Effect of La and Ce on the catalytic performance of ZSM-۵ with the optimal Si/Al ratio in the HTO process
Publish Year: 1402
نوع سند: مقاله ژورنالی
زبان: English
View: 17
This Paper With 9 Page And PDF Format Ready To Download
- Certificate
- من نویسنده این مقاله هستم
استخراج به نرم افزارهای پژوهشی:
شناسه ملی سند علمی:
JR_JPSTR-13-3_005
تاریخ نمایه سازی: 9 اردیبهشت 1403
Abstract:
This study investigates, the performance of ZSM-۵ zeolite catalysts with different Si/Al ratios equal to ۴۰, ۱۲۰, and ۲۰۰ in the n-hexane catalytic cracking process in a fixed bed microreactor at ۵۵۰°C under atmospheric pressure with a WHSV = ۴ h-۱. To improve the acidity of the catalysts and increase the yield of light olefins, the best catalyst among the three synthesized catalysts was modified by lanthanum and cerium metals. These two rare earth metals were chosen as modifiers since they were expected to improve the acidic properties of the parent catalyst. Furthermore, XRD, FT-IR, FESEM, EDX Dot-Mapping, BET, and NH۳-TPD analyses were used to evaluate and characterize the synthesized catalysts. According to the results, the Z-La catalyst has significantly improved catalytic performance, such as the yield of light olefins, P/E ratio, and a decrease in the production of light alkanes and aromatic compounds compared to other catalysts. The yield of light olefins obtained from it was equal to ۶۲.۹۱%, and the P/E ratio was equal to ۳.۲۵. This significant progress in this catalyst compared to other catalysts in this research is due to adding La to H–ZSM-۵ zeolite, which causes changes and modifies the acidity properties of this catalyst (S/W ratio of acidity = ۰.۵۴).
Keywords:
Authors
Maryam Ghazimoradi
Department of Chemistry, Shahid Beheshti University, Tehran, Iran
Saeed Soltanali
Catalysis Technologies Development Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran
Nasser Safari
Department of Chemistry, Shahid Beheshti University, Tehran, Iran
Hamid Kiarad
Catalysis Technologies Development Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran
Hamid Karami
Catalysis Technologies Development Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran
مراجع و منابع این Paper:
لیست زیر مراجع و منابع استفاده شده در این Paper را نمایش می دهد. این مراجع به صورت کاملا ماشینی و بر اساس هوش مصنوعی استخراج شده اند و لذا ممکن است دارای اشکالاتی باشند که به مرور زمان دقت استخراج این محتوا افزایش می یابد. مراجعی که مقالات مربوط به آنها در سیویلیکا نمایه شده و پیدا شده اند، به خود Paper لینک شده اند :