The conversion of propane in the presence of oxygen on V-K/Al2O3 catalysts with different surface area and in different feed conditions has been investigated. The activation energy measured at low conversion is 21 kcal/mol (88 kJ/mol) and the reaction order of propane is 1. In order to propose a reaction pathway, complementary experiments have been performed with a K-free V/Al2O3 catalyst, and propene and 2-propanol oxidation tests have also been done. A reaction scheme for the propane oxidation process is proposed. Two different reaction regimes have been observed. Below 950 K true catalytic reaction occurs with propene, ethene, CO2 and CO as the only detectable products. Both CO, and ethene productions likely occur through a parallel-successive reaction scheme with respect to propene production. The key surface intermediate is thought to be the sec-propoxide species, that can give propene by elimination and either COchi or ethene by oxidation. Above near 950 K a new regime involving gas-phase species is observed. In this range, where consumption of oxygen is already total or nearly total, the cracking of propane to ethene+methane becomes predominant. This reaction can be limited by filling the empty space of the reactor. (C) 2002 Elsevier Science B.V. All rights reserved.
A study of the reaction pathway upon propane oxidation over V-K/Al2O3 catalysts
RESINI, CARLO;BUSCA, GUIDO;
2002-01-01
Abstract
The conversion of propane in the presence of oxygen on V-K/Al2O3 catalysts with different surface area and in different feed conditions has been investigated. The activation energy measured at low conversion is 21 kcal/mol (88 kJ/mol) and the reaction order of propane is 1. In order to propose a reaction pathway, complementary experiments have been performed with a K-free V/Al2O3 catalyst, and propene and 2-propanol oxidation tests have also been done. A reaction scheme for the propane oxidation process is proposed. Two different reaction regimes have been observed. Below 950 K true catalytic reaction occurs with propene, ethene, CO2 and CO as the only detectable products. Both CO, and ethene productions likely occur through a parallel-successive reaction scheme with respect to propene production. The key surface intermediate is thought to be the sec-propoxide species, that can give propene by elimination and either COchi or ethene by oxidation. Above near 950 K a new regime involving gas-phase species is observed. In this range, where consumption of oxygen is already total or nearly total, the cracking of propane to ethene+methane becomes predominant. This reaction can be limited by filling the empty space of the reactor. (C) 2002 Elsevier Science B.V. All rights reserved.I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.