@article { ISI:000232773100050, title = {Conversion of fly ash - an environmentally detrimental waste to zeolite beta (BEA) for commercial catalytic applications}, journal = {Journal of the American Ceramic Society}, volume = {88}, number = {11}, year = {2005}, month = {NOV}, pages = {3260-3263}, publisher = {BLACKWELL PUBLISHING}, type = {Article}, address = {9600 GARSINGTON RD, OXFORD OX4 2DQ, OXON, ENGLAND}, abstract = {

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.

}, issn = {0002-7820}, doi = {10.1111/j.1551-2916.2005.00575.x}, author = {Kasture, M. W. and Bokade, Vijay V. and Joshi, P. N.} } @article { ISI:000226929600009, title = {Vapour phase oxidation of acetophenone to benzoic acid over binary oxides of V and Mo}, journal = {Chemical Engineering Research and Design}, volume = {83}, number = {A1}, year = {2005}, month = {JAN}, pages = {75-80}, publisher = {INST CHEMICAL ENGINEERS}, type = {Article}, address = {165-189 RAILWAY TERRACE, DAVIS BLDG, RUGBY CV21 3HQ, ENGLAND}, abstract = {

Test data for catalytic oxidation of acetophenone into benzoic acid performed at bench scale with V2O5-MoO3 catalyst in a continuous downflow metal reactor are presented. The process parameters such as temperature and flow rate influence the product distribution. The P2O5, B2O3 and Na2O when used as dopant on V2O5-MoO3 catalyst showed marked influence on activity and selectivity. An acidic catalyst like V2O5-MoO3-P2O5 favours formation of benzoic acid while a basic catalyst like V2O5-MoO3-Na2O favours formation of benzaldehyde. The addition of Na2O into V2O5-MoO3 binary oxides formed new phases (NaVMoO6 and Na2V2Mo3O15), which increased Arrhenius activation energy from 18.24 to 31.35 kcal mol(-1).

}, keywords = {acetophenone, activity, benzoic acid, carbon oxides, oxidation of acetophenone, selectivity}, issn = {0263-8762}, doi = {10.1205/cherd.03206}, author = {Chumbhale, Vilas R. and Paradhy, S. A. and Anilkumar, Mettu and Kadam, S. T. and Bokade, Vijay V.} } @proceedings { ISI:000291657600051, title = {Synthesis and characterization of value added catalysts zeolite beta using environmentally detrimental flyash}, volume = {170}, year = {2007}, note = {15th International Zeolite Conference, Beijing, PEOPLES R CHINA, AUG 12-17, 2007}, month = {AUG}, pages = {438-443}, publisher = {Elsevier Science BV}, address = {Beijing, Peoples R China}, abstract = {

Fly ash is a major byproduct of Thermal power plant, which makes a lot of pollution to the environment due to its fineness. When a large amount of fly ash is dumped in the places near to power plants, it mixes in all segment of environment like water, air as well as soil. Though it can be utilized for different useful purposes, due to the lack of technical knowledge about how and proper motivation, no progress has been made in its utilization. It has been demonstrated that the fly ash can be used for making a value added catalyst zeolite beta by using simple and low cost process. In the present paper it is demonstrated that the fly ash can be used as a source of silica and alumina in the synthesis of value added catalyst zeolite beta. Moreover, the influence of different silica sources such as tetraethylortho silicate, silica sol and fumed silica on the physiochemical characteristics of well crystallized zeolite beta was also studied. The detailed characterization was carried out by using powder XRD, (27)Al and (29)Si MAS NMR, chemical analysis and low temperature nitrogen adsorption. Based on the data obtained from various systems containing different silica source, fumed silica is found to be most efficient source materials and showed superiority in the uniformity of aluminum distribution and possesses higher surface area.

}, isbn = {978-0-444-53068-4}, issn = {0167-2991}, author = {Kasture, M. W. and Bokade, Vijay V. and Joshi, P. N. and Kumar, R.}, editor = {Xu, R and Gao, Z. and Chen, J and Yan, W} } @article {Hung, title = {Synthesis of Bio-diesel and Bio-lubricant by transesterification of vegetable oil with lower and higher alcohols over heteropolyacids supported by clay (K-10)}, journal = {Process Safety and Environmental Protection}, volume = {85}, number = {B5}, year = {2007}, note = {Theoretical Chemistry Symposium 2006 (TCS 2006), Bharathidasan Univ, Trichy, INDIA, DEC 11-13, 2006}, month = {SEP}, pages = {372-377}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

{The use of different lower and higher alcohols viz; methanol, ethanol, n-propanol and n-octanol, for the synthesis of methyl, ethyl, propyl and octyl fatty acid esters by transesterification of vegetable oil (triglycerides) with respective alcohols also known as {\textquoteleft}Bio-diesel{\textquoteright} and {\textquoteleft}Biolubricants{\textquoteright} was studied in detail. The reactions were carried out in a batch process. The activity with different supports like clay (K-10), activated carbon, ZSM-5, H-beta and TS-1 were compared. The superacids (heteropolyacids, HPA) viz; Dodeca-Tungstophosphoric acid [

}, keywords = {coprecipitation, lithium aluminate, Microemulsion, Nanoparticles, sol-gel, Surfactants}, issn = {0167-577X}, author = {Bokade, Vijay V. and Yadav, G. D.} } @article {33}, title = {Synthesis of pharmaceutical intermediates by toluene benzylation over heteropoly acids on different support}, journal = {Journal of Natural Gas Chemistry}, volume = {16}, number = {2}, year = {2007}, note = {International Conference on Nano Science and Technology (ICONSAT 2006), New Delhi, INDIA, MAR 16-18, 2006}, month = {JUN}, pages = {186-192}, publisher = {AMER SCIENTIFIC PUBLISHERS}, type = {Article}, address = {25650 NORTH LEWIS WAY, STEVENSON RANCH, CA 91381-1439 USA}, abstract = {

{Selective formation of pharmaceutical intermediates like diphenylmethane, dimethyl-diphenylmethane, benzyl toluene and benzoic acid by liquid phase, toluene benzylation with benzyl chloride as a benzylating agent, was systematically studied over plane clay (K-10, montmorillonite), plane H-Beta, plane MFI structured titanosilicate (TS-1) and heteropoly acids [

}, keywords = {heteroassembly, nanoplates, polyfunctional capping agents, shape selective synthesis of gold-silver nanostructures, surface confinement}, issn = {1533-4880}, doi = {10.1016/S1003-9953(07)60046-2}, author = {Bokade, Vijay V. and Yadav, G. D.} } @article {40}, title = {Toluene alkylation with methanol to p-xylene over heteropoly acids supported by clay}, journal = {Journal of Natural Gas Chemistry}, volume = {16}, number = {1}, year = {2007}, month = {MAR}, pages = {42-45}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

{The alkylation of toluene with methanol for the selective formation of p-xylene was systematically studied. Very few studies have been reported on the use of superacids such as heteropolyacids on cheap supports, such as clay. This article deals with the use of different heteropoly acids (HPAs), viz, Dodeca-Tungstophosphoric acid [

}, keywords = {co-crystalline, p-xylene, toluene alkylation, ZSM-12, ZSM-5}, issn = {1003-9953}, doi = {10.1016/S1003-9953(07)60024-3}, author = {Bokade, Vijay V. and Deshpande, Suvarna S. and Patil, R. and Jain, S. and Yadav, G. D.} } @article { ISI:000256178900021, title = {Heteropolyacid supported on acidic clay: a novel efficient catalyst for alkylation of ethylbenzene with dilute ethanol to diethylbenzene in presence of C-8 aromatics}, journal = {Journal of Molecular Catalysis A-Chemical}, volume = {285}, number = {1-2}, year = {2008}, month = {APR}, pages = {155-161}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Vapor phase alkylation of ethylbenzene with ethanol to diethylbenzene is industrially relevant. Diethylbenzene is an important raw material for the conversion of divinyl benzene monomer. Conventionally, it is prepared from diacetophenone by reduction. It is also prepared by vapor phase alkylation of ethylbenzene with ethylene using zeolitic catalysts. The efficacy of dodecatungsotphosphoric acid (DTPA) supported on acid treated clay has been evaluated in the current work in the alkylation of ethylbenzene with 80\% (w/w) ethanol. 15\% (w/w) DTPA/K-10 clay was found to be an efficient and robust catalyst. The use of aqueous ethanol and a mixed C-8 stream lowers the cost of production. A kinetic model is developed by studying the important process parameters with 15\% (w/w) DTPA/K-10 as the catalyst. (c) 2008 Elsevier B.V. All rights reserved.

}, keywords = {Alkylation, diethylbenzene, Heteropolyacid, kinetics, Solid acids}, issn = {1381-1169}, doi = {10.1016/j.molcata.2007.11.018}, author = {Bokade, Vijay V. and Yadav, Ganapati D.} } @article { ISI:000271072500019, title = {Disproportionation of ethylbenzene in the presence of C-8 aromatics}, journal = {Journal of Natural Gas Chemistry}, volume = {18}, number = {3}, year = {2009}, month = {SEP}, pages = {369-374}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The selective synthesis of p-diethylbenzene (p-DEB) by disproportionation of ethylbenzene (EB) in the presence of aromatics like m- and p-xylene isomers has been studied over a pore size regulated HZSM-5 catalyst. The industrial feed having different compositions of ethylbenzene and xylene isomers was used for the experimentation. Hence, they were expected to hinder the movement of reactant molecules both on the external surface and within the zeolite channels. It was observed that irrespective of the different feed compositions the concentration of the xylene isomers was intact in the product. There is no other byproducts formation like para-ethylmethyl benzene. The effects of varying the concentration of aromatic compounds in the feed on ethylbenzene conversion and product distribution over the parent and modified H-ZSM-5 catalyst have been discussed. Ethylbenzene disproportionation reaction follows the pseudo first order reaction with an activation energy of 8.6 kcal/mol.

}, keywords = {Catalyst, diethylbenzene, disproportionation, ethylbenzene, xylene isomers}, issn = {1003-9953}, doi = {10.1016/S1003-9953(08)60125-5}, author = {Sharnappa, N. and Pai, S. and Bokade, Vijay V.} } @article { ISI:000266185600012, title = {Selective N-alkylation of aniline with methanol over a heteropolyacid on montmorillonite K10}, journal = {Applied Clay Science}, volume = {44}, number = {3-4}, year = {2009}, month = {MAY}, pages = {255-258}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

N-methylaniline is an industrially important product in the manufacture of paper, textile dyes, drugs, perfumes and explosives. The vapour phase alkylation of aniline with methanol forming N-methylaniline is advantageous over liquid phase alkylation. In present study, vapour phase methylation of aniline over dodecatungestophosphoric acid supported on K10 montmorillonite was systematically studied and optimization of process parameters was carried out. The 20\% m/m DTPA/K10 was found to be optimum with 79\% aniline conversion and 99\% N-methylaniline selectivity. The reaction required milder operating conditions than reported for commercial catalysts. We also studied the feasibility of 20\% m/m DTPA/K10 as a catalyst for the alkylation of aniline with other alcohols like ethanol, n-propanol, iso-propanol and n-butanol. The activity of 20\% m/m DTPA/K10 decreased with increasing carbon number. (C) 2009 Elsevier B.V. All rights reserved.

}, keywords = {Alkylation, Aniline, Heteropolyacid, montmorillonite K10, N-methylaniline}, issn = {0169-1317}, doi = {10.1016/j.clay.2009.02.011}, author = {Nehate, Manoj and Bokade, Vijay V.} } @article { ISI:000264521700002, title = {Selective synthesis of cumene by isopropylation of benzene using catalytic membrane reactor}, journal = {Chemical Engineering Journal}, volume = {147}, number = {2-3}, year = {2009}, month = {APR}, pages = {97-101}, publisher = {ELSEVIER SCIENCE SA}, address = {PO BOX 564, 1001 LAUSANNE, SWITZERLAND}, abstract = {

Selective isopropylation of benzene to cumene is demonstrated using catalytic membrane reactor (CMR), to our knowledge for the first time and the performance was evaluated against conventional plug flow reactor (PFR). Almost complete elimination of byproducts like polyalkylated benzene and higher aromatics could be made possible by using CMR. These are present in significant amount when reaction is carried out with PFR. The cumene selectivity increased up to a maximum of 97.25\% by CMR as against 90.05\% with conventional PFR. The effect of reaction parameters that can greatly influence the process economics, such as liquid hourly space velocity (LHSV), reactant mole ratio and catalyst/reactor volume ratio were investigated. Changes in these parameters made for CMR are industrially advantageous. The process by CMR is more economical and ecofriendly than PFR as far as milder process parameters (higher LHSV, lower reactant feed mole ratio, less catalyst require, etc.) and process intensification (reaction and separation in single reactor) are concerned. The study provides new insights for benzene isopropylation reaction. (C) 2008 Elsevier B.V. All rights reserved.

