بررسی اثر شرایط خشک‌کردن بر خواص ساختاری و عملکرد کاتالیستی کاتالیزور Fe-Co-Ni/MgO در تولید اولفین‌های سبک از گاز سنتز

نوع مقاله : مقاله پژوهشی

نویسندگان
1 استادیار، گروه آموزش شیمی، دانشگاه فرهنگیان، صندوق پستی ۸۸۹-۱۴۶۶۵، تهران، ایران
2 استادیار، گروه مهندسی شیمی، دانشکده مهندسی، دانشگاه سیستان و بلوچستان، زاهدان، ایران
چکیده
در این پژوهش، کاتالیزورهای Fe-Co-Ni تهیه‌شده به روش هم‌رسوبی برای سنتز اولفین‌های سبک از طریق فرایند فیشر–تروپش مورد بررسی قرار گرفتند. تأثیر دما و زمان خشک کردن پیش‌سازهای کاتالیزور بر عملکرد نمونه Fe-Co-Ni ساپورت‌شده با MgO در یک میکرو راکتور بستر ثابت و تحت شرایط عملیاتی ثابت (GHSV=۵۴۰۰ h⁻¹، نسبت H₂/CO=۱/۳، فشار ۱ بار، دما ۳۰۰ درجه سانتی‌گراد) ارزیابی شد. نتایج نشان داد که خشک‌کردن در دمای ۱۲۰ درجه سانتی‌گراد به مدت ۱۶ ساعت عملکرد بهینه‌ای در هیدروژناسیون CO دارد. تأثیر خشک کردن بر رفتار احیا و سطح ویژه کاتالیست نیز به ترتیب با روش‌های TPR و BET مورد بررسی قرار گرفت. تحلیل آماری ANOVA نشان داد که هم دمای خشک کردن و هم زمان خشک کردن به طور معناداری موجب افزایش سطح ویژه کاتالیست می‌شوند، اما تنها زمان خشک کردن بر کاهش گزینش‌پذیری تولید اتان موثر است. در نهایت دمای ۱۵۶/۵ درجه سانتی‌گراد و زمان ۱۸/۶۲ ساعت به عنوان شرایط بهینه تعیین شد.

کلیدواژه‌ها

موضوعات


عنوان مقاله English

Investigation of the Effect of Drying Conditions on the Structural Properties and Catalytic Performance of Fe-Co-Ni/MgO Catalyst for Light Olefins Production from Syngas

نویسندگان English

Samaneh Vahid 1
Vajiheh yousefi 2
1 Assistant Professor, Department of Chemistry Education, Farhangian University, P.O. Box 14665-889, Tehran, Iran
2 Assistant Professor, Department of Chemical Engineering, Faculty of Engineering, University of Sistan and Baluchestan, Zahedan, Iran
چکیده English

This study investigates Fe-Co-Ni catalysts prepared by co-precipitation for light olefin production via Fischer-Tropsch synthesis. The effects of drying temperature and time on MgO-supported Fe-Co-Ni catalyst performance were examined in a fixed-bed microreactor under constant conditions (GHSV = 5400 h-1, H2/CO = 1:3, pressure = 1 bar, temperature = 300°C). Drying at 120°C for 16 hours resulted in the highest catalytic activity for CO hydrogenation. Reduction behavior and surface area changes due to drying were analyzed by TPR and BET techniques, respectively. ANOVA analysis showed that both drying temperature and time significantly increased catalyst surface area (P < 0.05). However, only drying time significantly affected ethane selectivity, decreasing it with longer drying periods, while temperature had no significant impact. Optimal drying conditions were predicted at 156.5°C and 18.62 hours.

