Eine Plattform für die Wissenschaft: Bauingenieurwesen, Architektur und Urbanistik
Specifics of the deactivation of acid and zinc-containing propane aromatization catalysts
Abstract The specifics of the deactivation of acid and Zn-containing MFI catalysts in the propane aromatization reaction at high-feed space velocities (600–2400 h−1) and temperatures (550–610°C) was studied. The kinetics of the buildup of carbonaceous products (coke) was investigated in situ during the catalytic reaction in a thermal analyzer coupled to a mass spectrometer and a gas chromatograph (TA-MS-GC). The nature of the coke was studied by means of differential thermal analysis (DTA) and elemental analysis. It was found that the buildup of heavy coke on the H-MFI zeolite takes place on the outer crystal surface and pore openings, thus leading to a decrease in the propane conversion at the beginning of the reaction. In contrast, light coke appears first and is transformed to heavy coke at later stages on Zn/H-MFI. The light coke leads to a decrease in the yield of methane, ethane, and ethylene, and the heavy coke impedes the formation of aromatic hydrocarbons.
Specifics of the deactivation of acid and zinc-containing propane aromatization catalysts
Abstract The specifics of the deactivation of acid and Zn-containing MFI catalysts in the propane aromatization reaction at high-feed space velocities (600–2400 h−1) and temperatures (550–610°C) was studied. The kinetics of the buildup of carbonaceous products (coke) was investigated in situ during the catalytic reaction in a thermal analyzer coupled to a mass spectrometer and a gas chromatograph (TA-MS-GC). The nature of the coke was studied by means of differential thermal analysis (DTA) and elemental analysis. It was found that the buildup of heavy coke on the H-MFI zeolite takes place on the outer crystal surface and pore openings, thus leading to a decrease in the propane conversion at the beginning of the reaction. In contrast, light coke appears first and is transformed to heavy coke at later stages on Zn/H-MFI. The light coke leads to a decrease in the yield of methane, ethane, and ethylene, and the heavy coke impedes the formation of aromatic hydrocarbons.
Specifics of the deactivation of acid and zinc-containing propane aromatization catalysts
Asachenko, E. V. (Autor:in) / Rodina, O. V. (Autor:in) / Ordomskii, V. V. (Autor:in) / Gur’ev, Yu. V. (Autor:in) / Ivanova, I. I. (Autor:in)
Petroleum Chemistry ; 48 ; 100-104
01.03.2008
5 pages
Aufsatz (Zeitschrift)
Elektronische Ressource
Englisch
Specifics of the deactivation of acid and zinc-containing propane aromatization catalysts
Springer Verlag | 2008
|Deactivation features of gallium-containing zeolites in the propane aromatization process
Springer Verlag | 2017
|Oxidative aromatization of propane, butane, and butane-butylene fraction
Springer Verlag | 2007
|A study of propane aromatization on a zeolite-containing catalyst with different Si/Al ratios
Springer Verlag | 2012
|