Production of 1-Butene and Propylene From Ethylene
    1.
    发明申请
    Production of 1-Butene and Propylene From Ethylene 有权
    从乙烯生产1-丁烯和丙烯

    公开(公告)号:US20120095275A1

    公开(公告)日:2012-04-19

    申请号:US12903794

    申请日:2010-10-13

    IPC分类号: C07C2/10 C07C2/08

    摘要: A process for producing propylene and 1-butene is disclosed. The process comprises dimerizing ethylene in the presence of a dimerization catalyst to produce a dimerization mixture comprising 1-butene and 2-butenes. The dimerization mixture is distilled to produce a 1-butene stream containing 1-butene and ethylene, a 2-butenes stream, and a heavy stream. The 2-butenes stream is reacted with ethylene in the presence of a metathesis catalyst to produce a metathesis mixture comprising propylene, ethylene, and 2-butenes. Propylene is separated from the metathesis mixture.

    摘要翻译: 公开了一种生产丙烯和1-丁烯的方法。 该方法包括在二聚催化剂存在下二聚乙烯以产生包含1-丁烯和2-丁烯的二聚混合物。 将二聚混合物蒸馏以产生含有1-丁烯和乙烯,2-丁烯流和重流的1-丁烯流。 在复分解催化剂存在下,使2-丁烯物流与乙烯反应以产生包含丙烯,乙烯和2-丁烯的复分解混合物。 丙烯与复分解混合物分离。

    PROCESS FOR CRACKING HEAVY HYDROCARON FEED
    2.
    发明申请
    PROCESS FOR CRACKING HEAVY HYDROCARON FEED 有权
    破碎重油加料方法

    公开(公告)号:US20120130139A1

    公开(公告)日:2012-05-24

    申请号:US12951106

    申请日:2010-11-22

    IPC分类号: C07C4/04

    摘要: A process for cracking a heavy hydrocarbon feed is disclosed. The heavy hydrocarbon feed is passed to a first zone of a vaporization unit to separate a first vapor stream and a first liquid stream. The first liquid stream is passed to a second zone of the vaporization unit and contacted intimately with a countercurrent steam to produce a second vapor stream and a second liquid stream. The second vapor stream is contacted with a wash liquid in a rectification section to form a rectified stream. The first vapor stream and the rectified stream are cracked in the radiant section of the steam cracker to produce a cracked effluent.

    摘要翻译: 公开了一种用于裂解重质烃进料的方法。 将重质烃进料通入蒸发单元的第一区域以分离第一蒸气流和第一液体流。 将第一液体流送至蒸发单元的第二区域,并与逆流蒸汽紧密接触以产生第二蒸气流和第二液体流。 第二蒸气流与整流段中的洗涤液体接触以形成整流流。 第一蒸汽流和精馏流在蒸汽裂解器的辐射段中裂解,产生裂化流出物。

    Process for cracking heavy hydrocarbon feed
    4.
    发明授权
    Process for cracking heavy hydrocarbon feed 有权
    裂解重烃进料的方法

    公开(公告)号:US08273936B2

    公开(公告)日:2012-09-25

    申请号:US12951106

    申请日:2010-11-22

    IPC分类号: C10G9/36

    摘要: A process for cracking a heavy hydrocarbon feed is disclosed. The heavy hydrocarbon feed is passed to a first zone of a vaporization unit to separate a first vapor stream and a first liquid stream. The first liquid stream is passed to a second zone of the vaporization unit and contacted intimately with a countercurrent steam to produce a second vapor stream and a second liquid stream. The second vapor stream is contacted with a wash liquid in a rectification section to form a rectified stream. The first vapor stream and the rectified stream are cracked in the radiant section of the steam cracker to produce a cracked effluent.

