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The recovery system in the plant of olefins using distillation catalìtica.

机译:使用蒸馏催化法在烯烃工厂中的回收系统。

摘要

Invention patent: b "system of recurau00e7u00e3o in plant of olefins using distillation catalu00ectica" d .The C ~ 2 ~ C ~ 5 ~ and heavier acetilenos and dienes in a feed stream are hydrogenated without heat generation hidrogenar significantly the C ~ 2 ~ C ~ 3 ~.In addition, the C ~ 4 ~ and heavier olefins may be hydrogenated.Specifically,The gas supply craqueado in a plant of olefins is hydrogenated in a distillation reaction column containing a catalyst for hydrogenation without the need to separate hydrogen from alimeNtau00e7u00e3o and without any significant hydrogenation of ethylene and propylene.A combined reaction fractionation step known as catalytic distillation hydrogenation is used to simultaneously carry out the reactions and separations.While maintaining the hydrogenation conditions such that the ethylene and propylene remain substantially non hydrogenated and essentially of the total other C ~ 2 ~ and heavier hydrocarbon - S.More are hydrogenated.Any non reacted hydrogen can be separated by a membrane and then reacted with materials C ~ 9 ~ and heavier separated to produce hydrogenated pyrolysis gasoline.
机译:发明专利:“使用蒸馏催化剂的烯烃工厂中的精馏体系”。进料流中的C〜2〜C〜5〜以及较重的乙炔和二烯被氢化在没有生热氢的情况下,C〜2〜C〜3〜明显地被氢化。此外,C〜4〜和更重的烯烃可能会被氢化。特别地,烯烃工厂中的供气craqueado在包含无需从alimeNta u00e7 u00e3o中分离氢并且无需对乙烯和丙烯进行任何显着加氢的氢化催化剂。使用称为催化蒸馏加氢的联合反应分馏步骤可同时进行反应和分离。这样的条件使得乙烯和丙烯基本上保持未氢化状态,并且基本上所有其他C〜2〜和更重的烃-S都被氢化。活性氢可通过膜分离,然后与C〜9〜物质反应,并重分离以生产氢化裂解汽油。

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