TY - JOUR
T1 - Effect of Thermal, Acid, and Alkaline Treatments over SAPO-34 and Its Agglomerated Catalysts
T2 - Property Modification and Methanol-to-Olefin Reaction Performance
AU - Zapater, Diego
AU - Lasobras, Javier
AU - Zambrano, Naydu
AU - Hita, Idoia
AU - Castaño, Pedro
AU - Soler, Jaime
AU - Herguido, Javier
AU - Menéndez, Miguel
N1 - Publisher Copyright:
© 2024 The Authors. Published by American Chemical Society.
PY - 2024/2/28
Y1 - 2024/2/28
N2 - SAPO-34 zeolite is one of the most well-studied methanol-to-olefin catalysts, with applications from laboratory to commercial scale. Here, we have studied the impact on the properties and performance of different modifications of a commercial zeolite, including thermal, acid, and alkaline treatments, along with its agglomeration with bentonite and alumina required in the technical catalyst. We prepared three zeolites and agglomerated them, making a total of seven materials, along with our benchmark catalyst. These were characterized and tested in a packed bed reactor. We analyzed the conversion, yield, and deactivation (coke) based on the effective acid site density ρAS* (a parameter correlating acid strength, density, and micropore volume). Thermal treatment increased the effective acid site density of the commercial zeolite by 60%, while only a 10% increase was found in the parent agglomerated catalyst. Acid etching increased the effective acid site density by 80%, while the basic treatment completely amorphized the framework of the zeolite. After agglomeration, the performance of the catalysts (by means of olefin production and deactivation) correlated with effective acid site density. The catalysts based on thermally and acid-treated zeolites performed best, while they had the lowest effective acid site density.
AB - SAPO-34 zeolite is one of the most well-studied methanol-to-olefin catalysts, with applications from laboratory to commercial scale. Here, we have studied the impact on the properties and performance of different modifications of a commercial zeolite, including thermal, acid, and alkaline treatments, along with its agglomeration with bentonite and alumina required in the technical catalyst. We prepared three zeolites and agglomerated them, making a total of seven materials, along with our benchmark catalyst. These were characterized and tested in a packed bed reactor. We analyzed the conversion, yield, and deactivation (coke) based on the effective acid site density ρAS* (a parameter correlating acid strength, density, and micropore volume). Thermal treatment increased the effective acid site density of the commercial zeolite by 60%, while only a 10% increase was found in the parent agglomerated catalyst. Acid etching increased the effective acid site density by 80%, while the basic treatment completely amorphized the framework of the zeolite. After agglomeration, the performance of the catalysts (by means of olefin production and deactivation) correlated with effective acid site density. The catalysts based on thermally and acid-treated zeolites performed best, while they had the lowest effective acid site density.
UR - https://www.scopus.com/pages/publications/85182559429
U2 - 10.1021/acs.iecr.3c03956
DO - 10.1021/acs.iecr.3c03956
M3 - Article
AN - SCOPUS:85182559429
SN - 0888-5885
VL - 63
SP - 3586
EP - 3599
JO - Industrial & Engineering Chemistry Research
JF - Industrial & Engineering Chemistry Research
IS - 8
ER -