    摘要翻译: 公开了一种用于裂解重质烃进料的方法。 将重质烃进料通入蒸发单元的第一区域以分离第一蒸气流和第一液体流。 将第一液体流送至蒸发单元的第二区域,并与逆流蒸汽紧密接触以产生第二蒸气流和第二液体流。 第二蒸气流与整流段中的洗涤液体接触以形成整流流。 第一蒸汽流和精馏流在蒸汽裂解器的辐射段中裂解,产生裂化流出物。

    ETHYLENE SEPARATION PROCESS
    7.
    发明申请
    ETHYLENE SEPARATION PROCESS 有权
    乙烯分离方法

    公开(公告)号:US20140194664A1

    公开(公告)日:2014-07-10

    申请号:US13738685

    申请日:2013-01-10

    IPC分类号: C07C7/04 C07C4/06

    摘要: Ethylene separation processes are described herein. The ethylene separation processes generally include introducing a feed stream including ethylene and butene into a de-ethenizer; and separating the ethylene from the butene via fractional distillation within the de-ethenizer to form an overhead stream including separated ethylene and a bottoms stream including separated butene, wherein the de-ethenizer operates at a pressure of less than 350 psig.

    摘要翻译: 乙烯分离方法在本文中描述。 乙烯分离方法通常包括将包含乙烯和丁烯的进料流引入去乙烯化器中; 以及在去乙烯化器内通过分馏从乙烯中分离出乙烯以形成包括分离的乙烯和包含分离的丁烯的塔底物流的塔顶物流,其中脱乙烯化器的操作压力小于350psig。

    Production of 1-butene and propylene from ethylene
    8.
    发明授权
    Production of 1-butene and propylene from ethylene 有权
    从乙烯生产1-丁烯和丙烯

    公开(公告)号:US08395005B2

    公开(公告)日:2013-03-12

    申请号:US12903794

    申请日:2010-10-13

    IPC分类号: C07C6/04 C07C5/25 C07C2/06

    摘要: A process for producing propylene and 1-butene is disclosed. The process comprises dimerizing ethylene in the presence of a dimerization catalyst to produce a dimerization mixture comprising 1-butene and 2-butenes. The dimerization mixture is distilled to produce a 1-butene stream containing 1-butene and ethylene, a 2-butenes stream, and a heavy stream. The 2-butenes stream is reacted with ethylene in the presence of a metathesis catalyst to produce a metathesis mixture comprising propylene, ethylene, and 2-butenes. Propylene is separated from the metathesis mixture.

    摘要翻译: 公开了一种生产丙烯和1-丁烯的方法。 该方法包括在二聚催化剂存在下二聚乙烯以产生包含1-丁烯和2-丁烯的二聚混合物。 将二聚混合物蒸馏以产生含有1-丁烯和乙烯,2-丁烯流和重流的1-丁烯流。 在复分解催化剂存在下,使2-丁烯物流与乙烯反应以产生包含丙烯,乙烯和2-丁烯的复分解混合物。 丙烯与复分解混合物分离。

    Propylene production
    10.
    发明授权
    Propylene production 失效
    丙烯生产

    公开(公告)号:US06872862B2

    公开(公告)日:2005-03-29

    申请号:US10606026

    申请日:2003-06-25

    IPC分类号: C07C5/25 C07C6/04

    CPC分类号: C07C5/2568 C07C6/04 C07C11/06

    摘要: A method for making propylene from alpha olefins, internal linear olefins and isoolefins wherein the alpha olefins are subjected to a combination of hydrogenation and double bond isomerization to form additional internal linear olefins, the internal linear olefins are separated from the isoolefins and disproportionated with ethylene to form a propylene product, while the thus separated isoolefins are subjected to skeletal isomerization to form yet additional internal linear olefins to be converted into yet additional propylene product.

    摘要翻译: 由α-烯烃,内部线性烯烃和异烯烃制备丙烯的方法,其中α-烯烃经受氢化和双键异构化的组合以形成另外的内部线性烯烃,内部线性烯烃与异烯烃分离并用乙烯歧化 形成丙烯产物,同时将如此分离的异烯烃进行骨架异构化以形成另外的内部直链烯烃,以转化为另外的丙烯产物。