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Fluid Catalytic Cracking process and apparatus for miximizar Light Olefins or olefin Light and Middle distillates

机译:混合亚胺轻烯烃或烯烃轻馏分和中间馏分的流化催化裂化工艺及装置

摘要

Disclosed is an apparatus and Process for Fluid Catalytic Cracking, which provides an efficient conversion of heavy Hydrocarbon feeds to Light Olefins, AROMATICS, and Gasoline. A countercurrent flow reactor that operates in Turbulent Fluidization regimes of Bubbling or is integrated with a Lifting Fluid Catalytic Cracking reactor.A Hydrocarbon feed is heavy catalytic cracked Gasoline and Light Olefins in the Reactor Riser reactor in co current Flow.To improve the production and the selectivity of Light olefin Hydrocarbon products from the Reactor of Elevation, such as in the range of C 4 Hydrocarbon and naphtha, can be recycled and processed in the Reactor in countercurrent Flow.The Integration of flow reactor in countercurrent reactor with a Lifting System of a FCC Catalyst regeneration and conventional Heat balance can address problems commonly associated with Cracking processes in two stages, Can Substantially increase the conversion Global Production of Light Olefins,And / or may increase the ability to process heavier feedstock.
机译:公开了一种用于流体催化裂化的设备和方法,其提供了将重质烃进料有效转化为轻质烯烃,AROMATICS和汽油的方法。逆流反应器在鼓泡的湍流流化状态下运行或与提升流化催化裂化反应器集成。烃类进料是并流的反应器立管反应器中的重催化裂化汽油和轻烯烃,以提高产量和来自高程反应器的轻质烯烃产物的选择性(例如C 4烃和石脑油范围内的产物)可以在反应器中以逆流方式进行循环和处理。 FCC催化剂的再生和常规的热平衡可以在两个阶段解决裂化工艺通常存在的问题,可以显着提高轻质烯烃的全球转化率,并且可以提高处理重质原料的能力。

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