Effect of the catalyst in the BTX production by hydrocracking of light cycle oil

• Published in: Applied petrochemical research Vol. 11; no. 1; pp. 19 - 38
• Main Authors: Laredo, Georgina C., García-Gutiérrez, José L., Pérez-Romo, Patricia, Olmos-Cerda, Eli H.
• Format: Journal Article
• Language: English
• Published: Cham Springer International Publishing 01.05.2021; Springer; Springer Nature B.V
• Subjects: Alkylbenzenes; Analysis; Benzene; Catalysis; Catalysts; Chemistry; Chemistry and Materials Science; Energy Systems; Gas formation; Hydrocracking; Industrial Chemistry/Chemical Engineering; Methods; Nanochemistry; Nanotechnology and Microengineering; Naphthalene; Petrochemicals; Refineries; Review; Toluene; Xylene; Yield; Zeolites; Mexico; Light cycle oil; Hydrocracking; Hydrogenation; BTX
• ISSN: 2190-5525; 2190-5525; 2190-5533
• DOI: 10.1007/s13203-021-00266-y

Catalysts to produce the important petrochemicals like benzene, toluene, and xylene (BTX) from refinery feedstocks, like light cycle oil (LCO) are reviewed here by covering published papers using model mixtures and real feeds. Model compounds experiments like tetralin and naphthalene derivatives provided a 53–55% total BTX yield. Higher yields were never attained due to the inevitable gas formation and other C 9+ -alkylbenzenes formed. For tetralin, the best catalysts are those conformed by Ni, CoMo, NiMo, or NiSn over zeolite H-Beta. For naphthalene derivatives, the best catalysts were those conformed by W and NiW over zeolite H-Beta silylated. Real feeds produced a total BTX yield of up to 35% at the best experimental conditions. Higher yields were never reached due to the presence of other types of hydrocarbons in the feed which can compete for the catalytic sites. The best catalysts were those conformed by Mo, CoMo, or NiMo over zeolite H-Beta. Some improvements were obtained by adding ZSM-5 to the support or in mixtures with other catalysts.