJ/mol) for DGC method were found to be lower than that of the E-n (55.70 kJ/mop and E-c (60.23 kJ/mol) for hydrothermal method. The kinetics parameters viz. K and q were derived from kinetic expressions and DGC method showed higher value of K and lower value of q compared to hydrothermal crystallization method at identical temperature. Various DGC method parameters such as water content at the bottom of autoclave and SiO2/SnO2 mole ratio have shown the influence on the kinetics of crystallization of Sn-MFI. (C) 2013 Elsevier Inc. All rights reserved.</p>10aCrystallization10aDGC10akinetics10aNucleation10aSn-MFI1 aNiphadkar, P., S.1 aTangale, N., P.1 aJoshi, P., N.1 aAwate, S., V.  uhttps://library.ncl.res.in/content/crystallization-kinetics-sn-mfi-molecular-sieve-formation-dry-gel-cross-mark-conversion-0