Zobrazeno 1 - 10
of 47
pro vyhledávání: '"O.V. Buyevskaya"'
Autor:
M. Baerns, O.V. Buyevskaya
Publikováno v:
Catalysis from A to Z.
Autor:
M. Baerns, O.V. Buyevskaya
Publikováno v:
Catalysis from A to Z.
Autor:
O.V. Buyevskaya, M. Baerns
Publikováno v:
Catalysis from A to Z.
Publikováno v:
Applied Catalysis A: General. 226:73-78
Studies on the catalytic and non-catalytic oxidative dehydrogenation of ethane (ODE) to ethylene have been carried out between 600 and 800 °C in the presence of 30% of steam in the feed and in its absence at a contact time of 0.2 g s ml −1 and at
Publikováno v:
Chemical Engineering Journal. 82:3-11
Low-temperature catalysts for the total combustion of low-concentration propane in air have been searched for applying a combinatorial approach including an optimization procedure based on a genetic algorithm. A 1st generation of catalysts was prepar
Publikováno v:
Journal of Catalysis. 197:43-48
The behavior of SrxLa1.0Nd1.0Oy catalysts with different Sr loadings (x=0, 0.001, 0.01, 0.1, and 1.0) was examined regarding their application as ignitors for the autothermal oxidative dehydrogenation of ethane. Ethylene yields as high as 42% (S>69%)
Publikováno v:
Topics in Catalysis. 15:175-180
The study is based on the previous development of α-Al2O3-supported multi-metal-oxide materials for oxidative dehydrogenation of propane by applying a combinatorial approach (773 K, ambient pressure, a feed composition of C3H8 : O2 : N2=30 : 10 : 60
Publikováno v:
Journal of Molecular Catalysis A: Chemical. 158:199-208
The oxidative dehydrogenation of ethane (ODE) was studied over Na 2 O/CaO, Sm 2 O 3 /CaO and Sm 2 O 3 catalysts at 923 K using different oxygen partial pressures. The type of interaction of oxygen with these catalysts was derived from measurements of
Autor:
M Baerns, O.V Buyevskaya
Publikováno v:
Catalysis Today. 42:315-323
Results on the oxidative conversion of propane on three types of catalysts on which different mechanisms of propane activation prevail are discussed, whereby the reaction conditions and final product distribution are affected. In the case of the redo
Ethylene recovery from the gas product of methane oxidative coupling by temperature swing adsorption
Publikováno v:
Gas Separation & Purification. 10:85-88
Ethylene recovery was carried out from the gas product of oxidative coupling of methane by the temperature swing adsorption (TSA) method on NaA zeolites modified by Ca2+. The maximum concentration of ethylene was 98 vol.% in the output mixture. The r