Catalytic dehydrogenation coupling of methane (DCM) represents an effective way to convert natural gas to more useful C2 products (C2H6, C2H4). In this work, BaCe0.85Tb0.05Co0.1O3-δ (BCTCo) perovskite hollow fiber membranes were fabricated by the combined phase inversion and sintering method. SrCe0.95Yb0.05O3-δ (SCYb) perovskite oxide was loaded as a catalyst onto the inner hollow fiber membrane surface, which promoted the CH4 conversion and the C2 hydrocarbon selectivity during the DCM reaction. The introduction of steam into the methane feed gas mixture elevated the C2 selectivity and yield due to the alleviation of coke deposition. Switching N2 to air as the sweep gas further increased the C2 selectivity and yield. However, the conversio...
The equilibrium limitations of water splitting and the coupling of methane to C-2 hydrocarbons (etha...
Two consecutive model reactions of the type A -> B -> C are studied in two kinds of catalytic membra...
The equilibrium limitations of water splitting and the coupling of methane to C-2 hydrocarbons (etha...
Using the prepared La0.6Sr0.4Co0.2Fe0.8O3 (LSCF) hollow fibre membranes via the phase inversion and ...
The performance of a dense ceramic hydrogen-permeable membrane reactor for the nonoxidative methane ...
The performance of a dense ceramic hydrogen-permeable membrane reactor for the nonoxidative methane ...
In this study, a micro-structured catalytic hollow fiber membrane reactor (CHFMR) has been prepared,...
Gas-tight La0.7Sr0.3FeO3−α (LSF) perovskite hollow fiber membranes were fabricated by the phase inve...
Oxygen permeable ceramic membranes have potential applications as the high temperature membrane reac...
Perovskite membranes have the potentials to be applied in a novel cost-effective technology for air ...
Partial funding for Open Access provided by the UMD Libraries' Open Access Publishing Fund.Understan...
Two consecutive model reactions of the type A->B->C are studied in two kinds of catalytic membrane r...
Research focus, for the development of a radial flow catalytic membrane reactor for studying methane...
A catalytic hollow fibre membrane reactor (CHFMR) was developed in this study for combined steam met...
Pre-combustion decarbonisation is one of the three main routes widely discussed for CO2 capture from...
The equilibrium limitations of water splitting and the coupling of methane to C-2 hydrocarbons (etha...
Two consecutive model reactions of the type A -> B -> C are studied in two kinds of catalytic membra...
The equilibrium limitations of water splitting and the coupling of methane to C-2 hydrocarbons (etha...
Using the prepared La0.6Sr0.4Co0.2Fe0.8O3 (LSCF) hollow fibre membranes via the phase inversion and ...
The performance of a dense ceramic hydrogen-permeable membrane reactor for the nonoxidative methane ...
The performance of a dense ceramic hydrogen-permeable membrane reactor for the nonoxidative methane ...
In this study, a micro-structured catalytic hollow fiber membrane reactor (CHFMR) has been prepared,...
Gas-tight La0.7Sr0.3FeO3−α (LSF) perovskite hollow fiber membranes were fabricated by the phase inve...
Oxygen permeable ceramic membranes have potential applications as the high temperature membrane reac...
Perovskite membranes have the potentials to be applied in a novel cost-effective technology for air ...
Partial funding for Open Access provided by the UMD Libraries' Open Access Publishing Fund.Understan...
Two consecutive model reactions of the type A->B->C are studied in two kinds of catalytic membrane r...
Research focus, for the development of a radial flow catalytic membrane reactor for studying methane...
A catalytic hollow fibre membrane reactor (CHFMR) was developed in this study for combined steam met...
Pre-combustion decarbonisation is one of the three main routes widely discussed for CO2 capture from...
The equilibrium limitations of water splitting and the coupling of methane to C-2 hydrocarbons (etha...
Two consecutive model reactions of the type A -> B -> C are studied in two kinds of catalytic membra...
The equilibrium limitations of water splitting and the coupling of methane to C-2 hydrocarbons (etha...