Dry reforming experiments are performed for five different CH4/CO2 ratios at three different operating temperatures. The focus of the work is on the short-term catalyst deactivation due to carbon deposition and analysis of the nature and structure of deposited carbon at CH4/CO2 ratio of 2, which is typical for biogas. The dry reforming experiments indicate that the short-term deactivation is insignificant at an equimolar ratio of CH4 and CO2. The rate of carbon deposition becomes faster at higher CH4/CO2 ratios and higher temperatures. CH4 and CO2 conversions and the exit mole fraction of CO and H2 confirm the occurrence of the reverse water–gas shift reaction. Characterization of the spent catalyst and deposited carbon is performed using X...
The dry and oxidative dry reforming of CH4 over alumina-supported CoeNi catalysts were investigated ...
The dry reforming of biogas on a Ni catalyst supported on three commercially available materials (Zr...
Highly stable Ni catalysts with varying Ni contents up to 50 mol% originating from hydrotalcite-like...
The dry reforming of biogas on a Ni catalyst supported on three commercially available materials (Zr...
The dry reforming of biogas on a Ni catalyst supported on three commercially available materials (Zr...
This paper presents a detailed study of catalyst deactivation as a result of simultaneous sulfur poi...
This paper presents a detailed study of catalyst deactivation as a result of simultaneous sulfur poi...
Summarization: The dry reforming of biogas on a Ni catalyst supported on three commercially availabl...
This article belongs to the Special Issue Catalyst Deactivation in Hydrocarbon Processing.The tackli...
Ni/Al2O3 and Ni/CaO-MgO-Al2O3 catalysts were investigated for the biogas dry reforming reaction usin...
5 pags, 6 figures, 2 tablesA conceptually similar approach to dry reforming of CH4 (DRM) called Cata...
Ni/Al2O3 and Ni/La2O-Al2O3 catalysts were investigated for the biogas reforming reaction using CH4/C...
The tackling of carbon deposition during the dry reforming of biogas (BDR) necessitates research of ...
A La-NiMgAlO catalyst, obtained after calcination of a hydrotalcite precursor, was evaluated in dry ...
A La-NiMgAlO catalyst, obtained after calcination of a hydrotalcite precursor, was evaluated in dry ...
The dry and oxidative dry reforming of CH4 over alumina-supported CoeNi catalysts were investigated ...
The dry reforming of biogas on a Ni catalyst supported on three commercially available materials (Zr...
Highly stable Ni catalysts with varying Ni contents up to 50 mol% originating from hydrotalcite-like...
The dry reforming of biogas on a Ni catalyst supported on three commercially available materials (Zr...
The dry reforming of biogas on a Ni catalyst supported on three commercially available materials (Zr...
This paper presents a detailed study of catalyst deactivation as a result of simultaneous sulfur poi...
This paper presents a detailed study of catalyst deactivation as a result of simultaneous sulfur poi...
Summarization: The dry reforming of biogas on a Ni catalyst supported on three commercially availabl...
This article belongs to the Special Issue Catalyst Deactivation in Hydrocarbon Processing.The tackli...
Ni/Al2O3 and Ni/CaO-MgO-Al2O3 catalysts were investigated for the biogas dry reforming reaction usin...
5 pags, 6 figures, 2 tablesA conceptually similar approach to dry reforming of CH4 (DRM) called Cata...
Ni/Al2O3 and Ni/La2O-Al2O3 catalysts were investigated for the biogas reforming reaction using CH4/C...
The tackling of carbon deposition during the dry reforming of biogas (BDR) necessitates research of ...
A La-NiMgAlO catalyst, obtained after calcination of a hydrotalcite precursor, was evaluated in dry ...
A La-NiMgAlO catalyst, obtained after calcination of a hydrotalcite precursor, was evaluated in dry ...
The dry and oxidative dry reforming of CH4 over alumina-supported CoeNi catalysts were investigated ...
The dry reforming of biogas on a Ni catalyst supported on three commercially available materials (Zr...
Highly stable Ni catalysts with varying Ni contents up to 50 mol% originating from hydrotalcite-like...