}, keywords = {Benzene, Catalytic membrane reactor, cumene, Diisopropyl benzene, Friedel-Craft alkylation}, issn = {1385-8947}, doi = {10.1016/j.cej.2008.06.035}, author = {Bokade, Vijay V. and Kharul, Ulhas K.} } @article { ISI:000271443200024, title = {Synthesis of N-methylaniline by aniline alkylation with methanol over Sn-MFI molecular sieve}, journal = {Catalysis Letters}, volume = {133}, number = {1-2}, year = {2009}, month = {NOV}, pages = {175-184}, publisher = {SPRINGER}, address = {233 SPRING ST, NEW YORK, NY 10013 USA}, abstract = {

Sn-MFI molecular sieves (Tin silicalite-1) with SiO(2)/SnO(2) molar ratio of 50-150 were synthesized and characterized. Elemental analysis, XRD and DRUV-vis confirmed that prepared samples were of MFI zeolite structure and Sn was incorporated in MFI framework. Vapor phase methylation of aniline over Sn-MFI was systematically studied and optimizations of process parameters were carried out. Sn-MFI (SiO(2)/SnO(2) = 50) was found to be optimum catalyst with 55\% aniline conversion and 60\% N-methylaniline selectivity. At lower space velocity (higher contact time) of 1 h(-1), aniline conversion was found to be increased to 71\% with reduction in N-methylaniline selectivity to 39\% and increased in N,N-dimethylaniline selectivity to 58\%. The reaction follows first order kinetics with respect to aniline having activation energy of 7.3 kcal/mol.

}, keywords = {Aniline, Lewis acid, Methanol, N-methylaniline, Sn-MFI}, issn = {1011-372X}, doi = {10.1007/s10562-009-0143-4}, author = {Niphadkar, P. S. and Joshi, P. N. and Gurav, H. R. and Deshpande, Suvarna S. and Bokade, Vijay V.} } @article { ISI:000263249600064, title = {Tin-silicalite-1: synthesis by dry gel conversion, characterization and catalytic performance in phenol hydroxylation reaction}, journal = {Materials Chemistry and Physics}, volume = {114}, number = {1}, year = {2009}, month = {MAR}, pages = {344-349}, publisher = {ELSEVIER SCIENCE SA}, address = {PO BOX 564, 1001 LAUSANNE, SWITZERLAND}, abstract = {

Tin-silicalite-1 (Sn-MFI) has been successfully synthesized by dry gel conversion (DGC) method. The influence of various synthesis parameters such as crystallization time, temperature, water content at the bottom of autoclave, molar ratios of (TPA)(2)O/SiO(2) and SiO(2)/SnO(2) in dry gel on the crystallization kinetics and physico-chemical properties of Sn-MFI materials has been investigated. Powder-X-ray diffraction (XRD),XPS,AAS, DRUV-vis and SEM techniques were employed as characterization tools. Time-dependent studies revealed that, the progressive crystallization of Sn-MFI depend not only on the synthesis time but also on the other various synthesis parameters. Increase in the crystallization temperature, water content at bottom of autoclave (TPA)(2)O/SiO(2) and SiO(2)/SnO(2) molar ratios in dry gel resulted in the lowering of overall crystallization period. A good correspondence between the chemical composition of the surface and the bulk indicated the uniform distribution of Sn(4+) ions. The presence of these ions in tetrahedral coordination has been indicated by DRUV-vis spectral studies. Although, not better but comparable activity has been shown by Sn-MFI prepared by dry gel conversion method with Sn-MFI prepared by conventional hydrothermal crystallization method in the hydroxylation of phenol reaction. Increase in concentration of isolated Sn(4+) ions led to increase in phenol conversion and H(2)O(2) efficiency. (c) 2008 Elsevier B.V. All rights reserved.

}, keywords = {crystallisation, Dry gel conversion, microporous materials, Sn-MFI}, issn = {0254-0584}, doi = {10.1016/j.matchemphys.2008.09.026}, author = {Niphadkar, Prashant S. and Kotwal, Mehejabeen S. and Deshpande, Shilpa S. and Bokade, Vijay V. and Joshi, Praphulla N.} } @article { ISI:000271103500009, title = {Transesterification of edible and nonedible vegetable oils with alcohols over heteropolyacids supported on acid-treated clay}, journal = {Industrial \& Engineering Chemistry Research}, volume = {48}, number = {21}, year = {2009}, month = {NOV}, pages = {9408-9415}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

In the current work, the novelty of heteropolyacid on clay (K-10) for the transesterification of vegetable oil with lower and higher alcohols is presented. Methyl esters (biodiesel) and glycerol were produced by the transesterification of vegetable oil with methanol in the presence of dodecatungestophosphoric acid (DTPA) supported on K-10 clay. The transesterification consists of three consecutive reversible reactions Diglycerides (DG) and monoglycerides (MG) are intermediate products. The optimal catalyst concentration was 5\% w/w of oil. Detailed studies were done for optimization of the process parameters. The rate of transesterification in a batch reactor increased with temperature up to 170 degrees C. Higher temperatures did not reduce the time to reach maximum conversion. The study was also extended to reactions of different edible and nonedible oils with lower and higher alcohols. The conversion of TG, DG, and MG seemed to be a second-order mechanism for the forward and reverse reactions, where the reaction system could be described as a pseudo-heterogeneous catalyzed reaction. The reaction rate constants for the TG. DG, and MG transesterification reactions were 0.12-0.84 h(-1) and were higher for the MG reaction than for the TG transesterification. The activation energies were 4.2, 26, and 7.4 kcal/mol for the TG, DG, and MG transesterification reactions, respectively. The proposed kinetic model fits the experimental results well.

}, issn = {0888-5885}, doi = {10.1021/ie801543k}, author = {Bokade, Vijay V. and Yadav, Ganapati D.} } @article { ISI:000267531100032, title = {Transesterification of sunflower oil catalyzed by flyash-based solid catalysts}, journal = {Fuel}, volume = {88}, number = {9}, year = {2009}, month = {SEP}, pages = {1773-1778}, publisher = {ELSEVIER SCI LTD}, address = {THE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, OXON, ENGLAND}, abstract = {

Flyash-based base catalyst was used in the transesterification of sunflower oil with methanol to methyl esters in a heterogeneous manner. Catalyst preparation variables such as, the KNO(3) loading amount and calcination temperature were optimized. The catalysts were characterized by powder XRD. The catalyst prepared by loading of 5 wt.\% KNO(3) on flyash followed by its calcination at 773 K has exhibited maximum oil conversion (87.5 wt.\%). The influence of various reaction parameters such as \% catalyst loading, methanol to oil molar ratio, reaction time, temperature, reusability of the catalyst on the catalytic activity was investigated. K(2)O derived from KNO(3) might be an essential component in the catalyst for its efficiency. (C) 2009 Elsevier Ltd. All rights reserved.

}, keywords = {Flyash, heterogeneous catalyst, Methyl ester, Sunflower oil, transesterification}, issn = {0016-2361}, doi = {10.1016/j.fuel.2009.04.004}, author = {Kotwal, M. S. and Niphadkar, P. S. and Deshpande, Suvarna S. and Bokade, Vijay V. and Joshi, P. N.} } @article { ISI:000276957700010, title = {Synthesis of ethyl acetate by esterification of acetic acid with ethanol over a heteropolyacid on montmorillonite K10}, journal = {Journal of Natural Gas Chemistry}, volume = {19}, number = {2}, year = {2010}, month = {MAR}, pages = {161-164}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

In present work, liquid phase esterification of acetic acid with ethanol over dodecatungestophosphoric acid (DTPA) supported on K10 mommorillonite was systematically studied and optimization of process parameters was carried out The 20\% m/m urpAtK tO was found to be the optimum catalyst with 90\% acetic acid conversion and 100\% ethyl acetate selectivity The study was also explored to see the feasibility of 20\% m/m DTPA/K10 as a catalyst for the alkylation of acetic acid with other alcohols like methanol, iso-propanol and sr-butanol. The 20\% m/m DTPA/K10 has shown increased activity with the increase in carbon number, at the same alcohol reflux The results are novel

}, keywords = {Acetic acid, Ethanol, ethyl acetate, Heteropolyacid, montmorillonite K10}, issn = {1003-9953}, doi = {10.1016/S1003-9953(09)60048-7}, author = {Gurav, Hanumant and Bokade, Vijay V.} } @article { ISI:000287281900003, title = {Esterification of levulinic acid to n-butyl levulinate over heteropolyacid supported on acid-treated clay}, journal = {Journal of Natural Gas Chemistry}, volume = {20}, number = {1}, year = {2011}, month = {JAN}, pages = {18-24}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Levulinic acid has been identified as a promising green, biomass-derived platform chemical. n-Butyl levulinate is used as an important intermediate having diverse applications. The present work focuses on the synthesis of n-butyl levulinate by esterification of levulinic acid with n-butanol using heteropolyacid (HPA) supported on acid-treated clay montmorillonite (K10). 20\% (w/w) dodecatungestophosphoric acid (DTPA) supported on K10 was found to be the most efficient catalyst with 97\% levulinic acid conversion and 100\% selectivity towards n-butyl levulinate. Effects of various process parameters were studied to examine the efficacy of 20\% (w/w) DTPA/K10 for optimization of the activity.

}, keywords = {dodectungestophosphoric acid, K10, levulinic acid, n-butanol, n-Butyl levulinate}, issn = {1003-9953}, doi = {10.1016/S1003-9953(10)60147-8}, author = {Dharne, S. and Bokade, Vijay V.} } @article { ISI:000294374900020, title = {Heteropolyacid supported on montmorillonite catalyst for dehydration of dilute bio-ethanol}, journal = {Applied Clay Science}, volume = {53}, number = {2, SI}, year = {2011}, month = {AUG}, pages = {263-271}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Vapour phase dehydration of dilute bio-ethanol (EtOH) to ethylene (E) and diethyl ether (DEE) is industrially relevant. Ethylene is an important raw material for many petrochemical products and Diethyl ether (DEE) can be used as an alternative fuel. The efficacy of montmorillonite (K-10) and dodecatungestophosphoric acid (DTPA) supported on montmorillonite (DTPA/K-10), has been evaluated in the current work in the dehydration of dilute bio-ethanol (80\%m/m). The dehydration of ethanol and cracking of diethyl ether were studied independently. 30\% m/m DTPA/K-10 was found to be more active with 74\% ethanol conversion and 92\% ethylene selectivity at 250 degrees C in comparison with other acid catalysts used. The merit of the process lies in its use of dilute bio-ethanol, a new avenue for ethylene production from a non-petroleum feedstock. Kinetic interpretation has been made by studying the important process parameters by using 30\%m/m DTPA/montmorillonite as the catalyst. The mechanism of the dehydration of ethanol reaction suggests that two types of sites are responsible. The dehydration of ethanol and cracking of diethyl ether are second order reactions with weak adsorption of species. (C) 2011 Elsevier B.V. All rights reserved.

}, keywords = {Bio-ethanol, dehydration, Diethyl ether, Ethylene, Heteropolyacid}, issn = {0169-1317}, doi = {10.1016/j.clay.2011.03.006}, author = {Bokade, Vijay V. and Yadav, Ganapati D.} } @article { ISI:000293492300024, title = {Influence of Al3+ insertion in the stannosilicate MFI framework on the catalytic performance in vapor phase aniline N-methylation}, journal = {Applied Catalysis A-General}, volume = {401}, number = {1-2}, year = {2011}, month = {JUL}, pages = {182-188}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Silica-based Sn-MFI, Al-MFI and Al-Sn-MFI molecular sieves were synthesized by hydrothermal crystallization of gels having molar compositions SiO2:xSnO(2):yAl(2)O(3):0.23 (TPA)(2)O:35H(2)O, where x ranges from 1/0 to 1/200 and y from 1/0 to 1/400. Keeping molar Si/(Al + Sn) = 50, the amount of tin and aluminum in hydrogel was varied (Sn:Al molar ratios = 1:0, 1:0.33, 1:1, 1:3, 0:1) to investigate the synergy between Lewis and Bronsted acid sites in acid catalyzed aniline N-methylation reaction. Catalyst characterization was done by Powder X-ray diffraction, DRUV-vis spectroscopy, temperature programmed ammonia desorption (TPAD) and FTIR spectroscopy. An increase in the Al3+ insertion in Sn-MFI framework resulted in the increase in the stronger acid sites. Al-Sn-MFI showed higher aniline conversion than their monometallic counterparts. A sample having B/L ratio in between 0.67 and 0.91 was found to be optimum for maximizing the NMA yield, indicating the existence synergistic properties of Al-Sn-MFI. Upon process parameter optimization, the optimum sample M50 [Si/Al = 50.2, Si/Sn = 93.8, Si/(Al + Sn) = 43.2] showed the maximum aniline conversion (67\%) and NMA selectivity (81\%) at reaction temperature = 220 degrees C, weight hourly space velocity (WHSV) = 3 h(-1), molar ratio (aniline to methanol) = 1:8 and TOS = 4 h. (C) 2011 Elsevier B.V. All rights reserved.

