Role of preparation parameters of Cu-Zn mixed oxide catalyst in solvent free glycerol carbonylation with urea
Title | Role of preparation parameters of Cu-Zn mixed oxide catalyst in solvent free glycerol carbonylation with urea |
Publication Type | Journal Article |
Year of Publication | 2021 |
Authors | Charate, S, Shinde, S, Kondawar, S, Desai, U, Wadgaonkar, P, Rode, C |
Journal | Journal of the Indian Chemical Society |
Volume | 98 |
Issue | 7 |
Pagination | 100090 |
Date Published | JUL |
Type of Article | Article |
ISSN | 0019-4522 |
Keywords | Co-precipitation (CP), Glycerol, Glycerol carbonate, Oxalate gel (OG) |
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. |
DOI | 10.1016/j.jics.2021.100090 |
Type of Journal (Indian or Foreign) | Indian |
Impact Factor (IF) | 0.284 |
Divison category:
Chemical Engineering & Process Development
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