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Dual riser catalytic cracker for increased light olefin yield

机译:双提升管催化裂化器可提高轻质烯烃的收率

摘要

A process for improving the yield of ethylene and propylene from a light naphtha feedstock includes obtaining light naphtha feedstock from a primary cracking zone having a cracking catalyst. The light naphtha feedstock is contacted with an olefin catalyst in an olefin producing zone to produce an ethylene- and propylene-rich stream. After reacting with the olefin catalyst, the ethylene- and propylene-rich stream is separated from the olefin catalyst from in a separator zone. At least a portion of the olefin catalyst is regenerated by combusting coke deposited on a surface of the olefin catalyst in an oxygen-containing environment, and at least a portion of the olefin catalyst is heated. These portions could be the same one or they could be different. In some embodiments, at least a portion of the olefin catalyst could be neither regenerated nor heated. The olefin catalyst is returned to the olefin producing zone.
机译:一种提高轻质石脑油原料的乙烯和丙烯收率的方法,包括从具有裂化催化剂的初级裂化区获得轻质石脑油原料。轻石脑油原料在烯烃生产区中与烯烃催化剂接触,以生产富含乙烯和丙烯的料流。与烯烃催化剂反应后,从分离器区域将富含乙烯和丙烯的料流与烯烃催化剂分离。通过在含氧环境中燃烧沉积在烯烃催化剂表面上的焦炭来再生至少一部分烯烃催化剂,并且加热至少一部分烯烃催化剂。这些部分可以相同,也可以不同。在一些实施方案中,至少一部分烯烃催化剂既不再生也不加热。烯烃催化剂返回到烯烃生产区。

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