A series of Li-doped catalysts on zirconia or sulfated zirconia were prepared and investigated in the catalytic reaction of ethane oxidative dehydrogenation into ethylene. It is found that zirconia and sulfated zirconia supports prepared by different methods show varying nature and thus influence th
Oxidative coupling of methane and oxidative dehydrogenation of ethane over strontium-promoted rare earth oxide catalysts
✍ Scribed by Vasant R. Choudhary; Shafeek A. R. Mulla; Vilas H. Rane
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 1998
- Tongue
- English
- Weight
- 275 KB
- Volume
- 71
- Category
- Article
- ISSN
- 0268-2575
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✦ Synopsis
Sr-promoted rare earth (viz. La, Ce, Pr, Nd, Sm, Eu, Gd, Dy, Er and Yb)
oxide catalysts (Sr/rare earth ratio \ 0É1) 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 †erent temperatures (700 and 800¡C) and (or ratios (4È8), at low contact time (space CH 4 C 2 H 6 )/O 2 velocity \ 102 000 cm3 g~1 h~1). For the OCM process, the catalyst SrÈLa 2 O 3 shows the best performance. The Sr-promoted and Nd 2 O 3 , Sm 2 O 3 , Eu 2 O 3 catalysts also show good methane conversion and selectivity for Er 2 O 3 C 2 hydrocarbons but the and catalysts show very poor per-SrÈCeO 2 SrÈDy 2 O 3 formance. However, for the ODE process, the best performance is shown by the catalyst. The other catalysts also show good ethane conversion and SrÈNd 2 O 3 selectivity for ethylene ; their performance is comparable at higher temperatures (º800¡C), but at lower temperature (700¡C) the and cata-SrÈCeO 2 SrÈPr 6 O 11 lysts show poor selectivity. 1998 SCI.
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The energy‐efficient and safe conversion of ethane into ethylene is possible by simultaneous exothermic oxidative dehydrogenation and endothermic cracking of ethane in the presence of steam and limited amounts of O~2~, by using the thermally and hydrothermally stable supported catalyst SrO/La~2~O~3~
reforming, oxidative conversion and simultaneous oxidative con-CO 2 version and or steam reforming of methane to syngas (CO and over CO 2 H 2 ) NiOÈCoOÈMgO (Co : Ni : Mg \ 0É5 : 0É5 : 1É0) solid solution at 700È850¡C and high space velocity (5É1 ] 105 cm3 g~1 h~1 for oxidative conversion and 4É5 ] 1