A catalytic ruthenium membrane reactor (CRMR) is analyzed with regard to the methane partial oxidation reaction for synthesis gas production. The catalytic membrane consists of a commercial ceramic tube, where two different layers of ruthenium nanoparticles have been deposited on the inner surface. The metal deposition was performed by decomposition of a Ru complex under mild conditions. Different operating modes are analyzed for CRMR to establish the potentiality of the Ru catalyst deposited on the tubular ceramic support. A comparison in terms of methane conversion at various temperatures is presented. Experimental runs of CRMR containing a one-Ru-layer membrane and a two-Ru-layer membrane have also been compared
The research focus, for the development of a radial flow catalytic membrane reactor for studying met...
The external surface of a commercial porous stainless steel (PSS) was modified by either oxidation i...
Ruthenium catalysts supported on a lanthanum oxycarbonate phase (La2O2CO3) with high surface area we...
A catalytic ruthenium membrane reactor (CRMR) is analyzed with regard to the methane partial oxidati...
Partial oxidation of methane (POM) to synthesis gas was studied over Ru catalysts (1% (w/w)) support...
The methane reforming with CO2 seems to be a promising reaction system useful to reduce the greenhou...
Two consecutive model reactions of the type A->B->C are studied in two kinds of catalytic membrane r...
Two consecutive model reactions of the type A -> B -> C are studied in two kinds of catalytic membra...
Partial oxidation of methane is one of the most important chemical processes for the production of s...
This report summarizes progress made on a new method of producing synthesis gas via partial oxidatio...
Partial oxidation of methane (POM) offers a promising option to produce syngas for downstream proces...
Partial oxidation of methane is one of the most important chemical processes for the production of s...
The mechanism of the partial oxidation of methane has been investigated over a bimetallic Pt-Ru cata...
Methane steam reforming has been carried out in a Pd-Ru membrane reactor at 500-600°C. The membrane ...
Research focus, for the development of a radial flow catalytic membrane reactor for studying methane...
The research focus, for the development of a radial flow catalytic membrane reactor for studying met...
The external surface of a commercial porous stainless steel (PSS) was modified by either oxidation i...
Ruthenium catalysts supported on a lanthanum oxycarbonate phase (La2O2CO3) with high surface area we...
A catalytic ruthenium membrane reactor (CRMR) is analyzed with regard to the methane partial oxidati...
Partial oxidation of methane (POM) to synthesis gas was studied over Ru catalysts (1% (w/w)) support...
The methane reforming with CO2 seems to be a promising reaction system useful to reduce the greenhou...
Two consecutive model reactions of the type A->B->C are studied in two kinds of catalytic membrane r...
Two consecutive model reactions of the type A -> B -> C are studied in two kinds of catalytic membra...
Partial oxidation of methane is one of the most important chemical processes for the production of s...
This report summarizes progress made on a new method of producing synthesis gas via partial oxidatio...
Partial oxidation of methane (POM) offers a promising option to produce syngas for downstream proces...
Partial oxidation of methane is one of the most important chemical processes for the production of s...
The mechanism of the partial oxidation of methane has been investigated over a bimetallic Pt-Ru cata...
Methane steam reforming has been carried out in a Pd-Ru membrane reactor at 500-600°C. The membrane ...
Research focus, for the development of a radial flow catalytic membrane reactor for studying methane...
The research focus, for the development of a radial flow catalytic membrane reactor for studying met...
The external surface of a commercial porous stainless steel (PSS) was modified by either oxidation i...
Ruthenium catalysts supported on a lanthanum oxycarbonate phase (La2O2CO3) with high surface area we...