}, keywords = {Al-Sn-MFI, Aniline, Bronsted and Lewis acid, Methanol, N-methylaniline}, issn = {0926-860X}, doi = {10.1016/j.apcata.2011.05.019}, author = {Niphadkar, P. S. and Joshi, P. N. and Deshpande, Suvarna S. and Bokade, Vijay V.} } @article { ISI:000299404900016, title = {Dodecatungstophosphoric acid supported on acidic clay catalyst for disproportionation of ethylbenzene in the presence of C-8 aromatics}, journal = {Industrial \& Engineering Chemistry Research}, volume = {51}, number = {3}, year = {2012}, month = {JAN}, pages = {1209-1217}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

Vapor-phase disproportionation of ethylbenzene (EB) to diethylbenzene (DEB) in a single step is industrially relevant. Diethylbenzene is an important raw material for the conversion of divinylbenzene monomer. Conventionally, it is prepared from diacetophenone by reduction. It is also prepared by vapor-phase alkylation of ethylbenzene with ethylene/ethanol using zeolitic catalysts. In the current work, the efficacy of dodecatungstophosphoric acid (DTPA) supported on acid-treated clay has been evaluated in the disproportionation of ethylbenzene. A 20\% (w/w) DTPA/K-10 clay catalyst was found to be efficient and robust. An industrial feed having different compositions of ethylbenzene and xylene isomers was used for the experimentation. Hence, they were expected to hinder the movement of reactant molecules on the catalyst surface. It was observed that irrespective of feed composition the concentration of the xylene isomers was intact in the product. There was no other byproduct formation like p-ethylrnethylbenzene. Optimization of process parameters is presented. The effect of varying the concentration of aromatic compounds in the feed on ethylbenzene conversion and product distribution over the plain clay (K-10) and heteropolyacid-loaded clay catalyst have been discussed. The effect of catalyst bed length to inner diameter of reactor (L/D) ratio on the ethylbenzene conversion and selective formation of p-diethylbenzene (p-DEB) are also discussed.

}, issn = {0888-5885}, doi = {10.1021/ie202298e}, author = {Bokade, Vijay V. and Yadav, Ganapati D.} } @article { ISI:000320976600013, title = {Catalytic upgrading of renewable levulinic acid to ethyl levulinate biodiesel using dodecatungstophosphoric acid supported on desilicated H-ZSM-5 as catalyst}, journal = {Applied Catalysis A-General}, volume = {460}, year = {2013}, month = {JUN}, pages = {90-98}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Levulinic acid (LA) is considered as a renewable platform chemical and can be used for the synthesis of variety of important fuels and chemicals. In particular, its esterification with ethanol produces ethyl levulinate (EL) would be green process, as it can be used as diesel miscible biofuel (DMB), preventing global warming by decreasing atmospheric CO2. This study explores the use of modified H-ZSM-5 by desilication viz.; DH-ZSM-5 and dodecatungstophosphoric acid (DTPA) loaded on DH-ZSM-5 for esterification of LA with ethanol aiming to EL. Different degree of desilication of H-ZSM-5 was performed by using aq. NaOH (0.2-1.5 M) at 338 K for 30 min and then DTPA was loaded on these desilicated H-ZSM-5 (DH-ZSM-5) support. H-ZSM-5, DH-ZSM-5 and DTPA on these DH-ZSM-5 samples were characterized by powder x-ray diffraction (XRD), N-2 adsorption-desorption, pyridine chemisorbed IR spectroscopy, Temperature Programmed Ammonia Desorption (TPAD). The increase in conversion of levulinic acid was observed from 28\% to 94\% with increase of DTPA loading from 0\% to 15\%. The increased LA conversion may be due to increase in total acidity from 43.14\% to 84.31\%. The use of DH-ZSM-5 as support for deposition of DTPA may be reported for the first time. The present work also extended to optimize process parameters such as DTPA loading on DH-ZSM-5, catalyst to LA ratio, LA to ethanol molar ratio, speed of agitation, particle size reaction temperature and catalyst reusability. Kinetic study based on pseudo-homogeneous (P-H) model is also presented. The experimental results follow second order kinetics. (C) 2013 Elsevier B.V. All rights reserved.

}, keywords = {desilicated H-ZSM-5, DTPA on desilicated H-ZSM-5, Esterification, ethyl levulinate, levulinic acid}, issn = {0926-860X}, doi = {10.1016/j.apcata.2013.04.024}, author = {Nandiwale, Kakasaheb Y. and Sonar, Shilpa K. and Niphadkar, Prashant S. and Joshi, Praphulla N. and Deshpande, Shilpa S. and Patil, Vilas S. and Bokade, Vijay V.} } @article { ISI:000328527000041, title = {Esterification of levulinic acid to ethyl levulinate over bimodal micro-mesoporous H/BEA zeolite derivatives}, journal = {Catalysis Communications}, volume = {43}, year = {2014}, month = {JAN}, pages = {188-191}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

A series of bimodal micro-mesoporous H/BEA zeolite derivatives were prepared by the post-synthesis modification of H/BEA zeolite by NaOH (0.05 M-1.2 M) treatment Samples were characterized by powder XRD, low temperature nitrogen adsorption/desorption, temperature programmed desorption of ammonia and ICP. The mesopore formation was found to play a crucial role in liquid phase esterification of levulinic acid with ethanol. The enhanced catalytic activity of a bimodal micro-mesoporous H/BEA zeolite derivative (H/BEA(0.10)) prepared by treatment with 0.1M NaOH can be mainly attributed to the high mesoporosity coupled with better preserved crystallinity and acidic properties. (C) 2013 Elsevier B.V. All rights reserved.

}, keywords = {Esterification, ethyl levulinate, H/BEA zeolite, Mesoporosity, Post-synthesis modification}, issn = {1566-7367}, doi = {10.1016/j.catcom.2013.10.006}, author = {Patil, C. R. and Niphadkar, P. S. and Bokade, Vijay V. and Joshi, P. N.} } @article { ISI:000341764500007, title = {Esterification of renewable levulinic acid to ethyl levulinate biodiesel catalyzed by highly active and reusable desilicated H-ZSM-5}, journal = {Journal of Chemical Technology and Biotechnology}, volume = {89}, number = {10}, year = {2014}, month = {OCT}, pages = {1507-1515}, publisher = {WILEY-BLACKWELL}, type = {Article}, address = {111 RIVER ST, HOBOKEN 07030-5774, NJ USA}, abstract = {

BACKGROUNDIn the near future, fossil fuel will have limitations in terms of availability and also great concerns over its environmental impact. New routes and related technologies based on renewable feedstocks can overcome most of these problems associated with fossil fuel. Among current biodiesel sources, ethyl levulinate (EL) biodiesel obtained from catalytic esterification of renewable levulinic acid (LA) with ethanol has received a great deal of attention. The use of desilicated H-ZSM-5 (DH-ZSM-5) as heterogeneous acid catalyst for EL biodiesel production in a closed system (under autogeneous pressure) was studied. RESULTSThe effect of reaction parameters such as ethanol to LA molar ratio (4:1 to 10:1), catalyst to LA ratio (0.10-0.25), speed of agitation (100-400rpm), particle size (53-355 mu m), reaction temperature (363-403K) and reaction time (7h) was investigated to maximize LA conversion. CONCLUSIONLevulinic acid conversion reached 95\% over DH-ZSM-5 and the catalyst was reusable for up to six cycles. This LA conversion and the catalyst reusability values are higher than others reported in the literature. A pseudo-homogeneous (P-H) kinetic model indicated that reaction rate constants increased with increasing molar ratio, catalyst to LA ratio and reaction temperature. The activation energy decreased from 73.14 to 21.08 kJ mol(-1) when increasing the catalyst to LA ratio from 0.10 to 0.25, which implies a kinetically controlled reaction. (c) 2013 Society of Chemical Industry

}, keywords = {desilicated H-ZSM-5, Esterification, ethyl levulinate, levulinic acid}, issn = {0268-2575}, doi = {10.1002/jctb.4228}, author = {Nandiwale, Kakasaheb Y. and Niphadkar, Prashant S. and Deshpande, Shilpa S. and Bokade, Vijay V.} } @article { ISI:000338353000004, title = {Glycerol etherification using n-butanol to produce oxygenated additives for biodiesel fuel over H-beta zeolite catalysts}, journal = {Energy Technology}, volume = {2}, number = {5}, year = {2014}, month = {MAY}, pages = {446-452}, publisher = {WILEY-V C H VERLAG GMBH}, address = {BOSCHSTRASSE 12, D-69469 WEINHEIM, GERMANY}, abstract = {

The catalytic etherification of glycerol has been systematically studied in batch process by using n-butanol to produce oxygenated additives for biodiesel fuels over various solid-acid catalysts, such as H-beta zeolite, ZSM-5, K10, etc.. The present work includes a detailed study of the optimization of the etherification process parameters, such as catalyst loading (7-20 wt\% of glycerol), molar ratio of glycerol/n-butanol (1: 6 to 1: 15), speed of agitation (100-400 rpm), reaction temperature (413-453 K), and reaction time (0.5-4 h) in view of maximizing the glycerol conversion and selectivity towards mono-butyl-glycerol ether (ME). The catalyst reusability was studied using the optimized process parameters. Amongst the studied catalysts, the H-beta zeolite was found to be the most promising for the etherification of glycerol with glycerol conversion of 55\% and a 98\% selectivity towards ME formation. The H-beta zeolite was found to be an active and stable catalyst for up to 4 cycles. The use of n-butanol as alkylating agent is presented for first time, to the authors knowledge. The reaction was performed at milder operating conditions (0.5 MPa) than previously reported (2 MPa). A kinetic model was developed for the etherification reaction and the data obtained at optimized process parameters was used to calculate the kinetic parameters. The reaction rate constants at different reaction temperatures, activation energies, and pre-exponential factors were obtained for the etherification reaction with an accuracy of R-2 \> 0.989.

}, keywords = {biofuels, catalysis, etherification, fuel additives, zeolites}, issn = {2194-4288}, doi = {10.1002/ente.201300169}, author = {Nandiwale, Kakasaheb Y. and Patil, Shivraj E. and Bokade, Vijay V.} } @article { ISI:000338748400051, title = {One-pot synthesis of 5-hydroxymethylfurfural by cellulose hydrolysis over highly active bimodal micro/mesoporous H-ZSM-5 catalyst}, journal = {ACS Sustainable Chemistry \& Engineering}, volume = {2}, number = {7}, year = {2014}, month = {JUL}, pages = {1928-1932}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

Direct synthesis of 5-hydroxymethylfurfural (5-HMF), a useful renewable biofuel and biochemical, was systematically studied by hydrolysis of microcrystalline cellulose over Bimodal-HZ-5 zeolite. Bimodal-HZ-5 zeolite obtained by post-synthesis modification of H-ZSM-5 with desilication was found to be a potential heterogeneous catalyst with 67\% cellulose conversion and 46\% yield of 5-HMF. Bimodal-HZ-5 was observed to be reusable for four cycles, without any loss in activity. The detailed optimization of process parameters and catalyst reusability are also presented. The present study opens a new avenue for the renewable one-pot synthesis of 5-HMF, a valuable product.

}, keywords = {5-Hydroxymethylfurfural, Biomodal-HZ-5, glucose, Hydrolysis, Microcrystalline cellulose}, issn = {2168-0485}, doi = {10.1021/sc500270z}, author = {Nandiwale, Kakasaheb Y. and Galande, Nitish D. and Thakur, Pratika and Sawant, Sanjay D. and Zambre, Vishal P. and Bokade, Vijay V.} } @article { ISI:000346322200011, title = {Process optimization by response surface methodology and kinetic modeling for synthesis of methyl oleate biodiesel over H3PW12O40 anchored montmorillonite K10}, journal = {Industrial \& Engineering Chemistry Research}, volume = {53}, number = {49}, year = {2014}, month = {DEC}, pages = {18690-18698}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

Heterogeneous acid catalysts comprised of 1030\% (w/w) H3PW12O40 anchored to montmorillonite (K10) were used for synthesis of methyl oleate biodiesel by esterification of free fatty acid (oleic acid) with methanol in closed batch system. Response surface methodology (RSM) was employed to optimize esterification of oleic acid with methanol over 20\% (w/w) H3PW12O40/K-10. The effects of various process parameters such as catalyst loading, molar ratio, and reaction temperature on oleic acid conversion were addressed by BoxBehnken experimental design (BBD). Coefficient of determination (R-2) of this model was 0.996. 20\% (w/w) H3PW12O40/K-10 was proved to be potential catalyst with 100\% oleic acid conversion at optimized process parameters and with reusability of four cycles. Moreover, a second-order pseudohomogeneous (PH) kinetic model has been proposed and validated (R-2 \> 0.97) with experimental data. Kinetics confirmed that esterification reaction is performed in the kinetic regime due to high activation energy of 43.7 kJ mol(-1).

