PROCESS FOR THE PRODUCTION OF AROMATICS WITH EXTRACTION BEFORE AROMATIZATION

    公开(公告)号:US20200339892A1

    公开(公告)日:2020-10-29

    申请号:US16767935

    申请日:2018-11-16

    Abstract: Process for the production of C6-C7 aromatic compounds from a hydrocarbon feedstock of naphtha type comprising the following stages: a) the said feedstock (1) is sent into a first fractionation unit (2) in order to obtain an upper stream (3) comprising C6 and C7 hydrocarbon compounds and a lower stream (4) comprising C8 to C10 hydrocarbon compounds; b) the upper stream (3) and a stream (12) comprising C6 and C7 aromatic compounds obtained on conclusion of stage e) are sent into a unit for extraction of the aromatics (5) in order to obtain an aromatic base (6) and a liquid effluent (7); c) the liquid effluent (7) is sent into a first catalytic reforming unit (8) in order to obtain a first reformate effluent (9); d) the said first reformate effluent (9) is sent into a reformate separation section (10) in order to obtain a first stream (11) comprising C5 hydrocarbon compounds and a second stream (12) comprising C6 and C7 aromatic compounds; e) the second stream (12) comprising C6 and C7 aromatic compounds is recycled in stage b).

    REFORMING PROCESS WITH OPTIMIZED DISTRIBUTION OF THE CATALYST
    13.
    发明申请
    REFORMING PROCESS WITH OPTIMIZED DISTRIBUTION OF THE CATALYST 有权
    具有优化催化剂分布的改性方法

    公开(公告)号:US20160032199A1

    公开(公告)日:2016-02-04

    申请号:US14810990

    申请日:2015-07-28

    CPC classification number: C10G59/02

    Abstract: The invention relates to a process for catalytic reforming of a naphtha hydrocarbon feedstock using a number of reaction zones in series, wherein the reaction zones contain a reforming catalyst bed. The process comprises comprising the following stages: sending hydrocarbon feedstock that is heated with hydrogen through the reaction zones to convert paraffinic and naphthenic compounds into aromatic compounds, with the effluent that is produced by each reaction zone, except for the last reaction zone, being heated before its introduction into the following reaction zone; drawing off a reformate from the last reaction zone.

    Abstract translation: 本发明涉及使用多个串联反应区的石脑油原料的催化重整方法,其中反应区含有重整催化剂床。 该方法包括以下步骤:将通过氢气加热的烃原料通过反应区转化成链烷烃和环烷化合物转化为芳族化合物,除了最后一个反应区之外,每个反应区产生的流出物被加热 在引入以下反应区之前; 从最后一个反应区撤出重整产品。

    MULTI-TUBE RADIAL BED REACTOR
    14.
    发明申请
    MULTI-TUBE RADIAL BED REACTOR 有权
    多管径向床反应器

    公开(公告)号:US20150328612A1

    公开(公告)日:2015-11-19

    申请号:US14712965

    申请日:2015-05-15

    Abstract: The present invention concerns a radial bed reactor comprising a vessel provided with a reaction zone with a moving catalyst bed. The reactor further comprises, inside the reaction zone: at least two feed distribution tubes, each having a first end in communication with the feed inlet means and a second, closed end, the distribution tubes extending in a substantially vertical manner and being designed to allow the feed to pass through the reaction zone and to retain the catalysts; and at least two effluent collection tubes, each having a first end (14) communicating with the effluent outlet means and a second, closed end (15), the collection tubes extending in a substantially vertical manner and being designed to allow effluent to pass through the collection tube and to retain the catalysts.

    Abstract translation: 本发明涉及一种径向床反应器,其包括设置有与移动的催化剂床的反应区的容器。 反应器还包括在反应区内:至少两个进料分配管,每个进料分配管具有与进料入口装置连通的第一端和第二封闭端,分配管以基本垂直的方式延伸并被设计成允许 进料通过反应区并保留催化剂; 和至少两个流出物收集管,每个具有与流出物出口装置连通的第一端(14)和第二封闭端(15),所述收集管以基本垂直的方式延伸并设计成允许流出物通过 收集管并保留催化剂。

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