کلیدواژه‌ها English

Fe-Co-Ni catalyst
Fischer-Tropsch synthesis
Drying conditions
Carbon monoxide hydrogenation
Statistical analysis
ANOVA
  1. Chen, G., et al., Alumina-Supported CoFe Alloy Catalysts Derived from Layered-Double-Hydroxide Nanosheets for Efficient Photothermal CO2 Hydrogenation to Hydrocarbons. Advanced Materials, 2018. 30(3): p. 1704663.
  2. Zhao, Z., et al., A review of Co/Co2C-based catalysts in Fischer–Tropsch synthesis: from fundamental understanding to industrial applications. Chemical Communications, 2023. 59(26): p. 3827–3837.
  3. Jahangiri, H., et al., A review of advanced catalyst development for Fischer–Tropsch synthesis of hydrocarbons from biomass derived syn-gas. Catalysis Science & Technology, 2014. 4(8): p. 2210–2229.
  4. Sun, Y., et al., Optimization using response surface methodology and kinetic study of Fischer–Tropsch synthesis using SiO2 supported bimetallic Co–Ni catalyst. Journal of Natural Gas Science and Engineering, 2016. 28: p. 173–183.
  5. Gill, S.S., et al., Combustion characteristics and emissions of Fischer–Tropsch diesel fuels in IC engines. Progress in Energy and Combustion Science, 2011. 37(4): p. 503–523.
  6. Zhang, J.p., et al., Preparation of steam activated carbon from black liquor by flue gas precipitation and its performance in hydrogen sulfide removal: Experimental and simulation works. Journal of the Taiwan Institute of Chemical Engineers, 2016. 59: p. 395–404.
  7. Liu, Q.-Y., C. Shang, and Z.-P. Liu, In Situ Active Site for Fe-Catalyzed Fischer–Tropsch Synthesis: Recent Progress and Future Challenges. The Journal of Physical Chemistry Letters, 2022. 13(15): p. 3342–3352.
  8. Amin, M., et al., Issues and challenges of Fischer–Tropsch synthesis catalysts. Frontiers in Chemistry, 2024. Volume 12 - 2024.
  9. Torres Galvis, H.M., et al., Effects of sodium and sulfur on catalytic performance of supported iron catalysts for the Fischer–Tropsch synthesis of lower olefins. Journal of Catalysis, 2013. 303: p. 22–30.
  10. Liu, Y., et al., Strategic assembly of active phases on Co-Fe bimetallic catalysts for efficient Fischer-Tropsch synthesis. Chemical Engineering Journal, 2024. 494: p. 152936.
  11. Sonal, et al., Synergistic Effect of Fe–Co Bimetallic Catalyst on FTS and WGS Activity in the Fischer–Tropsch Process: A Kinetic Study. Industrial & Engineering Chemistry Research, 2017. 56(16): p. 4659–4671.
  12. Amin, M., et al., The Conversion of Waste Biomass into Carbon-Supported Iron Catalyst for Syngas to Clean Liquid Fuel Production. Catalysts, 2022. 12(10): p. 1234.
  13. Li, Y., et al., Effect of Support on Catalytic Performance of Photothermal Fischer-Tropsch Synthesis to Produce Lower Olefins over Fe5C2-based Catalysts. Chemical Research in Chinese Universities, 2020. 36(6): p. 1006–1012.
  14. Wang, P., et al., Efficient conversion of syngas to linear α-olefins by phase-pure χ-Fe5C2. Nature, 2024. 635: p. 102–107.
  15. Scarfiello, C., et al., Oxide Supported Cobalt Catalysts for CO2 Hydrogenation to Hydrocarbons: Recent Progress. Advanced Materials Interfaces, 2023. 10(15): p. 2202516.
  16. Gupta, S., et al., A review of cobalt-based catalysts for sustainable energy and environmental applications. Applied Catalysis A: General, 2023. 661: p. 119254.
  17. Usman, M., A.G. Fareed, and M. Amin, A bibliometric analysis of CO2 methanation: research trends and comprehension of effective catalysts. Journal of the Iranian Chemical Society, 2024. 21(5): p. 1185–1201.
  18. Yousefi, V. and H.-R. Kariminia, Statistical analysis for enzymatic decolorization of acid orange 7 by Coprinus cinereus peroxidase. International Biodeterioration & Biodegradation, 2010. 64(3): p. 245–252.
  19. Yousefi, V. and H.-R. Kariminia, The optimization of reactive black 5 dye removal using Coprinus cinereus peroxidase (CIP). Advances in Environmental Technology, 2024. 10(2): p. 85–101.
  20. Yousefi, V., Statistical investigation of pivotal physical and chemical factors on the performance of ceramic-based microbial fuel cells. Energy Harvesting and Systems, 2022. 9(2): p. 239–252.
  21. Keshavarz, M., D. Mohebbi-Kalhori, and V. Yousefi, Multi-Response Optimization of Tubular Microbial Fuel Cells Using Response Surface Methodology (RSM). Journal of Renewable Energy and Environment, 2022. 9(2): p. 49–58.
  22. Mirzaei, A.A., S. Vahid, and H.O. Torshizi, Effect of support and promoter on the catalytic performance and structural properties of the Fe–Co–Ni catalysts for CO hydrogenation. Journal of Natural Gas Science and Engineering, 2013. 15: p. 106–117.
  23. Wan, H.-j., et al., Effects of SiO2 and Al2O3 on performances of iron-basedcatalysts for slurry Fischer–Tropsch synthesis. Journal of Fuel Chemistry and Technology, 2007. 35(5): p. 589–594.
  24. Xue, L., et al., Catalytic decomposition of N2O over CeO2 promoted Co3O4 spinel catalyst. Applied Catalysis B: Environmental, 2007. 75(3): p. 167–174.
  25. Lin, H.-Y. and Y.-W. Chen, The mechanism of reduction of cobalt by hydrogen. Materials Chemistry and Physics, 2004. 85(1): p. 171–175.
  26. González-Cortés, S.L., et al., Synthesis of light alkenes on manganese promoted iron and iron-cobalt Fischer-Tropsch catalysts. Reaction Kinetics and Catalysis Letters, 2002. 75(1): p. 3–12.
  27. Hu, C.-W., et al., On the Inhomogeneity of Low Nickel Loading Methanation Catalyst. Journal of Catalysis, 1997. 166(1): p. 1–7.
  28. Chen, R., et al., Effect of Alumina Particle Size on Ni/Al2O3 Catalysts for p-Nitrophenol Hydrogenation* *Supported by the Special Funds for Major State Basic Research Program of China (No.2003CB615702), the National Natural Science Foundation of China (No.20636020) and the Natural Science Foundation of Jiangsu Province (No.BK2006722). Chinese Journal of Chemical Engineering, 2007. 15(6): p. 884–888.

  • تاریخ دریافت 11 خرداد 1404
  • تاریخ بازنگری 12 مرداد 1404
  • تاریخ پذیرش 13 شهریور 1404