}, issn = {0888-5885}, doi = {10.1021/ie500672v}, author = {Nandiwale, Kakasaheb Y. and Bokade, Vijay V.} } @article { ISI:000340350900018, title = {Production of octyl levulinate biolubricant over modified H-ZSM-5: Optimization by response surface methodology}, journal = {Journal of Energy Chemistry}, volume = {23}, number = {4}, year = {2014}, month = {JUL}, pages = {535-541}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The present study highlighted the use of modified H-ZSM-5 (Meso-HZ-5) as heterogeneous catalyst for the synthesis of octyl levulinate biolubricant by catalytic esterification of biomass derived renewable levulinic acid (LA) with n-octanol. The process variables such as catalyst loading (X-1), n-octanol to LA molar ratio (X-2) and reaction temperature (X-3) were optimized through response surface methodology (RSM), using Box-Behnken model. Analysis of variance was performed to determine the adequacy and significance of the quadratic model. The yield of octyl levulinate was obtained to be 99\% at optimum process parameters. The developed quadratic model was found to be adequate and statistically accurate with correlation value (R-2) of 0.9971 to predict the yield of octyl levulinate biolubricant. The study was also extended on the validation of theoretical and experimental data, including catalyst reusability.

}, keywords = {biolubricant, Esterification, H-ZSM-5, levulinic acid, octyl levulinate, Response surface methodology}, issn = {2095-4956}, doi = {10.1016/S2095-4956(14)60182-0}, author = {Nandiwale, Kakasaheb Y. and Yadava, Sunil K. and Bokade, Vijay V.} } @article { ISI:000329791800007, title = {Pseudo-homogeneous kinetic model for esterification of acetic acid with propanol isomers over dodecatungstophosphoric acid supported on montmorillonite k10}, journal = {Journal of Physical Organic Chemistry}, volume = {27}, number = {2}, year = {2014}, month = {FEB}, pages = {121-127}, publisher = {WILEY-BLACKWELL}, address = {111 RIVER ST, HOBOKEN 07030-5774, NJ USA}, abstract = {

Esterification of acetic acid with propanol isomers such as isopropanol and naEuropropanol was carried out over dodecatungstophosphoric acid (DTPA), dodecamolybdophosphoric acid ammonium salt hydrate, and sodium tungstate hydrated purified supported on montmorillonite K10, which were characterized by powder XaEuroray diffraction, BrunaueraEuro{\textquoteright}EmmettaEuro{\textquoteright}Teller, and temperature programmed ammonia desorption. A pseudoaEurohomogeneous (PaEuroH) kinetic model was established for esterification of acetic acid with propanol isomers over DTPA supported on montmorillonite K10. Effects of various parameters such as reaction time, speed of agitation, particle size, temperature, percent catalyst loading, molar ratio and mixture of propanol isomer were investigated in detail. The 20\% (w/w) DTPA/K10 was found to be an optimum solid catalyst with 82\% naEuropropanol and 53\% isopropanol conversion with 100\% selectivity toward propyl acetate. The 20\% (w/w) DTPA/K10 catalyst was found to be reusable for three cycles. The reaction follows secondaEuroorder kinetics with activation energies of 25.53aEuro?kJaEuro?mol(a?{\textquoteright}1) and 28.15aEuro?kJaEuro?mol(a?{\textquoteright}1) for isopropanol and naEuropropanol, respectively. PseudoaEurohomogeneous kinetic model fitted with R-2 value of trend line 0.999. This implies that esterification reaction is kinetically controlled owing to high activation energy. Copyright a (c) 2013 John Wiley \& Sons, Ltd.

}, keywords = {Acetic acid, dodecatungstophosphoric acid, Esterification, kinetic model, montmorillonite K10}, issn = {0894-3230}, doi = {10.1002/poc.3249}, author = {Gurav, Hanumant R. and Nandiwale, Kakasaheb Y. and Bokade, Vijay V.} } @article { ISI:000340427600056, title = {Selective synthesis of propofol (2,6-diisopropylphenol), an intravenous anesthetic drug, by isopropylation of phenol over H-beta and H-mordenite}, journal = {RSC Advances}, volume = {4}, number = {61}, year = {2014}, month = {JUL}, pages = {32467-32474}, publisher = {ROYAL SOC CHEMISTRY}, address = {THOMAS GRAHAM HOUSE, SCIENCE PARK, MILTON RD, CAMBRIDGE CB4 0WF, CAMBS, ENGLAND}, abstract = {

Propofol (2,6-diisopropylphenol/DIPP) is the world{\textquoteright}s most widely used intravenous general anesthetic and is typically synthesized by isopropylation of phenol over an acid catalyst. It is highly difficult to stabilize bio-oil containing phenolic compounds. The isopropylation of this phenol (a model compound representing species in bio-oils) is one of the options to stabilize the bio-oil and convert it into valuable products. Probably for the first time, H-beta- and H-mordenite-catalysed vapour phase isopropylation of phenol with isopropyl alcohol (IPA) was studied to selectively synthesize DIPP. The optimization of various operating parameters such as molar ratio (phenol : IPA), weight hourly space velocity (WHSV), reaction temperature and time on stream were performed. H-beta (94\% phenol conv. and 56\% DIPP sel.) was found to be a potential and more active catalyst than H-mordenite (68\% phenol conv. and 43\% DIPP sel.) at optimized process parameters. A kinetic model is proposed to probe the intricate reaction kinetics and validated (R-2 \> 0.98) by the experimental results. H-beta catalyst was observed to be stable for more than 25 h with 94\% phenol conversion and 56\% selectivity towards DIPP at optimized process parameters. The phenol conversion and DIPP selectivity obtained in the present study are higher than those reported so far. The activation energy obtained for isopropylation of phenol with IPA over H-beta is calculated to be 25.39 kJ mol(-1).

}, issn = {2046-2069}, doi = {10.1039/c4ra03004d}, author = {Nandiwale, Kakasaheb Y. and Bokade, Vijay V.} } @article { ISI:000348878600053, title = {Benzylation of acetic acid to benzyl acetate over highly active and reusable micro/meso-HZSM-5}, journal = {Chemical Engineering Research \& Design}, volume = {93}, year = {2015}, month = {JAN}, pages = {584-590}, publisher = {INST CHEMICAL ENGINEERS}, address = {165-189 RAILWAY TERRACE, DAVIS BLDG, RUGBY CV21 3HQ, ENGLAND}, abstract = {

Catalytic benzylation of acetic acid (AA) with benzyl alcohol (BA) to benzyl acetate was studied over zeolites viz. H-ZSM-5 (microporous, medium pore), Micro/Meso-HZSM-5 (combination of micro- and meso pore), H-Beta (microporous, large pore) to investigate catalytic activity and selectivity towards benzyl acetate. Micro/Meso-HZSM-5 obtained by desilication post-treatment has been employed as a heterogeneous catalyst for benzylation reaction probably for the first time. Micro/Meso-HZSM-5 was found to be a promising catalyst for benzylation with AA conversion of 94\%, selectivity towards benzyl acetate of 95\%. The detailed optimization of process parameters such as molar ratio, catalyst loading, reaction temperature and time was also presented. Micro/Meso-HZSM-5 catalyst was observed to be stable for six cycles (1 fresh and 5 recycles). The first order reaction kinetics (R-2 \>0.98) indicated that reaction rate constants increased with increasing reaction temperature. The activation energy for benzylation of AA with BA over Micro/Meso-HZSM-5 was obtained to be 15.07 kJ mol(-1), which is far less than the reported. (C) 2014 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.

}, keywords = {Acetic acid, Benzyl acetate, Benzyl alcohol, Benzylation, Micro/Meso-HZSM-5, Reaction kinetics}, issn = {0263-8762}, doi = {10.1016/j.cherd.2014.06.015}, author = {Nandiwale, Kakasaheb Y. and Galande, Nitish D. and Raut, Sunil A. and Bokade, Vijay V.} } @article { ISI:000356755500019, title = {Catalytic upgrading of citric acid to environmental friendly tri-butyl citrate plasticizer over ultra stable phosphonated Y zeolite}, journal = {Chemical Engineering Research \& Design}, volume = {98}, year = {2015}, month = {JUN}, pages = {212-219}, publisher = {INST CHEMICAL ENGINEERS}, address = {165-189 RAILWAY TERRACE, DAVIS BLDG, RUGBY CV21 3HQ, ENGLAND}, abstract = {

The catalytic synthesis of non-toxic/eco-friendly tributyl citrate (TBC) plasticizer by esterification of renewable citric acid (CA) with butanol would be completely sustainable route. In this context, catalytic performance of parent ultra stable Y (USY) and phosphonated USY catalysts were investigated for TBC synthesis. Parent USY and phosphonated USY catalysts were characterized by powder X-ray diffraction (XRD), N-2 adsorption-desorption, NH3 temperature programmed desorption (TPD), pyridine-Fourier Transform Infrared Spectroscopy (FTIR), FTIR, SEM, ICP. The influence of various process parameters such as phosphorous (P) loading (0 to 4 wt/\%), catalyst loading (5-25\%), molar ratio of CA to n-butanol (1:4 to 1:12), reaction temperature (383-423 K) and reaction time (1-5 h) have been investigated over USY catalyst with aim to maximize CA conversion and TBC yield. Amongst the studied catalysts, the 2\% (w/w) P/USY was found to be highly potential catalyst with complete CA conversion (100\%) and 93\% TBC yield. The present method of using 2\% (w/w) P/USY catalyst for the synthesis of TBC would be environmentally benign in the context of bio-renewable synthetic route, high catalytic activity, non-toxic product, long term stability and reusability of catalyst (five catalytic cycles). (c) 2015 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved,

}, keywords = {Butanol, Citric acid, heterogeneous catalysis, Plasticizer, Tributyl citrate}, issn = {0263-8762}, doi = {10.1016/j.cherd.2015.04.037}, author = {Nandiwale, Kakasaheb Y. and Gogoi, Pranjal and Bokade, Vijay V.} } @article { ISI:000355231200019, title = {Environmentally benign catalytic process for esterification of renewable levulinic acid to various alkyl levulinates biodiesel}, journal = {Environmental Progress \& Sustainable Energy}, volume = {34}, number = {3}, year = {2015}, month = {SEP}, pages = {795-801}, publisher = {WILEY-BLACKWELL}, address = {111 RIVER ST, HOBOKEN 07030-5774, NJ USA}, abstract = {

This study explores, the use of modified zeolite (Micro/Meso-HZ-5) obtained by desilication post-treatment as heterogeneous catalyst for esterification of biomass derived renewable levulinic acid (LA) with different alkyl alcohols such as methanol, ethanol, n-butanol, and n-octanol aiming to produce corresponding alkyl levulinate. This method of production of alkyl levulinates would be sustainable process, as it can be used as novel miscible diesel biofuels preventing global warming by decreasing atmospheric CO2. The LA conversion obtained over Micro/Meso-HZ-5 was higher than H-ZSM-5, which is due to the combined effect of increase in Bronsted acid sites, total acidity, and other properties such as BET surface area and the generation of mesoporosity. The maximum LA conversion of 91, 95, 96, and 98\% with 100\% selectivity toward alkyl levulinate was obtained, when LA was being esterified over Micro/Meso-HZ-5 with methanol, ethanol, n-butanol, and n-octanol, respectively, at optimal process parameters. Micro/Meso-HZ-5 catalyst was found to be reusable for six cycles. Furthermore, pseudo homogeneous (P-H) kinetic model of the esterification of LA with the studied four alcohols were established with R-2\>0.99, using the experimental data. A P-H kinetic model implies that, the esterification reaction follows second order reversible kinetics. (c) 2014 American Institute of Chemical Engineers Environ Prog, 34: 795-801, 2015

}, keywords = {biofuels, Esterification, kinetic model, levulinic acid, meso-HZ-5, micro}, issn = {1944-7442}, doi = {10.1002/ep.12042}, author = {Nandiwale, Kakasaheb Y. and Bokade, Vijay V.} } @article { ISI:000348924600005, title = {Esterification of renewable levulinic acid to n-butyl levulinate over modified H-ZSM-5}, journal = {Chemical Engineering \& Technology}, volume = {38}, number = {2}, year = {2015}, month = {FEB}, pages = {246-252}, publisher = {WILEY-V C H VERLAG GMBH}, address = {BOSCHSTRASSE 12, D-69469 WEINHEIM, GERMANY}, abstract = {

The synthesis of n-butyl levulinate, one of the most important biodiesel additives, by catalytic esterification of biomass-derived levulinic acid (LA) with n-butanol over modified H-ZSM-5 (micro/meso-HZ-5) in a closed-batch system is reported for the first time. The optimization of the reaction conditions such as the reactant molar ratio, the catalyst loading, the reaction time and the temperature was performed in view to maximize the yield of n-butyl levulinate. Micro/meso-HZ-5 was found to be the most efficient catalyst, with 98\% yield of n-butyl levulinate and a reusability for six cycles, which is higher than reported in the literature. A possible catalytic mechanism for the esterification reaction is also proposed. A second-order pseudo-homogeneous model with R-2 \> 0.97 confirmed that the esterification reaction is performed in the kinetic regime due to the high activation energy of 23.84 kJ mol(-1).

