Recovery of C4 olefins from a product stream comprising C4 olefins, dimethyl ether and C5+ hydrocarbons
    4.
    发明授权
    Recovery of C4 olefins from a product stream comprising C4 olefins, dimethyl ether and C5+ hydrocarbons 失效
    从包含C4烯烃,二甲醚和C5 +烃的产物流中回收C4烯烃

    公开(公告)号:US07060865B2

    公开(公告)日:2006-06-13

    申请号:US10292232

    申请日:2002-11-12

    摘要: Disclosed is a process for removing DME from a stream containing C4 olefins. The process includes providing a first stream comprising C4 olefins, C5+ hydrocarbons, DME, and methanol. The first stream is separated into a second stream comprising the C4 olefins and the DME and a third stream comprising the C5+ hydrocarbons and the methanol. The second stream is directed to a DME absorption unit, wherein the second stream contacts water under conditions effective to separate the C4 olefins from the DME. Also disclosed is a process including contacting the first stream with water in a methanol removal unit under conditions effective to separate remove the methanol therefrom; distilling the methanol-depleted stream to remove C5+ hydrocarbon components, and contacting the stream with water in a DME removal unit under conditions effective to form an overhead stream comprising the C4 olefins and a bottoms stream comprising the DME.

    摘要翻译: 公开了从含有C4烯烃的流中除去DME的方法。 该方法包括提供包含C4烯烃,C5 +烃,DME和甲醇的第一流。 将第一流分离成包含C4烯烃和DME的第二料流和包含C5 +烃和甲醇的第三料流。 第二流被引导到DME吸收单元,其中第二流在有效地将C 4烯烃与DME分离的条件下与水接触。 还公开了一种方法,包括在有效分离除去甲醇的条件下,使第一流与甲醇去除单元中的水接触; 蒸馏除去甲醇的流以除去C5 +烃组分,并在有效形成包含C 4烯烃的塔顶物流和包含DME的塔底物流的条件下,在DME去除单元中使该物流与水接触。

    Process for feeding ethylene to polymerization reactors
    7.
    发明授权
    Process for feeding ethylene to polymerization reactors 有权
    将乙烯供给聚合反应器的方法

    公开(公告)号:US08399586B2

    公开(公告)日:2013-03-19

    申请号:US12584338

    申请日:2009-09-03

    摘要: A process for feeding ethylene into a polymerization system includes providing a low-pressure ethylene stream, one or more low-pressure C3 to C20 monomer streams, an optional low-pressure inert solvent/diluent stream, and one or more reactors; metering the low-pressure ethylene stream, the one or more low-pressure C3 to C20 monomer streams, and the optional low-pressure inert solvent/diluent stream; blending the metered low-pressure ethylene stream, the metered one or more low-pressure C3 to C20 monomer streams, and the metered low-pressure optional inert solvent/diluent stream to form an ethylene-carrying low-pressure blended liquid feed stream; pressurizing the ethylene-carrying low-pressure blended liquid feed stream to the polymerization system pressure with one or more high-pressure pumps to thrm an ethylene-carrying high-pressure blended reactor feed stream; and feeding the ethylene-carrying high-pressure blended reactor feed stream to the one or more reactors.

    摘要翻译: 将乙烯进料到聚合体系中的方法包括提供低压乙烯流,一种或多种低压C3至C20单体流,任选的低压惰性溶剂/稀释剂流和一个或多个反应器; 计量低压乙烯流,一个或多个低压C3至C20单体流和任选的低压惰性溶剂/稀释剂流; 混合计量的低压乙烯流,计量的一个或多个低压C3至C20单体流和计量的低压可选惰性溶剂/稀释剂流,以形成携带乙烯的低压混合液体进料流; 使用一个或多个高压泵将携带乙烯的低压混合液体进料流加压至聚合系统压力以加入携带乙烯的高压共混反应器进料流; 并将含乙烯的高压共混反应器进料流输送到一个或多个反应器。

    Monomer recycle process for fluid phase in-line blending of polymers
    8.
    发明授权
    Monomer recycle process for fluid phase in-line blending of polymers 有权
    用于流体相在线共混聚合物的单体循环过程

