@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: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.} }