}, keywords = {Esterification, kinetic model, levulinic acid, Micro/meso-HZ-5, n-Butyl levulinate}, issn = {0930-7516}, doi = {10.1002/ceat.201400326}, author = {Nandiwale, Kakasaheb Y. and Bokade, Vijay V.} } @article { ISI:000361834900002, title = {One step synthesis of ethyl levulinate biofuel by ethanolysis of renewable furfuryl alcohol over hierarchical zeolite catalyst}, journal = {RSC Advances}, volume = {5}, number = {97}, year = {2015}, month = {SEP}, pages = {79224-79231}, publisher = {ROYAL SOC CHEMISTRY}, address = {THOMAS GRAHAM HOUSE, SCIENCE PARK, MILTON RD, CAMBRIDGE CB4 0WF, CAMBS, ENGLAND}, abstract = {

Ethanolysis of renewable furfuryl alcohol (FAL) to ethyl levulinate (EL) biofuel over various zeolites viz. H-ZSM-5 (microporous, medium pore), Hierarchical-HZ-5 (combination of micro-and meso pore), H-Beta (microporous, large pore) and Ultra Stable Y (USY, microporous, large pore) was studied in detail. To the best of our knowledge, probably for the first time, Hierarchical-HZ-5 synthesized by desilication post-treatment has been employed as a heterogeneous catalyst for ethanolysis of FAL. The synthesized catalysts were characterized by powder X-ray diffraction (PXRD), temperature programmed NH3 desorption (TPAD), Energy dispersive X-ray analysis (EDAX), etc. Response surface methodology (RSM) with Box-Behnken experimental design (BBD) was used to investigate the influence of three crucial process variables of ethanolysis such as ethanol to FAL molar ratio, percent catalyst loading and reaction temperature on EL yield. The optimization tool of design expert software was employed to obtain the optimum reaction parameters for FAL ethanolysis over Hierarchical-HZ-5 catalyst. Three intermediates of FAL ethanolysis reaction such as, ethoxymethylfuran (EMF), 4,5,5-triethoxypentan-2-one and diethyl ether (DEE) have been identified and quantified from the product mixture with the aid of Gas Chromatography-Mass Spectroscopy (GC-MS). Hierarchical-HZ-5 was found to be a potential catalyst for ethanolysis of FAL with 73\% EL yield and 26\% EMF yield at optimized process parameters.

}, issn = {2046-2069}, doi = {10.1039/c5ra13520f}, author = {Nandiwale, Kakasaheb Y. and Pande, Ashwini M. and Bokade, Vijay V.} } @article { ISI:000355786500005, title = {Phosphonated USY, a promising catalyst for the development of environmentally benign biodiesel (methyl acetate) process}, journal = {Journal of Energy Chemistry}, volume = {24}, number = {3}, year = {2015}, month = {MAY}, pages = {285-290}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The present study focuses on the evaluation of the potential applicability of Ultra Stable Y (USY) and phosphonated USY (1 wt\%-4 wt\% phosphorous loading) as heterogeneous catalysts for biodiesel (methyl acetate) production. The synthesized catalysts were characterized by powder X-ray diffraction (XRD), Brunaer-Emmett-Teller (BET) surface area, total acidity by temperature-programmed desorption of ammonia (TPD-NH3) and Fourier Transform Infrared (FTIR) spectra. The performances of catalysts were evaluated for the transesterification of butyl acetate with methanol (a model reaction in biodiesel production). In view to obtain a maximum yield of methyl acetate, the optimization of process parameters such as reactant molar ratio, catalyst loading, reaction temperature and reaction time was performed. All the phosphonated USY catalysts showed higher catalytic activity than the parent USY, which can be attributed to the increase of total acidity due to phosphonation. 2 wt\% P/USY (2\% phosphorous loaded on USY) exhibited 92\% methyl acetate yield with 100\% selectivity, which was proved to be a potential catalyst for biodiesel production. The invented catalyst was found to be stable and reusable for five catalytic cycles, demonstrating that it might be a environmentally benign catalytic process.

}, keywords = {Biodiesel, methyl acetate, phosphonated USY, transesterification}, issn = {2095-4956}, doi = {10.1016/S2095-4956(15)60313-8}, author = {Nandiwale, Kakasaheb Y. and Gopal, Gahana C. and Bokade, Vijay V.} } @article { ISI:000349556700067, title = {Process optimization by response surface methodology for transesterification of renewable ethyl acetate to butyl acetate biofuel additive over borated USY zeolite}, journal = {RSC Advances}, volume = {5}, number = {22}, year = {2015}, month = {JAN}, pages = {17109-17116}, publisher = {ROYAL SOC CHEMISTRY}, address = {THOMAS GRAHAM HOUSE, SCIENCE PARK, MILTON RD, CAMBRIDGE CB4 0WF, CAMBS, ENGLAND}, abstract = {

Butyl acetate, a renewable biofuel additive was synthesized by transesterification of butanol with ethyl acetate via a renewable and sustainable route. Use of fermentation derived bio-butanol and bio-ethyl acetate for synthesis of butyl acetate would be a more advantageous route over conventional Fischer Esterification. For the first time, a heterogeneous zeolite catalyst such as Ultra Stable Y (USY) and its modified versions obtained by borating on parent USY were used for the synthesis of butyl acetate. Response surface methodology (RSM) was employed to optimize the process parameters for transesterification of butanol with ethyl acetate over a 4\% (w/w) B-USY catalyst. The influence of three crucial process variables such as catalyst loading, molar ratio, and reaction temperature on yield of butyl acetate were addressed by Box-Behnken experimental design (BBD). 4\% (w/w) B-USY was proved to be a potential catalyst with 96\% yield of butyl acetate at optimum process parameters. The 4\% (w/w) B-USY catalyst was found to be reusable for 6 catalytic cycles.

}, issn = {2046-2069}, doi = {10.1039/c4ra14771e}, author = {Nandiwale, Kakasaheb Y. and Galande, Nitish D. and Bokade, Vijay V.} } @article {45942, title = {Synthesis of non-toxic triethyl citrate plasticizer by esterification of renewable citric acid using modified zeolite}, journal = {Clean-Soil Air Water}, volume = {43}, year = {2015}, month = {JUN}, pages = {927-931}, type = {Article}, abstract = {

Triethyl citrate (TEC), a non-toxic plasticizer, was synthesized by esterification of renewable citric acid (CA, from entire waste of oranges) with ethanol over modified H-ZSM-5 (HZ-5) zeolite. Different micro-meso composites (M-HZ-5) with varying crystallinities were prepared by alkaline treatment of HZ-5. M-HZ-5(0.6) (87\% crystallinity) was observed to be a potential and environmentally benign catalyst with 96\% CA conversion, 64\% TEC selectivity (61.44\% TEC yield), and a reusability of six cycles. The probable catalytic mechanism of esterification was also proposed.

}, keywords = {Biowaste, Catalysts, green chemistry, Micro-mesopre composites, reusability}, issn = {1863-0650}, doi = {10.1002/clen.201400189}, author = {Nandiwale, Kakasaheb Y. and Borikar, Sanjay P. and Bokade, Vijay V.} } @article { ISI:000381328300009, title = {Isolation and characterization of new lignin streams derived from extractive-ammonia (EA) pretreatment}, journal = {Green Chemistry}, volume = {18}, number = {15}, year = {2016}, month = {AUG}, pages = {4205-4215}, publisher = {ROYAL SOC CHEMISTRY}, address = {THOMAS GRAHAM HOUSE, SCIENCE PARK, MILTON RD, CAMBRIDGE CB4 0WF, CAMBS, ENGLAND}, abstract = {

One of the key challenges facing lignin conversion to fuels and chemicals is related to the level of carbohydrate and ash impurities found in extracted lignin. Structural modifications of lignin may also occur as a result of biomass pretreatment and harsh lignin extraction protocols. Extractive-Ammonia (EA) is a new pretreatment technology that uses liquid ammonia to cleave lignin-carbohydrate complexes, decrystallize cellulose, solubilize lignin, and selectively extract Lignin from lignocellulosic biomass, enabling better utilization of both lignin and carbohydrate components in a biorefinery. The EA-based biorefinery produces two different lignin-rich streams, with different properties, that could potentially be upgraded to fuels and chemicals using green processes. In this work, a water/ethanol-based fractionation method was developed to enrich the ammonia-soluble extractives, resulting in a major product stream containing 92\% lignin. Detailed characterization of the various streams resulting from EA treatment, including compositional analysis, structural characterization by nuclear magnetic resonance (NMR) spectrometry, elemental analysis, molecular weight analysis, and thermo-gravimetric analysis provides a broad evaluation of the EA derived lignin product stream structures and properties, assessing their potential for commercial applications. In summary, EA-derived lignins preserve much of lignin{\textquoteright}s functionality, including the sensitive (3-aryl ether units. Nitrogen incorporation was observed in the lignin-rich streams, notably due to the presence of hydroxycinnamoyl amides formed during ammonia pretreatment.

}, issn = {1463-9262}, doi = {10.1039/c6gc00298f}, author = {Sousa, Leonardo da Costa and Foston, Marcus and Bokade, Vijay V. and Azarpira, Ali and Lu, Fachuang and Ragauskas, Arthur J. and Ralph, John and Dale, Bruce E. and Balan, Venkatesh} } @article { ISI:000374351200005, title = {Next-generation ammonia pretreatment enhances cellulosic biofuel production}, journal = {Energy \& Environmental Science}, volume = {9}, number = {4}, year = {2016}, month = {FEB}, pages = {1215-1223}, publisher = {ROYAL SOC CHEMISTRY}, address = {THOMAS GRAHAM HOUSE, SCIENCE PARK, MILTON RD, CAMBRIDGE CB4 0WF, CAMBS, ENGLAND}, abstract = {

A new liquid ammonia pretreatment methodology called Extractive Ammonia (EA) was developed to simultaneously convert native crystalline cellulose I-beta (CI) to a highly digestible cellulose IIII (CIII) allomorph and selectively extract up to B45\% of the lignin from lignocellulosic biomass with near-quantitative retention of all polysaccharides. EA pretreated corn stover yielded a higher fermentable sugar yield compared to the older Ammonia Fiber Expansion (AFEX) process while using 60\% lower enzyme loading. The EA process preserves extracted lignin functionalities, offering the potential to co-produce lignin-derived fuels and chemicals in the biorefinery. The single-stage EA fractionation process achieves high biofuel yields (18.2 kg ethanol per 100 kg untreated corn stover, dry weight basis), comparable to those achieved using ionic liquid pretreatments. The EA process achieves these ethanol yields at industrially-relevant conditions using low enzyme loading (7.5 mg protein per g glucan) and high solids loading (8\% glucan, w/v).

}, issn = {1754-5692}, doi = {10.1039/c5ee03051j}, author = {Sousa, Leonardo da Costa and Jin, Mingjie and Chundawat, Shishir P. S. and Bokade, Vijay V. and Tang, Xiaoyu and Azarpira, Ali and Lu, Fachuang and Avci, Utku and Humpula, James and Uppugundla, Nirmal and Gunawan, Christa and Pattathil, Sivakumar and Cheh, Albert M. and Kothari, Ninad and Kumar, Rajeev and Ralph, John and Hahn, Michael G. and Wyman, Charles E. and Singh, Seema and Simmons, Blake A. and Dale, Bruce E. and Balan, Venkatesh} } @article { ISI:000370104700016, title = {Optimization by box-behnken experimental design fur synthesis of n-hexyl levulinate biolubricant over hierarchical H-ZSM-5: an effort towards agricultural waste minimization}, journal = {Process Safety and Environmental Protection}, volume = {99}, year = {2016}, month = {JAN}, pages = {159-166}, publisher = {INST CHEMICAL ENGINEERS}, type = {Article}, address = {165-189 RAILWAY TERRACE, DAVIS BLDG, RUGBY CV21 3HQ, ENGLAND}, abstract = {

The present study is devoted to develop efficient catalytic process for conversion of agricultural waste feedstock to value added chemicals. In this context, the n-hexyl levulinate, a renewable biolubricant was synthesized by esterification of biomass derived levulinic acid (LA) with n-hexanol in a closed batch system. Hierarchical-HZ-5 (modified H-ZSM-5) was used as a heterogeneous acid catalyst. There are no reports available on the synthesis of n-hexyl levulinate biolubricant using renewable levulinic acid. The process variables such as catalyst to LA ratio (X-1), n-hexanol to LA molar ratio (X-2), reaction time (X-3) and reaction temperature (X-4) were optimized by response surface methodology (RSM), using the Box-Behnken model. Analysis of variance was done to check the suitability and significance of the quadratic model. The yield of n-hexyl levulinate obtained was 97\% with 100\% selectivity at optimum process parameters. The RSM analysis predicted that catalyst to LA ratio is most significant (value of p \< 0.0001) and n-hexanol to LA molar ratio is least significant (value of p = 0.0064) process parameter in esterification. The quadratic model established was revealed to be suitable and statistically precise with correlation value (R-2) of 0.9837 to predict the yield of n-hexyl levulinate. (C) 2015 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.

