## Sr-promoted rare earth (viz. La, Ce, Pr, Nd, Sm, Eu, Gd, Dy, Er and Yb) oxide catalysts (Sr/rare earth ratio \ 0Γ1) are compared for their performance in the oxidative coupling of methane (OCM) to hydrocarbons and C 2 oxidative dehydrogenation of ethane (ODE) to ethylene at di β erent temperatur
Comparison of the surface and catalytic properties of rare earth-promoted CaO catalysts in the oxidative coupling of methane
β Scribed by Vilas H Rane; Sopan T Chaudhari; Vasant R Choudhary
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 2006
- Tongue
- English
- Weight
- 141 KB
- Volume
- 81
- Category
- Article
- ISSN
- 0268-2575
No coin nor oath required. For personal study only.
β¦ Synopsis
Abstract
Rare earth (viz. La, Ce, Sm, Nd and Yb) promoted CaO catalysts have been investigated, comparing their surface properties (viz. surface area and basicity/base strength distribution) and catalytic activity/selectivity in the oxidative coupling of methane at different reaction conditions (temperatures, 650β800 Β°C, CH~4~/O~2~ ratios, 2.0β8.0 and space velocity, 51 360 cm^3^ g^β1^ h^β1^). The surface properties and catalytic activity/selectivity are strongly influenced by the rare earth promoter and its concentration. Apart from the Smβpromoted CaO catalyst, both the total and strong basic sites (measured in terms of CO~2~ chemisorbed at 50Β° and 500 Β°C respectively) are decreased due to the promotion of CaO by rare earth metals (viz. La, Ce, Nd and Yb). The catalytic activity/selectivity is strongly influenced by the temperature, particularly below β©½700 Β°C, whereas at higher temperature no further effect is seen. The La~2~O~3~ο£ΏCaO, Nd~2~O~3~ο£ΏCaO and Yb~2~O~3~ο£ΏCaO catalysts showed high activity and selectivity, and also their results are comparable. Among the catalysts, Ndβpromoted CaO (with Nd/Ca = 0.05) showed the best performance (19.5% CH~4~ conversion with 70.8% C~2+~ selectivity) in the oxidative coupling of methane. A close relationship between the surface density of total and strong basic sites (measured in terms of CO~2~ chemisorbed at 50Β° and 500 Β°C respectively) and the C~2+~ selectivity and/or C~2+~ yield has been observed. Copyright Β© 2005 Society of Chemical Industry
π SIMILAR VOLUMES
The catalytic activity and selectivity of and alkaline earth (viz. La 2 O 3 Mg, Ca, Sr and Ba) promoted (alkaline earth metal/La \ 0Γ1) catalysts in La 2 O 3 the oxidative coupling of methane (OCM) to (at 800Β‘C, C 2 -hydrocarbons ratio \ 4 or 8 and gas hourly space velocity \ 102 000 cm3 g~1 h~1) CH
Deposition of LiΓMgO catalyst on commonly used supports (containing SiC, etc.) causes a drastic reduction in SiO 2 , Al 2 O 3 , ZrO 2 , HfO 2 , the catalytic activity/selectivity for the oxidative methane coupling reaction and also in both the total and strong surface basicity. The decrease in the