Ethane may be catalytically oxidatively dehydrogenated to ethylene at high conversions and high selectivity in a circulating fluidized bed (CFB) reactor in the presence of oxygen in the feed in an amount above the flammability limit. The reactor has an attached regeneration reactor to regenerate the catalyst and cycle back to the CFB.
申请公布号
CA2867731(A1)
申请公布日期
2016.04.15
申请号
CA20142867731
申请日期
2014.10.15
申请人
NOVA CHEMICALS CORPORATION
发明人
SIMANZHENKOV, VASILY;GOODARZNIA, SHAHIN;GAO, XIAOLIANG;KUSTOV, LEONID MODESTOVICH;KUCHEROV, ALEKSEY VICTOROVICH;FINASHINA, ELENA DMITRIEVNA;SERHAL, KAMAL ELIAS