}, keywords = {Agricultural waste feedstock, Esterification, Hierarchical-HZ-5, n-Hexyl levulinate, Optimization, Response surface methodology}, issn = {0957-5820}, doi = {10.1016/j.psep.2015.11.003}, author = {Nandiwale, Kakasaheb Y. and Bokade, Vijay V.} } @article {43058, title = {Sustainable catalytic process for synthesis of triethyl citrate plasticizer over phosphonated USY zeolite}, journal = {Bulletin of Chemical Reaction Engineering and Catalysis}, volume = {11}, year = {2016}, month = {OCT}, pages = {292-298}, abstract = {

Fruits wastage is harmful to health and environment concerning spreading diseases and soil pollution, respectively. To avoid this issue, use of citrus fruit waste for the production of citric acid (CA) is one of viable mean to obtain value added chemicals. Moreover, synthesis of triethyl citrate (TEC), a non-toxic plasticizer by esterification of CA with ethanol over heterogeneous catalyst would be renewable and sustainable catalytic process. In this context, parent Ultrastable Y (USY) and different percentage phosphonated USY (P-USY) zeolites were used for the synthesis of TEC in a closed batch reactor, for the first time. The synthesized catalysts were characterized by N2-adsorption desorption isotherm, powder X-ray diffraction (XRD) and NH3 temperature programmed desorption (TPD. Effect of reaction conditions, such as the molar ratio of ethanol to CA (5:1 - 20:1), the catalyst to CA ratio (0.05-0.25) and reaction temperature (363-403 K), were studied in view to maximizing CA conversion and TEC yield. Phosphonated USY catalysts were found to be superior in activity (CA conversion and TEC yield) than parent USY, which is attributed to the increased in total acidity with phosphonation. Among the studied catalysts, the P2USY (2\% phosphorous loaded on USY) was found to be an optimum catalyst with 99\% CA conversion and 82\% TEC yield, which is higher than the reported values. This study opens new avenues of research demonstrating principles of green chemistry such as easy separable and reusable catalyst, non-toxic product, bio-renewable synthetic route, milder operating parameters and waste minimization.

}, doi = {10.9767/bcrec.11.3.569.292-298}, author = {Nandiwaleand, Kakasaheb Y. and Bokade, Vijay V.} } @article {45368, title = {Direct synthesis of diethyl carbonate from ethanol and carbon dioxide over ceria catalysts}, journal = {New Journal Of Chemistry}, volume = {42}, year = {2018}, month = {NOV}, pages = {17546-17552}, type = {Article}, abstract = {

Direct synthesis of diethyl carbonate (DEC) by carboxylation of ethanol with CO2 was investigated over ceria catalysts. 2-Cyanopyridine (2-CP) was used for trapping water formed in the reaction and to shift the equilibrium towards the product side. An optimal dependence (volcanic plot) of the catalytic activity on the acidity/basicity molar ratio was observed. Neat ceria (procured from Daiichi Kigenso Kagaku Kogyo Co. Ltd, Japan) showed higher catalytic activity than metal incorporated ceria catalysts. CeO2 had the right kind of acidity/basicity ratio to activate ethanol and CO2 simultaneously, yielding DEC. The catalyst was reusable. The yield of DEC obtained in this study using the commercial catalyst was higher than that reported by others using ceria catalysts prepared by other methods. Under optimum conditions (ethanol:2-CP molar ratio = 2:1, catalyst = 2.17 wt\% with respect to ethanol, CO2 pressure = 40 bar, reaction temperature = 150 degrees C and reaction time = 3 h) in a batch reaction, a DEC yield as high as 45 mol\% (i.e., 38.7 mmol mmol(-1) of CeO2) was obtained.

}, issn = { 1144-0546}, doi = {10.1039/c8nj04090g}, author = {Giram, Ganesh G. and Bokade, Vijay V. and Darbha, Srinivas} } @article {45404, title = { HPW anchored Meso-HZ-5, a novel catalyst for selective synthesis of ethyl levulinate biofuel by alcoholysis of biomass-derived furfuryl alcohol}, journal = {Environmental Progress \& Sustainable Energy}, volume = {37}, year = {2018}, month = {SEP}, pages = {1736-1742}, type = {Article}, abstract = {Ethanolysis of biomass derived furfuryl alcohol (FA) produces ethyl levulinate (EL), a biofuel additive and precursor for -valerolactone synthesis. The present study is devoted to develop an efficient and an environmentally benign catalytic system for one-pot conversion of FA to EL biofuel, by revealing an insight of the catalytic mechanism. The catalytic activity of H-ZSM-5, Meso-HZ-5 (desilicated H-ZSM-5) and different percentage H3PW12O40(HPW) anchored to Meso-HZ-5 catalysts have been evaluated for the FA ethanolysis. As per our knowledge, this is the first research reporting the application of HPW anchored to Meso-HZ-5 catalysts for the conversion of FA into EL in biomass utilization. These catalysts were synthesized and characterized by Powder X-ray diffraction (XRD), N-2 physisorption and temperature programmed NH3 desorption (TPAD). Products of FA ethanolysis viz., 4,5,5-triethoxypentan-2-one (TEP), ethoxy-methyl- furan (EMF), diethyl ether (DEE), EL were identified by Gas Chromatography-Mass Spectroscopy (GC-MS) and quantified by flame ionization detector (GC-FID). The physicochemical properties of catalysts were found to correlate to the product distribution matrix. Moreover, influences of several process parameters such as catalyst amount, reactant molar ratio, temperature and time on the extent of FA ethanolysis were systematically investigated. Under optimized conditions, 15\% (w/w) HPW/Meso-HZ-5 exhibited a remarkable catalytic performance with complete FA conversion (100\%) along with 97\% yield of EL, these activity values are superior than the previously reported studies. The present study provides an insight of the catalytic mechanism along with a potential environmental benign and the economic catalyst for the efficient synthesis of EL biofuel from the biomass-derived FA}, doi = { 10.1002/ep.12822}, author = {Nandiwale, Kakasaheb Y. and Pande, Ashwini M. and Bokade, Vijay V.} } @article {44213, title = {HxZr3-xPW12O40 as an insoluble and reusable heteropolyacid for highly selective dehydration of fructose to 5-hydroxymethyl fufural in DMSO system}, journal = {Chemistryselect}, volume = {3}, year = {2018}, month = {JAN}, pages = {832-836}, type = {Article}, abstract = {Dehydration of fructose is a way to produce an important platform chemical such as 5-hydroxymethylfurfural (HMF) which is widely used to synthesize variety of renewable chemicals and fuel. Heteropoly acid, H3PW12O40 is highly soluble strong acidic catalyst with well-defined structure. This study reports the modification of soluble heteropoly acid to insoluble and reusable heteropolyacid (HxZr3-xPW12O40 ) by exchanging with Zr and investigation of its catalytic performance in selective transformation of renewable fructose to 5-HMF in Dimethyl sulfoxide (DMSO) system. The physico-chemical properties of H(x)Zr(3-x)PW(12)O(40)were derived from Powder-XRD, NH3-TPAD and FT-IR technique. The characterization of HxZr3-xPW12O40 revealed that the Keggin structure of HPA remained intact as proton replaced by Zr. The partial exchange of Zr in H2Zr1PW12O40 catalyst resulted in an increase in acidity, however further increase of Zr above 1, acidity was found to be decreased. At optimized reaction condition, 5-HMF yield of 85\% with 100\% selectivity was achieved with H1Zr2 PW12O40 catalyst at much lower reaction time of 10 min than reported. The catalyst was observed to be recoverable, reusable as compared to parent H3PW12O40.}, doi = {10.1002/slct.201702669}, author = {Mulik, Nagesh L. and Niphadkar, Prashant S. and Pandhare, Kiran V. and Bokade, Vijay V.} } @article {46147, title = {Epoxidation of karanja (Millettia pinnata) oil methyl esters in the presence of hydrogen peroxide over a simple niobium-containing catalyst}, journal = {Catalysts}, volume = {9}, year = {2019}, month = {APR}, pages = {344}, type = {Article}, abstract = {

The synthesis, characterization and catalytic performance of a conceptually simple, novel NbOx-SiO2 catalyst are here described. The niobium(V)-silica catalyst was prepared starting from cheap and viable reactants, by alkaline deposition of NH4Nb(C2O4)(2)H2O in the presence of fructose as a stabilizer and subsequent calcination. The NbOx-SiO2 solid (0.95 Nb wt.\%) was tested in the liquid-phase epoxidation with aqueous hydrogen peroxide of methyl oleate, as a model substrate. It was then tested in the epoxidation of a mixture of methyl esters (FAMEs) obtained by transesterification with methanol and purification of karanja oil, extracted from the autochthonous Indian variety of Millettia pinnata tree. The catalyst showed a promising performance in terms of methyl oleate conversion (up to 75\%) and selectivity to epoxide (up to 82\%). It was then tested on the FAME mixture from karanja oil, where interesting conversion values were attained (up to 70\%), although with lower selectivities and yields to the mixture of desired epoxidized FAMEs. The solid withstood four catalytic cycles overall, during which a non-negligible surface reorganization of the Nb(V) sites was observed. However, this restructuring did not negatively affect the performance of the catalysts in terms of conversion or selectivity.

}, keywords = {epoxidation, fatty acid methyl esters, heterogeneous catalysis, Hydrogen peroxide, karanja oil, mesoporous silica catalyst, Millettia pinnata, niobium catalysts}, issn = {2073-4344}, doi = {10.3390/catal9040344}, author = {Scotti, Nicola and Ravasio, Nicoletta and Evangelisti, Claudio and Psaro, Rinaldo and Penso, Michele and Niphadkar, Prashant S. and Bokade, Vijay V. and Guidotti, Matteo} } @article {47148, title = {Carbon supported size-controlled ru catalysts for selective levulinic acid hydrogenation into γ-valerolactone}, journal = {Journal of Siberian Federal University-Chemistry}, volume = {13}, year = {2020}, month = {JAN}, pages = {5-16}, type = {Article}, abstract = {

Liquid phase levulinic acid hydrogenation into γ-valerolactone in 1,4-dioxane as a solvent (165{\textdegree}C, 20 bar) was studied over a range of Ru monometallic catalysts using mesoporous carbon material Sibunit as a support. In addition to the catalyst prepared by impregnation with RuCl3.nH2O (0.1 M) followed by reduction in H2, size-controlled Ru(NPs)/Sibunit catalysts were synthesized by immobilization of polyvinylpyrrolidone (PVP) stabilized Ru nanoparticles (NPs) (dRu=2.4 nm). Сarbon supported colloidal Ru NPs were not studied earlier in levulinic acid hydrogenation. Activity of colloidal Ru(NPs)/Sibunit catalysts was found to be lower than that of impregnated Ru/Sibunit which could be attributed to hampering effect of PVP. However, colloidal Ru(NPs)/Sibunit purified by thermal treatment in air (180{\textdegree}C) followed by reduction in H2 (400{\textdegree}C) exhibited the same activity as impregnated one yielding 93\% γ-valerolactone at 100\% levulinic acid conversion. Applicability of supported PVP-assisted colloidal Ru NPs in hydrogenation of levulinic acid illustrates a potential to prepare more efficient catalysts for this reaction with a desired particle size. The catalysts were characterized by TEM, XRF, and N2 physisorption to compare their physical chemical properties.

