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Impacts of Sn(II) doping on the Keggin heteropolyacid-catalyzed etherification of glycerol with tert-butyl alcohol.

Authors :
da Silva, Márcio José
Chaves, Diego Morais
ferreira, Sukarno Olavo
da Silva, Rene Chagas
Gabriel Filho, Jose Balena
Bruziquesi, Carlos Giovani Oliveira
Al-Rabiah, Abdulrahman A.
Source :
Chemical Engineering Science. Jan2022, Vol. 247, pN.PAG-N.PAG. 1p.
Publication Year :
2022

Abstract

[Display omitted] • H 3-x Sn x/2 PMo 12 O 40 -catalyzed glycerol etherification was assessed (x = 0.0, 1.0, 2.0, 3.0). • Analyses of TG/DSC, EDS/MEV, BET, DRX characterized Sn(II) heteropoly salts. • NH 3 -TPD and adsorbed pyridine FT-IR showed bifunctional Sn 3/2 PMo 12 O 40 catalyst. • Annual capacity of 30,000 ton3 with a return on investment (ROI) of 30.7%. In this work, phosphomolybdic acid salts were synthesized exchanging their protons by the Sn(II) cations (i.e., H 3-x Sn x/2 PMo 12 O 40 ; x = 0.0, 1.0, 2.0, 3.0), and evaluated in the etherification reactions of glycerol with tert-butyl alcohol (TBA). The catalytic activity of the phosphomolybdate salts containing a variable load of Sn(II) ions was further compared to phosphotungstic and silicotungstic acid salts (i.e., H 3-x Sn x/2 PW 12 O 40 ; x = 0.0, 1.0, 2.0, 3.0 and H 4-x Sn x/2 PW 12 O 40 ; x = 0.0, 1.0, 2.0, 4.0, respectively). The integrity of the Keggin anion after the synthesis was confirmed by infrared spectroscopy analysis. Physical properties were determined through thermal analyses, powder X-Rays diffraction patterns, N 2 adsorption-desorption isotherms, and scanning electron microscopy. The acidity properties were analyzed by adsorbed pyridine FT-IR spectroscopy, NH 3 -programmed-temperature desorption, and potentiometric titration. Among all the Sn(II) heteropoly salts tested, the Sn 3 PMo 12 O 40 was the most active and selective catalyst toward glyceryl ethers. The highest activity of Sn 3 PMo 12 O 40 was assigned to the greater Lewis acidity strength. Modeling, simulation, and economic analysis allowed to evaluate the viability of the process. An annual capacity of 30,000 metric tons was developed, and the process is feasible with a return on investment (ROI) of 30.7%. [ABSTRACT FROM AUTHOR]

Details

Language :
English
ISSN :
00092509
Volume :
247
Database :
Academic Search Index
Journal :
Chemical Engineering Science
Publication Type :
Academic Journal
Accession number :
152977962
Full Text :
https://doi.org/10.1016/j.ces.2021.116913