HYBRID EVENT: You can participate in person at Rome, Italy or Virtually from your home or work.
Speaker at Petroleum Engineering Conferences - Enkhsaruul Byambajav
National University of Mongolia, Mongolia
Title : Production of light hydrocarbons (C2-C4) by hydrogenation of CO2 using Co-K/?-Al2O3 catalysts with additional metal promoters (Ba, La, Ce) and combined supports (Y2O3, TiO2)

Abstract:

In this research work, we obtained C2-C4 hydrocarbons as a product of the Fischer-Tropsch synthesis (FT-CO2) by converting CO2 using Co-K/?-Al2O3 catalysts. The catalysts were enhanced with 1% Ba, La, Ce or 0.5-3% Ce promoters, respectively. Moreover, 10% Y2O3 or 10%TiO2 was added to the ?-Al2O3 support, respectively. Effect of the promoter and the support doping on CO2 conversion and C2-C4 selectivity was inverstigated in FT-CO2 synthesis.

The catalysts were prepared using the incipient wetness impregnation method, and characterized by X-ray diffraction analysis, Temperature-programmed hydrogen reduction, and CO2 desorption measurements. Catalytic activity of the catalysts was evaluated in a fixed-bed reactor at 350°C, 3 atm, and H2:CO2=3:1 molar ratio with a total volume rate of 3000 h-1.

At 350ºC, the addition of promoter metals to the catalysts increased catalyst activity. The Ce promoted Co-K/?-Al2O3 catalyst increased the C2-C4 yield by 10.67%. However, the catalyst activity decreased when the Y2O3, TiO2 was added into the ?-Al2O3 support. At 350ºC, the Co-K-1Ce/?-Al2O3 catalyst showed the highest activity in the FT-CO2 synthesis. With this catalyst, CO2 conversion, C2-C4 yield and C2-C4 hydrocarbon selectivity were reached 44.90%, 14.91%, and 37.17%, respectively. TPR results of the Co-K-1Ce/?-Al2O3 catalyst showed the creation of much active sites due to the interaction between metal and support, leading to an increase in selectivity towards light hydrocarbons. Also it was known by CO2-TPD analysis that the interaction between metal catalysts and support enhanced the CO2 activation over the Co-K-1Ce/?-Al2O3 by increasing the medium strength basic sites. Futhermore, additional supports such as Y2O3 and TiO2 increased the CO yield by the reverse-water gas shift reaction in FT-CO2 synthesis.

The addition of Ce as the promoter to the Co catalyst was found to be the most effective way for enhancing the catalytic activity, while the addition of Y2O3 and TiO2 to the ?-Al2O3 support did not show significant improvement in catalyst performance for the FT-CO2 synthesis.

Biography:

Dr. Enkhsaruul Byambajav studied at the Tohoku University, Japan and graduated her PhD course in 2004. Since then, she is teaching at the National University of Mongolia. She was promoted as a full professor the National University of Mongolia in 2020. Now she is supervising a laboratory of Clean energy technology development in the university. She has published more than 20 research articles in WoS-JCR journals.

Watsapp