4.6 Article

Catalytic Deactivation of HY Zeolites in the Dehydration of Glycerol to Acrolein

Journal

CATALYSTS
Volume 11, Issue 3, Pages -

Publisher

MDPI
DOI: 10.3390/catal11030360

Keywords

zeolite deactivation; glycerol dehydration; acrolein; HY zeolite; zeolite acidity; micro; mesoporous zeolites

Funding

  1. Universidad Autonoma Metropolitana
  2. Instituto Politecnico Nacional
  3. Instituto Mexicano del Petroleo
  4. company Sintesis y Aplicaciones Industriales S.A.

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The study found that increasing the SiO2/Al2O3 molar ratio of HY zeolites decreases the total amount of acid sites per unit area, leading to a reduced initial glycerol conversion; however, the initial acrolein selectivity increases with the higher Brønsted/Lewis acid sites ratio. The catalyst lifetime depends on pore structure, with larger surface areas improving deactivation rate constants.
The study of the deactivation of HY zeolites in the dehydration reaction of glycerol to acrolein has represented a challenge for the design of new catalysts. HY zeolites with SiO2/Al2O3 molar ratios between 3.5 and 80 were studied. The solids were characterized by XRD, N-2 physisorption, SEM-EDXS, Raman and UV-vis spectroscopies, infrared spectroscopy of pyridine (FTIR-Py) and catalytic activity tests from 250 degrees C to 325 degrees C. It was found that the total amount of acid sites per unit area of catalyst decreased as the SiO2/Al2O3 molar ratio increased from 3.5 to 80, resulting in the decrease in the initial glycerol conversion. The initial acrolein selectivity was promoted with the increase of the Bronsted/Lewis acid sites ratio at any reaction temperature. The deactivation tests showed that the catalyst lifetime depended on the pore structure, improving with the presence of large surface areas as evidenced by the deactivation rate constants. The characterization of the deactivated catalysts by XRD, N-2 physisorption and thermogravimetric analysis indicated that the deposition of coke resulted in the total obstruction of micropores and the partial blockage of mesopores. Moreover, the presence of large mesopores and surface areas allowed the amount of coke deposited at the catalyst surface to be reduced.

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