Recovery of deactivated γ-Al2O3 catalyst used in chlorination of benzene by a hybrid method: Acid washing and thermal treatment

Sh. Fallahi , M. Kord , M. Hajilari , A. Heidary Moghadam , T. Pirhoushyaran
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Abstract

This study implements a hybrid method to revive the deactivated γ-Al2O3 catalyst used in the chlorination of waste-recycled benzene in vinyl chloride production by Arvand Petrochemical Company. The method includes chemical and thermal remedies: acid washing and heating under steam. The acidity strength of two different acids, HCl and HNO3, and furnace temperature are perceived as influential variables in the reviving process in three levels of 0.5, 1, and 1.5 M, and 450, 500, and 550 °C. Characterization analyses including XRD, BET, SEM, and FTIR are employed to compare fresh, deactivated, and revived catalysts. The results suggested that HCl with a concentration of 0.5 M and a furnace temperature of 500 °C triggered the optimal conditions to recover the specific surface area. It is proven that HNO3 even in the lowest concentration could destroy the catalyst structure. On the contrary, thermal treatment was insufficient to revive the deactivated catalyst.
本研究采用了一种混合方法,以恢复 Arvand 石化公司在氯乙烯生产中使用的失活 γ-Al2O3 催化剂的活性。该方法包括化学和热补救措施:酸洗和蒸汽加热。两种不同酸(盐酸和硝酸)的酸度和炉温是再生过程中的影响变量,分别为 0.5、1 和 1.5 M,以及 450、500 和 550 °C。表征分析包括 XRD、BET、SEM 和 FTIR,用于比较新催化剂、失活催化剂和活化催化剂。结果表明,浓度为 0.5 M 的盐酸和 500 °C 的炉温是恢复比表面积的最佳条件。事实证明,即使是最低浓度的 HNO3 也会破坏催化剂结构。相反,热处理不足以恢复失活的催化剂。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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CiteScore
5.30
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