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dc.contributor.authorMulla, S A R-
dc.contributor.authorChoudhary, V R-
dc.date.accessioned2013-10-29T08:54:04Z-
dc.date.available2013-10-29T08:54:04Z-
dc.date.issued2003-11-
dc.identifier.issn0975-0991 (Online); 0971-457X (Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/22801-
dc.description615-618en_US
dc.description.abstractOxidative dehydrogenation of ethane to ethylene in presence of steam (steam/C2H6 mole ratio =1.0) and limited O2 (C2H6/O2 mole ratio ≥ 4.0) over a SrO-promoted Sm2O3, supported on low surface area macroporous silica-alumina commercial catalyst carrier (SA5205, obtained from Norton Co. USA) has been thoroughly investigated. Effect of different process parameters such as temperature (700-850°C), C2H6/O2 feed ratio (4.0-8.0) and gas hourly space velocity (5×104- 20×104 cm3g-1h-1) on the conversion of ethane and product selectivity in the process has been studied. High selectivity (≥80%) of C2+ olefins at 50-70% conversion of ethane could be obtained at very low contact time without coke deposition on the catalyst at 800-850°C.en_US
dc.language.isoen_USen_US
dc.publisherNISCAIR-CSIR, Indiaen_US
dc.rights CC Attribution-Noncommercial-No Derivative Works 2.5 Indiaen_US
dc.sourceIJCT Vol.10(6) [November 2003]en_US
dc.titleConversion of ethane to ethylene in presence of limited O2 over supported SrO promoted Sm2O3 catalysten_US
dc.typeArticleen_US
Appears in Collections:IJCT Vol.10(6) [November 2003]

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