In this study, oxidative steam reforming of ethanol at low-temperature was investigated over bimetallic catalysts supported on CeO2/SiO2, having different ceria content (20-40 wt%). The activity was studied between 300 and 600°C, under a 10%C2H5OH/40%H2O/5%O2/45%N2 stream; catalyst stability was evaluated at the same feeding conditions by fixing the temperature to 500°C. The results of catalyst characterization (BET, XRD, TPR) allowed the explanation of the different catalytic performances, in terms of activity and stability. The sample containing 30wt% of ceria displayed the highest durability, assuring total ethanol conversion and a stable behavior for more than 130 h. This result was related to the low dimension of Ni crystallites, which...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
In this study, oxidative steam reforming of ethanol at low-temperature was investigated over bimetal...
In this study, oxidative steam reforming of ethanol at low-temperature was investigated over bimetal...
In this study, oxidative steam reforming of ethanol at low-temperature was investigated over bimetal...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
In this study, oxidative steam reforming of ethanol at low-temperature was investigated over bimetal...
In this study, oxidative steam reforming of ethanol at low-temperature was investigated over bimetal...
In this study, oxidative steam reforming of ethanol at low-temperature was investigated over bimetal...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
In this paper, bimetallic Pt-Ni/CeO2 catalysts supported over mesoporous silica were employed for et...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...
The development of catalysts resistant to deactivation, especially to coke formation, is a key issue...