    公开(公告)号:US08080610B2

    公开(公告)日:2011-12-20

    申请号:US12074496

    申请日:2008-03-04

    IPC分类号: C08F2/04 C08F2/06

    摘要: A monomer recycle process for fluid phase in-line blending of polymers is provided. In one form, the monomer recycle process includes providing a first group (G1) of one or more reactor trains and a second group (G2) of one or more reactor trains and one or more separators fluidly connected to G1 and one separator fluidly connected to G2; polymerizing in each reactor train of G1 and G2 olefin monomers to form homogenous fluid phase polymer-monomer mixtures wherein each of the G1 and G2 reactor trains have at least one common monomer; passing the reactor effluents from the one or more G1 reactor trains through the one or more G1 separators to separate a monomer-rich phase from a polymer-enriched phase; passing the polymer-enriched phase and the reactor effluents from the one or more G2 reactor trains into the G2 separator (separator-blender) to separate another monomer-rich phase from a polymer-rich blend; recycling to one or more G1 reactor trains the separated monomer-rich phase from the one or more G1 separators; and recycling to one or more G2 reactor trains the separated monomer-rich phase from the G2 separator. The polymer-rich blend is conveyed to a downstream finishing stage for further monomer stripping, drying and/or pelletizing to form a polymer product blend.

    摘要翻译: 提供了用于聚合物的流体相在线共混的单体再循环方法。 在一种形式中,单体再循环方法包括提供一个或多个反应器列的第一组(G1)和一个或多个反应器列的第二组(G2)和与G1流体连接的一个或多个分离器和一个流体连接到 G2; 在G1和G2烯烃单体的每个反应器序列中聚合以形成均相流体相聚合物 - 单体混合物,其中每个G1和G2反应器列具有至少一个共同的单体; 使来自一个或多个G1反应器列的反应器流出物通过一个或多个G1分离器以将富含单体的相与富集聚合相分离; 将聚合物富集相和反应器流出物从一个或多个G2反应器列车通入G2分离器(分离器 - 共混器)中,以从富含聚合物的共混物中分离另一富含单体的相; 将一个或多个G1反应器再循环到一个或多个G1分离器中,从而分离出富含单体的相。 并循环到一个或多个G2反应器中,从G2分离器中将分离的富含单体的相进行培养。 将富含聚合物的共混物输送到下游整理阶段,以进一步进行单体汽提,干燥和/或造粒以形成聚合物产物混合物。

    Monomer recycle process for fluid phase in-line blending of polymers
    9.
    发明申请
    Monomer recycle process for fluid phase in-line blending of polymers 有权
    用于流体相在线共混聚合物的单体循环过程

    公开(公告)号:US20080281040A1

    公开(公告)日:2008-11-13

    申请号:US12074496

    申请日:2008-03-04

    IPC分类号: C08F2/01

    摘要: A monomer recycle process for fluid phase in-line blending of polymers is provided. In one form, the monomer recycle process includes providing a first group (G1) of one or more reactor trains and a second group (G2) of one or more reactor trains and one or more separators fluidly connected to G1 and one separator fluidly connected to G2; polymerizing in each reactor train of G1 and G2 olefin monomers to form homogenous fluid phase polymer-monomer mixtures wherein each of the G1 and G2 reactor trains have at least one common monomer; passing the reactor effluents from the one or more G1 reactor trains through the one or more G1 separators to separate a monomer-rich phase from a polymer-enriched phase; passing the polymer-enriched phase and the reactor effluents from the one or more G2 reactor trains into the G2 separator (separator-blender) to separate another monomer-rich phase from a polymer-rich blend; recycling to one or more G1 reactor trains the separated monomer-rich phase from the one or more G1 separators; and recycling to one or more G2 reactor trains the separated monomer-rich phase from the G2 separator. The polymer-rich blend is conveyed to a downstream finishing stage for further monomer stripping, drying and/or pelletizing to form a polymer product blend.

    摘要翻译: 提供了用于聚合物的流体相在线共混的单体再循环方法。 在一种形式中,单体再循环方法包括提供一个或多个反应器列的第一组(G1)和一个或多个反应器列的第二组(G2)和与G1流体连接的一个或多个分离器和一个流体连接到 G2; 在G1和G2烯烃单体的每个反应器序列中聚合以形成均相流体相聚合物 - 单体混合物,其中每个G1和G2反应器列具有至少一个共同的单体; 使来自一个或多个G1反应器列的反应器流出物通过一个或多个G1分离器以将富含单体的相与富集聚合相分离; 将聚合物富集相和反应器流出物从一个或多个G2反应器列车通入G2分离器(分离器 - 共混器)中,以从富含聚合物的共混物中分离另一富含单体的相; 将一个或多个G1反应器再循环到一个或多个G1分离器中,从而分离出富含单体的相。 并循环到一个或多个G2反应器中,从G2分离器中将分离的富含单体的相进行培养。 将富含聚合物的共混物输送到下游整理阶段,以进一步进行单体汽提,干燥和/或造粒以形成聚合物产物混合物。