Method for recovering entrained ionic liquid from an ionic liquid immiscible phase
    1.
    发明授权
    Method for recovering entrained ionic liquid from an ionic liquid immiscible phase 有权
    从离子液体不混溶相中回收夹带的离子液体的方法

    公开(公告)号:US09328296B2

    公开(公告)日:2016-05-03

    申请号:US14229462

    申请日:2014-03-28

    Applicant: UOP LLC

    CPC classification number: C10G29/205 B01D17/047 C10G2300/70

    Abstract: A method for recovering entrained ionic liquid from an immiscible phase containing droplets of ionic liquid is described. The method includes contacting the immiscible phase containing the droplets of ionic liquid with a scrubbing ionic liquid phase in a scrubbing zone. The immiscible phase containing the droplets of ionic liquid has a first level of droplets of ionic liquid. At least a portion of the droplets of ionic liquid are transferred to the scrubbing ionic liquid phase to form a recovered ionic liquid phase comprising the scrubbing ionic liquid and the transferred portion of the droplets of ionic liquid and a second immiscible phase having a second level of droplets of ionic liquid lower than the first level. The second immiscible phase is separated from the recovered ionic liquid phase.

    Abstract translation: 描述了从含有离子液体的液滴的不混溶相中回收夹带的离子液体的方法。 该方法包括使含有离子液体的液滴的不混溶相与洗涤区中的洗涤离子液相接触。 含有离子液体液滴的不混溶相具有离子液体的第一级液滴。 离子液体的至少一部分液滴被转移到洗涤离子液相以形成回收的离子液相,其包含洗涤离子液体和离子液体的液滴的转移部分和具有第二水平的第二不混溶相 离子液滴小于第一级。 第二不混溶相与回收的离子液相分离。

    Methods for recovering ionic liquid fines from a process stream
    7.
    发明授权
    Methods for recovering ionic liquid fines from a process stream 有权
    从工艺流中回收离子液体细粉的方法

    公开(公告)号:US09522859B2

    公开(公告)日:2016-12-20

    申请号:US14567877

    申请日:2014-12-11

    Applicant: UOP LLC

    Abstract: Methods of recovering droplets of ionic liquid catalyst from a process stream are described. The volume fraction of ionic liquid in the hydrocarbon is increased to cause the ionic liquid droplets to coalesce. One method incorporates various combinations of gravity separation zone(s) and fractionation zones. Another method involves using a combination of a flash vessel and a fractionation zone, as well as an optional gravity separation zone.

    Abstract translation: 描述了从工艺流中回收离子液体催化剂的液滴的方法。 烃中离子液体的体积分数增加,导致离子液滴聚结。 一种方法包括重力分离区和分馏区的各种组合。 另一种方法包括使用闪蒸容器和分馏区的组合以及可选的重力分离区。

    METHOD FOR RECOVERING ENTRAINED IONIC LIQUID FROM AN IONIC LIQUID IMMISCIBLE PHASE
    8.
    发明申请
    METHOD FOR RECOVERING ENTRAINED IONIC LIQUID FROM AN IONIC LIQUID IMMISCIBLE PHASE 有权
    从离子液体不稳定相中回收被引入的离子液体的方法

    公开(公告)号:US20150274614A1

    公开(公告)日:2015-10-01

    申请号:US14229462

    申请日:2014-03-28

    Applicant: UOP LLC

    CPC classification number: C10G29/205 B01D17/047 C10G2300/70

    Abstract: A method for recovering entrained ionic liquid from an immiscible phase containing droplets of ionic liquid is described. The method includes contacting the immiscible phase containing the droplets of ionic liquid with a scrubbing ionic liquid phase in a scrubbing zone. The immiscible phase containing the droplets of ionic liquid has a first level of droplets of ionic liquid. At least a portion of the droplets of ionic liquid are transferred to the scrubbing ionic liquid phase to form a recovered ionic liquid phase comprising the scrubbing ionic liquid and the transferred portion of the droplets of ionic liquid and a second immiscible phase having a second level of droplets of ionic liquid lower than the first level. The second immiscible phase is separated from the recovered ionic liquid phase.

    Abstract translation: 描述了从含有离子液体的液滴的不混溶相中回收夹带的离子液体的方法。 该方法包括使含有离子液体的液滴的不混溶相与洗涤区中的洗涤离子液相接触。 含有离子液体液滴的不混溶相具有离子液体的第一级液滴。 离子液体的至少一部分液滴被转移到洗涤离子液相以形成回收的离子液相,其包含洗涤离子液体和离子液体的液滴的转移部分和具有第二水平的第二不混溶相 离子液滴小于第一级。 第二不混溶相与回收的离子液相分离。

    Chloride management in ionic liquid alkylation processes

    公开(公告)号:US10384988B2

    公开(公告)日:2019-08-20

    申请号:US15346561

    申请日:2016-11-08

    Applicant: UOP LLC

    Abstract: The present invention involves processes and equipment for handling chloride in an ionic liquid alkylation system. The processes involve not only breaking down the organic chloride to active HCl for ionic liquid activation, but also recovering HCl in the effluent downstream to maintain the HCl requirements while also reducing HCl emissions. This equipment may be used in conjunction with an isomerization reaction zone which is integrated into the ionic liquid alkylation process to further isomerize n-paraffins to isoparaffins for recycle to the alkylation reaction zone.

Patent Agency Ranking