IONIC LIQUID CATALYZED OLEFIN OLIGOMERIZATION FOR DISTILLATE PRODUCTION
    1.
    发明申请
    IONIC LIQUID CATALYZED OLEFIN OLIGOMERIZATION FOR DISTILLATE PRODUCTION 有权
    离子液体催化烯烃低分子化生产

    公开(公告)号:US20120165586A1

    公开(公告)日:2012-06-28

    申请号:US12975750

    申请日:2010-12-22

    IPC分类号: C07C2/08

    摘要: Processes for upgrading condensate in a first hydrocarbon stream to provide distillate material may involve ionic liquid catalyzed olefin oligomerization of olefins in the first hydrocarbon stream to provide a first distillate enriched stream, dechlorination of the first distillate enriched stream, hydroprocessing at least one of a second and a third hydrocarbon stream to provide a second distillate enriched stream, and separation of a distillate product from the first and second distillate enriched streams.

    摘要翻译: 用于升级第一烃流中的冷凝物以提供馏出物材料的方法可以涉及第一烃流中的离子液体催化的烯烃低聚烯烃,以提供第一馏出物富集料流,第一馏出物富集料流的脱氯,加氢处理至少一个第二馏出物 和第三烃流,以提供富含第二馏出物的料流,以及将馏出物产物与第一和第二馏出物富集料流分离。

    PROCESS FOR REACTING ISO-ALKANE
    2.
    发明申请
    PROCESS FOR REACTING ISO-ALKANE 有权
    反应ISO-ALKANE的方法

    公开(公告)号:US20110130602A1

    公开(公告)日:2011-06-02

    申请号:US12628020

    申请日:2009-11-30

    IPC分类号: C07C2/76

    CPC分类号: C07C2/58 C07C2531/14 C07C9/14

    摘要: A process for reacting an iso-alkane, comprising: a) partially converting one or more olefins in an olefinic feedstock with an ionic liquid catalyst to make a converted olefinic feedstock; and b) alkylating the iso-alkane with the converted olefinic feedstock, wherein a reaction heat that is evolved during the alkylating is at least 20% less than if the alkylating step is done with the iso-alkane and the olefinic feedstock without the partially converting step. Also, a process for reacting an iso-alkane, comprising: a) partially converting one or more olefins in an olefinic feedstock to make a converted olefinic feedstock, wherein the converting is different from isomerization; b) isolating from the converted olefinic feedstock: i. an enriched feed that has linear internal olefins, and ii. products having a boiling point of 150° C. or higher; and c) alkylating the iso-alkane with the enriched feed to make an alkylate gasoline blending component.

    摘要翻译: 一种使异烷烃反应的方法,包括:a)使用离子液体催化剂部分地将烯烃原料中的一种或多种烯烃转化成转化的烯烃原料; 和b)用转化的烯烃原料烷基化异烷烃,其中在烷基化过程中放出的反应热比通过异烷烃和烯烃原料进行烷基化步骤少至少20%而不进行部分转化 步。 另外,使异烷烃反应的方法包括:a)部分转化烯烃原料中的一种或多种烯烃以制备转化的烯烃原料,其中转化不同于异构化; b)从转化的烯烃原料中分离: 具有线性内烯烃的富集饲料,和ii。 沸点为150℃以上的产品; 和c)用富集的进料烷基化异烷烃以制备烷基化汽油调和组分。

    Extremely low acidity ultrastable Y zeolite catalyst composition and process
    5.
    发明授权
    Extremely low acidity ultrastable Y zeolite catalyst composition and process 有权
    极低的酸度超稳定的Y沸石催化剂组成及工艺

    公开(公告)号:US06860986B2

    公开(公告)日:2005-03-01

    申请号:US10290791

    申请日:2002-11-08

    摘要: A catalyst composition comprising a low acidity, highly dealuminated ultra stable Y zeolite having an Alpha value of less than about 3 and Broensted acidity measured by FT-IR from about 1 to about 20, preferably from about 1-10, micro mole/g of, an amorphous cracking component and a catalytic amount of hydrogenation component selected from the group consisting of a Group VI metal, a Group VIII metal, and mixtures thereof is disclosed. The present invention provides for a process for converting hydrocarbonaceous oils comprising contacting the hydrocarbonaceous oils with the catalyst under suitable hydrocarbon conversion conditions. Such processes in include, but are not limited to, single stage hydrocracking, two-stage hydrocracking, series-flow hydrocracking, mild hydrocracking, lube hydrocracking, hydrotreating, lube hydrofinishing, hydrodesulphurization, hydrodenitrification, catalytic dewaxing and catalytic cracking.

    摘要翻译: 一种催化剂组合物,其包含具有低于约3的α值低于约3的低酸度,高度脱铝的超稳定Y沸石,通过FT-IR测量的Broensted酸度为约1至约20,优选约1-10微摩尔/ g 公开了无定形裂化组分和催化量的选自VI族金属,VIII族金属及其混合物的氢化组分。 本发明提供了一种用于转化含烃油的方法,包括在合适的烃转化条件下使烃类油与催化剂接触。 这些方法包括但不限于单级加氢裂化,两级加氢裂化,串联加氢裂化,轻度加氢裂化,润滑油加氢裂化,加氢处理,润滑油加氢精制,加氢脱硫,加氢脱氮,催化脱蜡和催化裂化。