1. Thermal dry reforming of methane over La2O3 co-supported Ni/MgAl2O4 catalyst for hydrogen-rich syngas production.
- Author
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Khoja, Asif Hussain, Anwar, Mustafa, Shakir, Sehar, Mehran, Muhammad Taqi, Mazhar, Arslan, Javed, Adeel, and Amin, Nor Aishah Saidina
- Subjects
NICKEL catalysts ,STEAM reforming ,CATALYSTS ,FIXED bed reactors ,CATALYTIC activity ,METHANE ,GREENHOUSE gases - Abstract
The excess emission of greenhouse gases (GHGs) such as CO
2 and CH4 is posing an acute threat to the environment, and efficient ways are being sought to utilize GHGs to produce syngas (H2 , CO) and lighter hydrocarbons (HCs). In this study, the dry reforming of methane (DRM) has been carried out at 700 °C using La2 O3 co-supported Ni/MgAl2 O4 nano-catalyst in a fixed bed thermal reactor. The catalyst is characterized using various techniques such as XRD, FESEM, EDX-mapping, CO2 -TPD, H2 -TPR and TGA. The modified MgAl2 O4 shows the flake type structure after the addition of La2 O3 . The TPR and TPD analysis shows the highly dispersed metal and strong basic nature of the catalyst consequently enhances the conversion of CO2 and CH4 . The highest conversion for CH4 is 87.3% while CO2 conversion is nearly 89.5% in 20 h of operation time. The selectivity of H2 and CO approached 50% making the H2 /CO ratio above unity. In the longer time-on-stream (TOS) test, the catalyst shows elevated potential for longer runs showcasing better catalytic activity. The stability of the catalyst is indicated via a proposed reaction mechanism for DRM in operating conditions. Moreover, TGA indicates the lower weight loss of spent catalyst which ascribed the lower formation of carbon during TOS 20 h. [ABSTRACT FROM AUTHOR]- Published
- 2020
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