@article { ISI:000309382100040, title = {Synthesis of glycidol from glycerol and dimethyl carbonate using ionic liquid as a catalyst}, journal = {Catalysis Communications}, volume = {27}, year = {2012}, month = {OCT}, pages = {184-188}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Transesterification of dimethyl carbonate with glycerol has been investigated using various ionic liquids as catalysts. Synthesis of glycidol with high selectivity (78\%) has been achieved using tetramethylammonium hydroxide ([TMA][OH]) as a catalyst at 80 degrees C. Effect of various reaction conditions on the activity and selectivity was investigated and catalyst concentration had a significant influence on conversion as well as selectivity to glycidol. Activity as well as selectivity of the catalyst decreased significantly with increase in moisture content. Recycle experiment indicated slight drop in glycerol conversion and selectivity to glycidol because of dilution of reaction mixture and also the presence of products from the initial experiment. (C) 2012 Elsevier B.V. All rights reserved.

}, keywords = {Glycerol carbonate, Glycidol, Ionic liquid, Transesterification of glycerol}, issn = {1566-7367}, doi = {10.1016/j.catcom.2012.07.003}, author = {Gade, Swapna M. and Munshi, Mudassir K. and Chherawalla, Batul M. and Rane, Vilas H. and Kelkar, Ashutosh A.} } @article { ISI:000338486300020, title = {1,8-Diazabicyclo[5.4.0]undec-7-ene (DBU): a highly efficient catalyst in glycerol carbonate synthesis}, journal = {Journal of Molecular Catalysis A-Chemical}, volume = {391}, year = {2014}, month = {SEP}, pages = {144-149}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Transesterification of dimethyl carbonate (DMC) with glycerol (GLY) was investigated using various amines as catalysts. Amidines like 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU) and 1,5-diazabicyclo[4.3.0]non-5-ene (DBN) were found to be the best catalysts for this reaction. Best results: 98\% conversion of GLY with 96\% selectivity to GC (TON: 9408), were obtained with DBU as a catalyst. Effect of various reaction conditions on activity and selectivity were investigated using DBU as catalyst. The mechanism of the reaction was investigated with the help of H-1, C-13 and N-15 NMR analysis and OFT calculations. (C) 2014 Elsevier B.V. All rights reserved.

}, keywords = {DBU, Glycerol, Glycerol carbonate, transesterification}, issn = {1381-1169}, doi = {10.1016/j.molcata.2014.04.016}, author = {Munshi, Mudassir K. and Gade, Swapna M. and Mane, Manoj V. and Mishra, Deepti and Pal, Sourav and Vanka, Kumar and Rane, Vilas H. and Kelkar, Ashutosh A.} } @article {43921, title = {Carbonylation of glycerol with urea to glycerol carbonate over supported Zn catalysts}, journal = {Applied Petrochemical Research}, volume = {7}, year = {2017}, month = {APR}, chapter = {41-53}, abstract = {

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

}, keywords = {Acid{\textendash}base ratio, Continuous process, Glycerol carbonate, Glycerol-urea carbonylation, reaction pathway, Supported Zn, Zn loading}, issn = {2190-5533}, doi = {10.1007/s13203-017-0177-2}, author = {Kondawar, S. E. and Mane, R. B. and Vasishta, A. and More, S. B. and Dhengale, S. D. and Rode, C. V.} } @article {47641, title = {Role of preparation parameters of Cu-Zn mixed oxide catalyst in solvent free glycerol carbonylation with urea}, journal = {Journal of the Indian Chemical Society}, volume = {98}, year = {2021}, month = {JUL}, pages = {100090}, type = {Article}, abstract = {Solvent-free carbonylation of glycerol with urea to glycerol carbonate (GC) was achieved over heterogeneous Cu-Zn mixed oxide catalyst. Cu-Zn catalysts with different ratios of Cu:Zn were prepared using co-precipitation (CP) and oxalate gel (OG) methods. As compared to CuO-ZnO(2:1) catalyst prepared by oxalate gel (OG) method, much higher conversion of glycerol and highest selectivity towards glycerol carbonate (GC) was achieved with CuO-ZnO_CP(2:1) catalyst. Physicochemical properties of prepared catalysts were investigated by using XRD, FT-IR, BET, TPD of CO2 and NH3 and TEM techniques. The effect of stoichiometric ratio of Cu/Zn, calcination temperature of CuO-ZnO catalysts and effect of reaction parameters such as molar ratio of substrates, time and temperature on glycerol conversion to GC were critically studied. Cu/Zn of 2:1 ratio, glycerol-urea 1:1 molar ratio, 145 degrees C reaction temperatures were found to be optimized reaction conditions to achieve highest glycerol conversion of 86\% and complete selectivity towards GC. The continuous expel of NH 3 from reaction the mixture avoided formation of ammonia complex with CuO-ZnO catalyst. As a result of this, CuO-ZnO catalyst could be recycled up to three times without losing its initial activity.}, keywords = {Co-precipitation (CP), Glycerol, Glycerol carbonate, Oxalate gel (OG)}, issn = {0019-4522}, doi = {10.1016/j.jics.2021.100090}, author = {Charate, Shrinivas and Shinde, Suhas and Kondawar, Sharda and Desai, Uday and Wadgaonkar, Prakash and Rode, Chandrashekhar} } @article {48072, title = {Perception of glycerol carbonate as green chemical: synthesis and applications}, journal = {Catalysis Communications}, volume = {172}, year = {2022}, month = {DEC}, pages = {106542}, type = {Article}, abstract = {

Glycerol carbonate (GC) is a prominent component in industrial practice and has a remarkable potential for the sophisticated applications. While GC has come into prominence due to the perceived overflow of glycerol (GLY) as a coproduct of biodiesel industry, its contemporary and future downstream applications are driving tremendous interest in recent years. This review comprises strategies for glycerol carbonate synthesis, properties and its applications. The conversion of GLY to GC via transesterification has appeared in consensus to be the most promising route. A detailed explanation of the effect of the catalysts and operating conditions on the GC yield to provide an updated understanding of the process are summarized. Future directions for GC production through catalytic transesterification are also discussed.

}, keywords = {Biodiesel, biofuels, catalysis, Glycerol, Glycerol carbonate, green chemistry, transesterification}, issn = {1566-7367}, doi = {10.1016/j.catcom.2022.106542}, author = {Gade, Swapna M. and Saptal, Vitthal B. and Bhanage, Bhalchandra M.} }