}, doi = {10.17516/1998-2836-0166}, author = {Simakova, Irina L. and Demidova, Yuliya S. and Simonov, Mikhail N. and Niphadkar, Prashant S. and Bokade, Vijay V. and Devi, Nandini and Dhepe, Paresh L. and Murzin, Dmitry Yu} } @article {46967, title = {Synthesis of ethyl furfuryl ether (potential biofuel) by etherification of furfuryl alcohol with ethanol over heterogenized reusable H1Cs2PW12O40 catalyst}, journal = {Research on Chemical Intermediates}, volume = {46}, year = {2020}, month = {APR}, pages = {2309-2325}, type = {Article}, abstract = {

{Ethyl furfuryl ether (EFE) considered as potential biofuel can replace petroleum diesel up to 100\%. EFE also has efficient blending properties with biodiesel to improve its cold flow properties. Herein we demonstrate efficient synthesis of EFE by etherification of renewable furfuryl alcohol (FAlc) with ethanol over heterogenized heteropoly acids. Cs-exchanged heterogenized heteropoly acid (H3-xCsxPW12O40

}, keywords = {B, etherification, Ethyl furfuryl ether, Furfuryl alcohol, H3-xCsxPW12O40, Heterogenized heteropoly acid, L ration}, issn = {0922-6168}, doi = {10.1007/s11164-020-04093-z, Early Access Date = FEB 2020}, author = {Mulik, Nagesh L. and Niphadkar, Prashant S. and Bokade, Vijay V.} } @article {47585, title = {Active nickel hollow nanosphere supported over SiO2 catalyst for reduction of nitro compound}, journal = {Particulate Science and Technology}, volume = {40}, year = {2021}, month = {APR}, pages = {325-335}, type = {Article}, abstract = {

Nickel hollow nanospheres (Ni HNSs) was prepared by solvothermal method using mixture of ethylenediamine (EN) and ethanol (ET), sodium borohydride as reducing agent and nickel chloride hexahydrate as precursor. The particle size of the Ni HNSs were tuned by varying several parameters including precursor concentrations, reaction temperatures (130-190 degrees C), and ET to EN volume ratios. The particle size and morphology of Ni HNSs were confirmed by dynamic light scattering and transmission electron microscope, respectively. Spherical shape of Ni nanoparticles of 300 nm size having similar to 200 nm hollow space and 50 nm thickness was achieved at optimize condition of 4:6 volume ratio of ET/EN, 150 degrees C temperature, 0.1 M NaBH4 concentration, and 7 h. Ni HNSs supported over SiO2 (Ni HNSs/SiO2) with different loading of Ni HNSs (1-10 wt.\%) were prepared by impregnation method. The catalyst was characterized by X-ray diffraction, and inductively coupled plasma - optical emission spectroscopy. The catalytic performance of Ni HNSs/SiO2 was carried out in the reduction of 4-Nitrophenol (4-NP) to 4 - Aminophenol (4-AP). 5 wt.\% Ni HNSs/SiO2 exhibited 87\% reduction of 4-NP in 25 min and stable up to 6 catalyst cycles due to higher surface area of the catalyst.

}, keywords = {4-Aminophenol, 4-nitrophenol, Catalyst, hollow nanospheres, Nanoparticles, Nickel}, issn = {0272-6351}, doi = {10.1080/02726351.2021.1947424}, author = {Pawar, Priyanka S. and Lokhande, Aboli A. and Nandanwar, Sachin U. and Niphadkar, Prashant S. and Bokade, Vijay V.} } @article {47071, title = {Effect of rice husk particle size on ZSM-5 physico-chemical properties for selective formation of 1,3,5-trimethyl-2-benzylbenzene (Pharmaceutical Intermediate)}, journal = {ChemistrySelect}, volume = {6}, year = {2021}, month = {FEB }, pages = {1255-1262}, type = {Article}, abstract = {

Rice husk, rich in silica and abundantly available as waste, is presently destroyed by burning, which creates environmental issues. Thus, it will be advantageous if this rice husk waste can be used for preparation of valuable products. One of the application is its use as silica source in the synthesis of zeolites like ZSM-5, which are silico-aluminates. Rice husk waste is available in wide range of particle sizes in agricultural farms. There is no study available in open literature on use of these wide particle ranges for its direct application. This paper is an attempt to use wide particle size rice husk, its effect on ZSM-5 synthesis and its physico-chemical properties. Further these prepared ZSM-5 catalyst was evaluated for benzylation of mesitylene reaction. The study found that, rice husk of 600 mu m particle size is optimum as far as ZSM-5 synthesis, its physicochemical properties and further its application in mesitylene benzylation reaction.

}, keywords = {Mesitylene, Particle size, rice husk, Silica Source, ZSM-5}, issn = {2365-6549}, doi = {10.1002/slct.202004802}, author = {Ghuge, Gorakh and Niphadkar, Prashant and Rathod, Simmy and Bokade, Vijay V.} } @article {46681, title = {Milder operating parameters for one-step conversion of fructose to levulinic acid over sulfonated H-beta zeolite in aqueous media}, journal = {Environmental Progress \& Sustainable Energy}, volume = {40}, year = {2021}, month = {JAN}, pages = {e13530}, type = {Article}, abstract = {

The sulfonated H-beta zeolite was successfully prepared and used for the synthesis of levulinic acid (LA) fromD-fructose. The catalyst was characterized by powder X-ray diffraction, Fourier transform infrared spectroscopy, scanning electron microscope, N-2 physisorption, NH3-temperature programmed desorption and carbon-hydrogen-nitrogen-sulfur analysis. The total acid amount is increased with increase in sulfur loading, confirmed that the sulfonic acid group (SO3-H) is successfully grafted onto zeolite structure. The various parameters such as different amount of sulfur loading, reaction temperature, time, catalyst loading was studied for selective production of LA. The catalytic activity of sulfonated H-beta (S-beta) zeolite was found to be efficient for synthesis of LA from D-fructose in aqueous media. Maximum LA yield of 43.5 mol\%, low HMF yield (\<1\%) with 98.15\% fructose conversion was obtained with 3\% S-beta catalyst at 160 degrees C for 7 hr. The catalyst was reusable for minimum three times by H2O2 regeneration. This study provides the new zeolitic catalyst for the efficient production of LA at shorter reaction time (7 hr) and low catalyst to substrate ratio (0.7:1).

}, keywords = {conversion, D-fructose, H-beta, HMF, levulinic acid, sulfonated zeolite, yield}, issn = {1944-7442}, doi = {10.1002/ep.13530, Early Access Date = OCT 2020}, author = {Bisen, Swapneel K. and Niphadkar, Prashant S. and Nandanwar, Sachin U. and Simakova, Irina and Bokade, Vijay V.} } @article {47811, title = {Milder operating parameters for one-step conversion of fructose to levulinic acid over sulfonated H-β zeolite in aqueous media}, journal = {Environmental Progress \& Sustainable Energy}, volume = {40}, year = {2021}, month = {FEB}, pages = {e13530}, type = {Article}, abstract = {Abstract The sulfonated H-β zeolite was successfully prepared and used for the synthesis of levulinic acid (LA) from D-fructose. The catalyst was characterized by powder X-ray diffraction, Fourier transform infrared spectroscopy, scanning electron microscope, N2 physisorption, NH3-temperature programmed desorption and carbon{\textendash}hydrogen{\textendash}nitrogen{\textendash}sulfur analysis. The total acid amount is increased with increase in sulfur loading, confirmed that the sulfonic acid group (SO3-H) is successfully grafted onto zeolite structure. The various parameters such as different amount of sulfur loading, reaction temperature, time, catalyst loading was studied for selective production of LA. The catalytic activity of sulfonated H-β (S-β) zeolite was found to be efficient for synthesis of LA from D-fructose in aqueous media. Maximum LA yield of 43.5 mol\%, low HMF yield (<1\%) with 98.15\% fructose conversion was obtained with 3\% S-β catalyst at 160{\textdegree}C for 7 hr. The catalyst was reusable for minimum three times by H2O2 regeneration. This study provides the new zeolitic catalyst for the efficient production of LA at shorter reaction time (7 hr) and low catalyst to substrate ratio (0.7:1).}, keywords = {conversion, D-fructose, H-β, HMF, levulinic acid, sulfonated zeolite, yield}, doi = {10.1002/ep.13530}, url = {https://aiche.onlinelibrary.wiley.com/doi/abs/10.1002/ep.13530}, author = {Bisen, Swapneel K. and Niphadkar, Prashant S. and Nandanwar, Sachin U. and Simakova, Irina and Bokade, Vijay V.} } @article {47116, title = {One-pot cascade conversion of renewable furfural to levulinic acid over a bifunctional H3PW12O40SiO2 catalyst in the absence of external H-2}, journal = {Energy \& Fuels}, volume = {35}, year = {2021}, month = {JAN }, pages = {539-545}, type = {Article}, abstract = {

The conversion of biomass-derived furfural (FUR) to levulinic acid (LA), a versatile platform chemical, involves catalytic hydrogenation of FUR followed by acid hydrolysis to LA. However, this two-step process demands expensive separation and purification of the furfuryl alcohol (FAL) intermediate. Herein, we demonstrate an ingenious catalytic strategy for the one-pot cascade conversion of FUR to LA over a bifunctional catalyst without using pure external H-2. Isopropyl alcohol (IPA) served a dual role as a hydrogen donor and solvent while inhibiting the side reactions. Catalysts with a tunable surface area and acidity were synthesized by impregnating different percentages of H3PW12O40 (heteropolyacid) over a SiO2 support. The bifunctionality of the H3PW12O40/SiO2 catalyst is ascribed to the mutual coexistence of Lewis and Brvinsted acid sites. The Lewis acid sites imparted by active W metal sites adsorb hydrogen proton for catalytic transfer hydrogenation of FUR to FAL, while the predominant Brvinsted acid sites catalyze the hydrolysis of FAL to LA. Consequently, H3PW12O40/SiO2 revealed to be a potential catalyst producing an similar to 51\% LA yield under optimized reaction conditions. Moreover, the catalyst was found to be reusable for three catalytic cycles. This study paves the way to develop future biorefinery, particularly direct conversion of FUR to LA over a bifunctional catalyst with a liquid H-donor, in an environmentally benign manner and comply with the green chemistry principles.

}, issn = {0887-0624}, doi = {10.1021/acs.energyfuels.0c03326}, author = {Nandiwale, Kakasaheb Y. and Vishwakarma, Mona and Rathod, Simmy and Simakova, Irina and Bokade, Vijay V.} } @article {47129, title = {Review on selective production of acetophenone from oxidation of ethylbenzene over heterogeneous catalysts in a decade}, journal = {Catalysis Letters}, year = {2021}, month = {JAN}, type = {Article; Early Access 2021}, abstract = {

The consumption of acetophenone (AP) is increasing worldwide because of its applications in products such as alcohol, aldehydes, resins, esters, fragrances, and pharmaceuticals. AP is manufactured via several methods like decomposition of cumene hydroperoxide, Hock process, and Friedel-Crafts acylation reaction using homogeneous catalysts with solvent and oxidant. However, it causes several environmental problems that deteriorate the production of AP with these methods. Oxidation of ethylbenzene (EB) is one of the promising methods to synthesize AP in liquid and vapor phases reaction using heterogeneous catalysts, which plays a vital role for selective production of AP. In this review, numerous heterogeneous catalysts are discussed including transition metal nanoparticles, transition metal complexes, and metal free catalysts (carbon nanotubes) used in last 10 years for oxidation of EB. Additionally, catalyst activity along with reaction parameters and its effect, mechanisms, and kinetics study are summarized in this article. The future scope of this reaction is also highlighted. Moreover, this work identifies best catalysts for bulk production of AP with high yield to satisfy global requirement.

}, keywords = {acetophenone, ethylbenzene, Heterogeneous catalysts, Oxidation reaction, reaction mechanisms}, issn = {1011-372X}, doi = {10.1007/s10562-020-03474-8, Early Access Date = JAN 2021}, author = {Nandanwar, Sachin U. and Rathod, Simmy and Bansal, Videsha and Bokade, Vijay V.} } @article {47895, title = {Catalytic activity of CuFe2O4 spinel oxide for liquid-phase oxidation of cinnamyl alcohol}, journal = {ChemistrySelect}, volume = {7}, year = {2022}, month = {FEB}, pages = {e202104441}, type = {Article}, abstract = {

CuFe2O4 spinel oxide catalyst was synthesized by sol-gel and co-precipitation methods for liquid phase oxidation of Cinnamyl alcohol (CnOH) to Cinnamaldehydes (CnHO) using tert-Butyl hydroperoxide (TBHP) as oxidising agent. Spinel oxide catalyst was characterized by different techniques such as X-ray diffraction (XRD), N-2 adsorption-desorption, BET surface area, and X-ray photoelectron spectroscopy (XPS) to understand the structural, physical properties and oxidation state of the catalyst. The result shows that catalyst prepared by sol-gel method was found higher surface area and smaller crystalline size than co-precipitation method. XPS data confirm the formation of Cu2+ in the spinel which helps to improve the catalytic activity of oxidation. This reaction follows radical mechanism, and exhibited 76.7 \% of CnOH conversion and 68.4 \% of CnHO, and 24.8 \% benzaldehyde (benzald) selectivity using TBHP at 60 degrees C. Kinetic data reveal that 41.2 kJ/mol of activation energy for the reaction. The higher activity of spinel oxide catalyst could be due synergetic effect of spinel (88 \%) and oxides (12 \%) formed in the catalyst, which helps to provide the oxygen during reaction. The contribution of Cu2+ is higher in sol-gel than co-precipitation, which may provide the better reactivity of catalyst. This work helps to select the effective and cost-effective catalyst for the oxidation of CnOH.

