Selective conversion of methane to C2 hydrocarbons using carbon dioxide as an oxidant over CaO-MnO/CeO2 catalyst - Diponegoro University | Institutional Repository (UNDIP-IR)
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Moreover, the effect of GHSV on the activity of 3%W-H 2 SO 4 /HZSM-5 catalysts with different Si/Al ratios indicates that the maximum activity appears on the catalyst with Si/Al
It can be concluded that the hybrid catalytic DBD plasma reactor is potential for co-generation of synthesis gas and higher hy- drocarbons from methane and carbon dioxide and
• The oxidation of methane to methanol is limited by catalyst reactivation • Oxidative dehydrogenation of light alkanes is limited by both primary. deep oxidation of the alkane
This article also focus on the effect of some reaction parameters, such as the amount of oxidant, presence of steam and reaction temperature on the catalyst activity
Kinetic of solventless palmitic acid deoxygenation over nickel functionalized mesostructured cellular foam catalyst (NiMCF) to selectively synthesize n -pentadecane and
Althoughthecommercializationandtechnologicaldevel- opment of this process has been considerable, kinetic modeling ofthis complex reaction networkwith heteroge- neous
high specific surface area, highly active site, dispersion, appropriate acid/basic sites distribution and smaller particle size in order to increase the activity and selectivity to
Other than the most important C–H bond activation step the whole catalytic cycle was explored and different reaction paths were identied for the formation of the active site and the
