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1.发明授权Method and device for catalytic cracking comprising in parallel at least an upflow reactor and at least a downflow reactor 有权用于催化裂化的方法和装置，其至少包括上流式反应器和至少一个下流式反应器公开(公告)号：US07220351B1
公开(公告)日：2007-05-22
申请号：US10149597
申请日：2000-11-28
摘要： An apparatus and a process for catalytic cracking of a hydrocarbon feed is described, carried out in at least two reaction zones, one (30) operating in catalyst riser mode, wherein the feed and catalyst from regeneration zone (3) are circulated from bottom to top, the first gases produced are separated from the coked catalyst in a first separation zone (38), the catalyst is stripped (40), a first cracking and stripping effluent (42) is recovered and the coked catalyst is recycled (45) to the regeneration zone. Catalyst (12) from regeneration zone (3) and a hydrocarbon feed (19) are introduced into the upper portion of a dropper reaction zone (16), the catalyst and feed being circulated from top to bottom, the coked catalyst is separated from the second gases produced in a second separation zone (20), the second gases (24) produced are recovered and the coked catalyst is recycled (25) to the regeneration zone.
摘要翻译： 描述了在至少两个反应区域中进行的用于烃进料的催化裂化的装置和方法，一个（30）以催化剂提升管模式操作，其中来自再生区（3）的进料和催化剂从底部循环到 在第一分离区（38）中将所产生的第一种气体与焦炭催化剂分离，将催化剂汽提（40），回收第一裂解和汽提流出物（42），将焦化的催化剂再循环（45）至 再生区域。 来自再生区（3）的催化剂（12）和烃进料（19）被引入滴管反应区（16）的上部，催化剂和进料从顶部向底部循环，将焦化的催化剂从 在第二分离区（20）中产生的第二气体，回收所生产的第二气体（24），并将焦化的催化剂再循环（25）至再生区。
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