Studying complex formation of zirconium in N,N dimethylformamide ( <scp>DMF</scp> ) [ <scp>ZrO</scp> ( <scp>OH</scp> ) <sub>2</sub> .( <scp>DMF</scp> )] using <scp>DFT</scp> calculations to produce dimethyl carbonate via transesterification

Abstract The transesterification reaction, for the synthesis of dimethyl carbonate (DMC) and propylene glycol (PG) from methanol and propylene carbonate, is a new and ecologically benign alternative to conventional methods such as phosgene methanolysis, urea methanolysis, electrochemical technique, and so forth. This research focuses on the possible complex structures produced by calcining zirconium salt with N,N‐dimethylformamide (DMF) at different calcination temperatures (450, 550, 650, and 750°C) to make catalysts. The catalysts are classified as Z‐450, Z‐550, Z‐650, and Z‐750 based on their calcination temperature. The catalysts are then examined using X‐ray photoelectron spectroscopy (XPS) and Fourier transform infrared spectroscopy (FTIR) to determine the reaction process. X‐ray diffraction (XRD) examination is used to evaluate the crystallinity of the catalysts, while field emission scanning electron microscopy (FE‐SEM) is utilized to study the morphology. The CO 2 ‐TPD aids in determining basicity to investigate the active locations for interaction. The reaction takes place in a batch reactor at a constant temperature of 150–180°C and a molar ratio of 5–10 for methanol to PC. The oxygen vacancy concentrations, basicity, and structure of the catalyst created by the mixing of DMF with zirconium produce [ZrO(OH) 2 .(DMF)] as simulated by DFT calculations improved the yield and selectivity of DMC. The Z‐750 catalyst provided maximal PC conversion of 88% at 170°C with stirring speeds ranging from 600 to 650 rpm.

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Publication Details

Journal
The Canadian Journal of Chemical Engineering
Published
2025-04-24
DOI
https://doi.org/10.1002/cjce.25709
Primary Topic
Carbon dioxide utilization in catalysis
Type
article
Field-Weighted Citation Impact
0.00

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article

Studying complex formation of zirconium in N,N dimethylformamide ( DMF ) [ ZrO ( OH ) 2 .( DMF )] using DFT calculations to produce dimethyl carbonate via transesterification

Vimal Chandra Srivastava, Vimal Kumar, Surbhi Dahiya, Pankaj Kumar
The Canadian Journal of Chemical Engineering
Carbon dioxide utilization in catalysis
article

Studying complex formation of zirconium in N,N dimethylformamide ( DMF ) [ ZrO ( OH ) 2 .( DMF )] using DFT calculations to produce dimethyl carbonate via transesterification

Vimal Chandra Srivastava, Vimal Kumar, Surbhi Dahiya, Pankaj Kumar
article en

Abstract

Abstract The transesterification reaction, for the synthesis of dimethyl carbonate (DMC) and propylene glycol (PG) from methanol and propylene carbonate, is a new and ecologically benign alternative to conventional methods such as phosgene methanolysis, urea methanolysis, electrochemical technique, and so forth. This research focuses on the possible complex structures produced by calcining zirconium salt with N,N‐dimethylformamide (DMF) at different calcination temperatures (450, 550, 650, and 750°C) to make catalysts. The catalysts are classified as Z‐450, Z‐550, Z‐650, and Z‐750 based on their calcination temperature. The catalysts are then examined using X‐ray photoelectron spectroscopy (XPS) and Fourier transform infrared spectroscopy (FTIR) to determine the reaction process. X‐ray diffraction (XRD) examination is used to evaluate the crystallinity of the catalysts, while field emission scanning electron microscopy (FE‐SEM) is utilized to study the morphology. The CO 2 ‐TPD aids in determining basicity to investigate the active locations for interaction. The reaction takes place in a batch reactor at a constant temperature of 150–180°C and a molar ratio of 5–10 for methanol to PC. The oxygen vacancy concentrations, basicity, and structure of the catalyst created by the mixing of DMF with zirconium produce [ZrO(OH) 2 .(DMF)] as simulated by DFT calculations improved the yield and selectivity of DMC. The Z‐750 catalyst provided maximal PC conversion of 88% at 170°C with stirring speeds ranging from 600 to 650 rpm.

The Canadian Journal of Chemical EngineeringVol. 103(11)
Indian Institute of Technology Roorkee (IN)
Strong, Department of Science and Technology, Ministry of Science and Technology, India, Science and Engineering Research Board
Openalex Percentile: Top 94%
Carbon dioxide utilization in catalysis
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