Catalytic cracking of C5 raffinate to light olefins over NaOH-treated ZSM-5

Catalytic cracking of C5 raffinate to light olefins over NaOH-treated ZSM-5 A series of ZSM-5 catalysts (ZSM-5 (X)) treated with different NaOH concentration (X = 0, 0.05, 0.1, and 0.2 M) were prepared for use in the production of light olefins (ethylene and propylene) through catalytic cracking of C5 raffinate. The effect of NaOH concentration on their physicochemical properties and catalytic activity was investigated. It was found that textural and physicochemical properties of ZSM-5 (X) catalysts were strongly influenced by the NaOH concentration. Mesopore volume of ZSM-5 (X) catalysts increased with increasing NaOH concentration, while acidity of the catalysts decreased with increasing NaOH concentration. Conversion of C5 raffinate and yield for light olefins (ethylene and propylene) showed the volcano-shaped curves with respect to NaOH concentration (X). This implies that NaOH treatment of ZSM-5 was an efficient method to produce light olefins through catalytic cracking C5 raffinate, and that optimal NaOH concentration was required for maximum production of light olefins. Among the catalysts tested, ZSM-5 (0.05) catalyst showed the best catalytic performance due to its favorable porosity and acidity. Research on Chemical Intermediates Springer Journals

Catalytic cracking of C5 raffinate to light olefins over NaOH-treated ZSM-5

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Springer Netherlands
Copyright © 2011 by Springer Science+Business Media B.V.
Chemistry; Physical Chemistry; Inorganic Chemistry; Catalysis
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