Process for distillation of petroleum by progressive separations
    4.
    发明授权
    Process for distillation of petroleum by progressive separations 失效
    通过逐步分离蒸馏石油的方法

    公开(公告)号:US4664785A

    公开(公告)日:1987-05-12

    申请号:US703496

    申请日:1985-02-20

    CPC classification number: C10G7/00

    Abstract: The process consists in successively separating increasingly heavy petroleum cuts at the head of a plurality of columns CO1, CO2, CO3 and Cl0 of a first series of columns which feed individually each column of the second series. The column CO7 is a gasoline stabilizing column which feeds an installation for fractionating light petroleum gases. The column CO4 is a gasoline fractionating column. The columns CO5 and CO6 are columns for separating petroleum naphthas from kerosine. The atmospheric residue collected at the bottom of the column Cl0 is processed in the vacuum distillation column Cl2 and the residue from this column is processed in the second vacuum distillation column Cl3 after reheating in a furnace.By carrying out a succession of progressive separations performed in a series of columns of small volume, more efficient utilization of the recovery heat is achieved.

    Abstract translation: 该方法包括在分别进料第二系列的每一列的第一系列塔的多个塔CO1,CO2,CO3和Cl0的塔头上连续分离越来越重的石油馏分。 柱CO7是汽油稳定塔,其供给用于分馏轻质石油气体的装置。 柱CO4是汽油分馏塔。 列CO5和CO6是用于将石脑油与煤油分离的柱。 在塔C1底部收集的常压残留物在真空蒸馏塔C12中进行处理,并且在炉中再加热之后,将该塔的残余物在第二真空蒸馏塔C13中进行处理。 通过在一系列小批量的列中进行一系列逐步分离,可以更有效地利用回收热量。

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