}, keywords = {Catalysts, Cinnamaldehyde, Cinnamyl Alcohol, Cupper, iron, oxide, spinel}, issn = {2365-6549}, doi = {10.1002/slct.202104441}, author = {Dange, Rutvija M. and Niphadkar, Prashant S. and Bokade, Vijay V. and Nandanwar, Sachin U.} } @article {47984, title = {Methanol-to-light olefins reaction using Zn-Ag modified SSZ-13 catalyst}, journal = {ChemistrySelect}, volume = {7}, year = {2022}, month = {SEP}, pages = {e202201476}, type = {Article}, abstract = {

The 2 wt.\% of Zn and Ag (Zn1-x-Ag-x; x=0.2, 0.4, 0.6 \%) modified SSZ-13 (SZ-13) zeolite was prepared by wet-impregnation method, and its catalytic activity was demonstrated for methanol-to-olefin (MTO). The Zn-0.6-Ag-0.4/SZ-13 catalyst exhibited high catalytic activity due to change in properties of catalyst. The Zn particles were highly dispersed inside the SZ-13; while Ag particles were dispersed on the surface of SZ-13, confirmed by HRTEM and surface area. The small \% of Ag over SZ-13 promotes ethylene production via aromatization of reaction, and highly dispersed Zn on SZ-13 help to produce stable ethylene and propylene. The Zn-0.6-Ag-0.4/SZ-13 catalyst showed (similar to 10 \%) higher light olefin (87 \%) selectivity than parent SZ-13 as well as mono metal incorporated SZ-13. The higher catalytic activity was attributed due to effect of both metals (Zn and Ag), where Ag promotes partial aromatization on the surface, and Zn increases the Lewis acidity in the zeolite pore. This catalyst can help to improve the selectivity of light olefin using MTO reaction.

}, keywords = {Ethylene, Methanol-to-Olef, Propyl, Silver, SSZ, zinc}, issn = {2365-6549}, doi = {10.1002/slct.202201476}, author = {Dange, Rutvija M. and Gawali, Chirag B. and Niphadkar, Prashant S. and Bokade, Vijay V. and Nandanwar, Sachin U.} } @article {48741, title = {Direct conversion of N-acetyl-d-glucosamine to N-containing heterocyclic compounds 3-acetamidofuran and 3-acetamido-5-acetyl Furan}, journal = {Waste and Biomass Valorization}, volume = {14}, year = {2023}, month = {DEC}, pages = {4201-4214}, type = {Article}, abstract = {

Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that La2O3 was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, N-2 sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Bronsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). La2O3 catalyst showed optimum 50\% 3AF yield from N-acetyl glucosamine at 180 degrees C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach.{GRAPHICAL ABSTRACT

}, keywords = {3-acetamido-5-acetylfuran, 3-acetamidofuran, dehydration, heterogeneous catalysis, Lanthanum oxide, N-acetyl-D-glucosamine, renewable feedstock}, issn = {1877-2641}, doi = {10.1007/s12649-023-02127-2}, author = {Shaikh, Samrin S. and Patil, Chetana R. and Lucas, Nishita and Bokade, Vijay V. and Rode, Chandrashekhar V.} } @article {48702, title = {Equilibrium adsorption of nitrogen, oxygen, and argon on silver-exchanged hierarchical ETS-10}, journal = {Journal of Chemical and Engineering Data}, volume = {68}, year = {2023}, month = {JUL}, pages = {2159-2172}, type = {Article}, abstract = {

Silver-exchanged hierarchical ETS-10(Ag-H-ETS-10) was synthesizedusing Ag+ exchange with hierarchical Engelhard titanosilicate(H-ETS-10) using silver nitrate solution. The physical propertiesof the adsorbent were analyzed using X-ray diffraction (XRD), BETsurface area, nitrogen adsorption-desorption, pore volume,energy dispersive spectroscopy (EDS), and high resolution-transmissionelectron microscopy (HR-TEM). N-2 physisorption data confirmedthat a micro-mesoporous (bimodal) structure was created in the Ag-H-ETS-10.The equilibrium adsorbent data of pure gases N-2, O-2, and Ar were investigated in the temperature range from 288to 318 K up to 10 bar. The equilibrium adsorption capacity of Ag-H-ETS-10was found to be 1.12 mmol g(-1) for N-2,0.87 mmol g(-1) for O-2, and 1.09 mmol g(-1) for Ar at 298 K and \& SIM;10 bar. \& SIM;20\% higheradsorption capacity was found for N-2 and Ar in Ag-H-ETS-10compared to Ag-ETS-10. The higher sorption capacity was attributedto the formation of a bimodal structure and \& pi;-complexation interactionby the Ag cation, which allows a multilayer of N-2 and Armolecules. The Sips isotherm model was well fitted for the Ag-H-ETS-10experimental data among Langmuir, Freundlich, Toth, and Temkin models.The measured equilibrium adsorption data for Ag-H-ETS-10 can be usefulfor the O-2 purification process.

}, issn = {0021-9568}, doi = {10.1021/acs.jced.3c00124}, author = {Shrotri, Aadesh R. and Niphadkar, Prashant S. and Bokade, Vijay V. and Nandanwar, Sachin U.} } @article {48905, title = {Effect of CTMABr/SiO2 molar ratio in synthesis of micro-mesoporous ZSM-5 composite and its application in 5-EMF (biofuel additive) formation}, journal = {Environmental Progress and Sustainable Energy }, volume = {43}, year = {2024}, month = {JAN}, type = {Article}, abstract = {

Synthesis of micro-mesoporous zeolite composite with optimum micro and mesoporosity is an emerging research area due to its wide applications, especially in bulk chemical or biomass transformations. It offers advantages in preserving zeolite crystallinity, creating mesoporosity and converting bulky molecules into valuable products. This work presents the process of preparing bimodal micro-mesoporous ZSM-5 using dual templates (CTMABr and TPABr). XRD, N2 adsorption-desorption, SEM, TEM, Si-29, and Al-27 NMR were used to analyze the two-dimensional micro-mesoporous ZSM-5. One-step synthesis of bimodal micro-mesoporous ZSM-5 features dual micro/mesoporosity by a marginal decrease in the crystallinity (71\%). Micro-mesoporous ZSM-5 composite was found to be dependent on the optimum CTMABr/SiO2 molar ratio of 0.04 to 0.06. The micro-mesoporous ZSM-5 zeolite composite was evaluated for cascade synthesis of 5-EMF (methoxymethyl furfural- biofuel additive) from fructose and exhibited a five fold increase in 5-EMF yield to 24.2\% as compared with parent ZSM-5 (4.6\%).

}, keywords = {fructose, methoxymethyl furfural-biofuel additive, micro-meso composite, ZSM-5}, issn = {1944-7442}, doi = {10.1002/ep.14258}, author = {Manal, Prajakta N. and Niphadkar, Prashant S. and Nandanwar, Sachin U. and Bokade, Vijay V.} } @article {49769, title = {Binderless low silica X zeolite for methane separation from binary CO2/CH4 biogas stream: A comprehensive experimental and computational study}, journal = {Journal of Industrial and Engineering Chemistry}, volume = {149}, year = {2025}, month = {SEP }, pages = {705-719}, type = {Article}, abstract = {

This study presents the synthesis of binderless Na-LSX (B-Na-LSX) and binderless NaK-LSX (B-NaK-LSX). XRD, SEM, EDS, and N-2 physisorption were used for characterization of samples. Computational modelling of prepared sorbent was performed for the fundamental understanding of zeolite topology and adsorption behaviour. The breakthrough experiments are used to evaluate the adsorption capacities on CO2/CH4 (40/60 vol\%) binary biogas stream. The results were compared with commercial Na-LSX (C-Na-LSX). The breakthrough adsorption capacity of B-Na-LSX was 3.08 mmol g(-1) and 0.29 mmol g(-1) of CO2 and CH4, respectively, at 300 K and 1 bar. CO2 sorption capacity of B-Na-LSX was similar to 11 \% and similar to 17 \% higher than B-NaK-LSX (2.77 mmol g(-1)) and C-Na-LSX (2.56 mmol g(-1)), respectively. DFT study reveals that the higher adsorption of CO2 over CH4 was attributed to higher charge transfer from CO2 to zeolite framework. Dual-bed six-step Pressure Swing Adsorption (PSA) was performed on B-Na-LSX at 6 bar. similar to 232 cycles were run with above 98 \% of CH4 purity and similar to 74 \% of recovery. The life-cycle test of sorbent was studied. It was implied that the designed sorbent is effective to produce the high purity of CH4 and can be utilized for a longer period for CH4 production.

}, keywords = {Binderless, Biogas, LSX zeolite, methane, PSA, Separation}, issn = {1226-086X}, doi = {10.1016/j.jiec.2025.02.031}, author = {Yadav, Tushar R. and Shrotri, Aadesh R. and Kate, Pranjali N. and Devasia, George and Niphadkar, Prashant S. and Mali, Nilesh A. and Krishnamurty, Sailaja and Bokade, Vijay V. and Nandanwar, Sachin U.} } @article {49812, title = {Influence of physicochemical properties of seed on template-free ferrierite synthesis and its application in oleic acid isomerization}, journal = {Journal of Chemical Sciences}, volume = {137}, year = {2025}, month = {JUL}, pages = {62}, type = {Article}, abstract = {

We have reported an effective, seed-assisted organic structure directing agent (OSDA) free synthesis of ferrierite (FER) zeolites. In the current study, we have observed effects of physicochemical properties of two different seeds over synthesis of FER zeolites. The physicochemical properties of seeds, such as particle size and phase purity impart significantly over crystallization time and overall synthesis duration, costs of process and crystalline nature of FER zeolites. It is noteworthy that particle size of seed mainly affects the kinetics of crystallization for concerned FER zeolites. The synthesized zeolites were well characterized by XRD, FESEM, TEM, Raman spectroscopy, 27Al and 29Si MAS NMR, EDAX and BET surface area analyser to get more insights. We also evaluated, the catalytic activity of synthesized FER zeolites in oleic acid isomerization study to derive branched-chain fatty acids formation and attempted their structure and catalytic activity relationship with respect to purity of phases in seed.

}, keywords = {crystallization kinetics, Ferrierite seed, oleic acid isomerization, OSDA-free synthesis}, issn = {0974-3626}, doi = {10.1007/s12039-025-02387-6}, author = {Patil, Shrinidhi D. and Mohanty, Ananya and Kudalkar, Mahadev and Niphadkar, Prashant S. and Bhatte, Kushal D. and Bokade, Vijay V.} } @article {50057, title = {Direct conversion of methane to formic acid over Au-Fe-NaZSM-5 at ambient pressure using H2O2}, journal = {Catalysis Science \& Technology}, volume = {16}, year = {2026}, month = {MAR}, pages = {1797-1805}, type = {Article}, abstract = {

Direct conversion of methane to value-added products is a long-standing challenge. This report presents the one-step conversion of methane to oxygenates using H2O2 as an oxidant over an Au and Fe supported on NaZSM-5 (0.1Au0.1FeNZ) catalyst, which produces 4264 mu mol of oxygenates with 89\% selectivity toward formic acid at 10 bar and 60 degrees C within 30 min in a batch process. The catalyst also produces 26.5 mu mol of oxygenates with 70\% selectivity for formic acid at atmospheric pressure and 80 degrees C in a continuous flow process over 9 h of reaction time, making it the first report of such a process. The synergistic interaction of Au and Fe, with the crucial role of Na ions in the zeolite framework in driving the reaction, is revealed through various characterization tools like TEM, XPS, and XAS. Theoretical studies elucidate the active sites responsible for lowering the activation barrier for the crucial C-H activation step. Thus, the catalyst enables the conversion of methane into formic acid with high activity and selectivity, offering new possibilities for harnessing this potent greenhouse gas under process-friendly conditions that were previously unexplored.

}, issn = {2044-4753}, doi = {10.1039/d5cy01422k}, author = {Kumar, Pawan and Ahangar, Iqra and Kesarwani, Srishti and Urkude, Rajashri and Patil, Nita A. R. and Niphadkar, Prashant and Bokade, Vijay V. and Haider, M. Ali and Vinod, C. P.} }