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

This study implements a hybrid method to revive the deactivated γ-Al 2 O 3 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 HNO 3 , 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 HNO 3 even in the lowest concentration could destroy the catalyst structure. On the contrary, thermal treatment was insufficient to revive the deactivated catalyst.

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Publication Details

Journal
Results in Materials
Published
2025-03-05
DOI
https://doi.org/10.1016/j.rinma.2025.100675
Primary Topic
Catalysis and Oxidation Reactions
Type
article
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article

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

Saeed Fallahi, Ali Heidary Moghadam, Tahereh Pirhoushyaran, M. Hajilari et al.
Results in Materials
Catalysis and Oxidation Reactions
article

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

Saeed Fallahi, Ali Heidary Moghadam, Tahereh Pirhoushyaran, M. Hajilari, M. Kord
article en

Abstract

This study implements a hybrid method to revive the deactivated γ-Al 2 O 3 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 HNO 3 , 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 HNO 3 even in the lowest concentration could destroy the catalyst structure. On the contrary, thermal treatment was insufficient to revive the deactivated catalyst.

Results in MaterialsVol. 26
Petroleum University of Technology (IR), Materials and Energy Research Center (IR), Islamic Azad University, Dezful Branch (IR)
Clean water and sanitation
Openalex Percentile: Top 98%
Catalysis and Oxidation Reactions
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