Processes for the reduction of alkylation catalyst deactivation utilizing low silica to alumina ratio catalyst
    1.
    发明授权
    Processes for the reduction of alkylation catalyst deactivation utilizing low silica to alumina ratio catalyst 有权
    使用低二氧化硅与氧化铝比的催化剂还原烷基化催化剂失活的方法

    公开(公告)号:US09556083B2

    公开(公告)日:2017-01-31

    申请号:US13212234

    申请日:2011-08-18

    摘要: Alkylation systems and methods of minimizing alkylation catalyst regeneration are described herein. The alkylation systems generally include a preliminary alkylation system adapted to receive an input stream including an alkyl aromatic hydrocarbon and contact the input stream with a preliminary alkylation catalyst disposed therein to form a first output stream. The preliminary alkylation catalyst generally includes a zeolite catalyst having a SiO2/Al2O3 ratio of less than about 25. The alkylation systems further include a first alkylation system adapted to receive the first output stream and contact the first output stream with a first alkylation catalyst disposed therein and an alkylating agent to form a second output stream.

    摘要翻译: 本文描述了使烷基化催化剂再生最小化的烷基化系统和方法。 烷基化系统通常包括适于接收包含烷基芳族烃的输入流并将输入流与设置在其中的预置烷基化催化剂接触以形成第一输出流的初步烷基化系统。 初步烷基化催化剂通常包括SiO 2 / Al 2 O 3比小于约25的沸石催化剂。烷基化系统还包括适于接收第一输出流并将第一输出流与置于其中的第一烷基化催化剂接触的第一烷基化系统 和烷基化剂以形成第二输出流。

    PROCESSES FOR THE REDUCTION OF ALKYLATION CATALYST DEACTIVATION UTILIZING LOW SILICA TO ALUMINA RATIO CATALYST
    2.
    发明申请
    PROCESSES FOR THE REDUCTION OF ALKYLATION CATALYST DEACTIVATION UTILIZING LOW SILICA TO ALUMINA RATIO CATALYST 审中-公开
    降低二氧化硅对氧化铝比催化剂的烷基化催化降解活性的研究进展

    公开(公告)号:US20110301396A1

    公开(公告)日:2011-12-08

    申请号:US13212234

    申请日:2011-08-18

    IPC分类号: C07C2/54

    摘要: Alkylation systems and methods of minimizing alkylation catalyst regeneration are described herein. The alkylation systems generally include a preliminary alkylation system adapted to receive an input stream including an alkyl aromatic hydrocarbon and contact the input stream with a preliminary alkylation catalyst disposed therein to form a first output stream. The preliminary alkylation catalyst generally includes a zeolite catalyst having a SiO2/Al2O3 ratio of less than about 25. The alkylation systems further include a first alkylation system adapted to receive the first output stream and contact the first output stream with a first alkylation catalyst disposed therein and an alkylating agent to form a second output stream.

    摘要翻译: 本文描述了使烷基化催化剂再生最小化的烷基化系统和方法。 烷基化系统通常包括适于接收包含烷基芳族烃的输入流并将输入流与设置在其中的预置烷基化催化剂接触以形成第一输出流的初步烷基化系统。 初步烷基化催化剂通常包括SiO 2 / Al 2 O 3比小于约25的沸石催化剂。烷基化系统还包括适于接收第一输出流并将第一输出流与置于其中的第一烷基化催化剂接触的第一烷基化系统 和烷基化剂以形成第二输出流。

    Processes for reduction of alkylation catalyst deactivation utilizing low silica to alumina ratio catalyst
    3.
    发明申请
    Processes for reduction of alkylation catalyst deactivation utilizing low silica to alumina ratio catalyst 审中-公开
    使用低二氧化硅与氧化铝比的催化剂还原烷基化催化剂失活的方法

    公开(公告)号:US20080058566A1

    公开(公告)日:2008-03-06

    申请号:US11515679

    申请日:2006-09-05

    IPC分类号: B01J8/04 C07C2/64

    摘要: Alkylation systems and methods of minimizing alkylation catalyst regeneration are described herein. The alkylation systems generally include a preliminary alkylation system adapted to receive an input stream including an alkyl aromatic hydrocarbon and contact the input stream with a preliminary alkylation catalyst disposed therein to form a first output stream. The preliminary alkylation catalyst generally includes a zeolite catalyst having a SiO2/Al2O3 ratio of less than about 25. The alkylation systems further include a first alkylation system adapted to receive the first output stream and contact the first output stream with a first alkylation catalyst disposed therein and an alkylating agent to form a second output stream.

    摘要翻译: 本文描述了使烷基化催化剂再生最小化的烷基化系统和方法。 烷基化系统通常包括适于接收包含烷基芳族烃的输入流并将输入流与设置在其中的预置烷基化催化剂接触以形成第一输出流的初步烷基化系统。 初步烷基化催化剂通常包括小于约25的SiO 2 / Al 2 O 3 N 3比的沸石催化剂。进一步的烷基化体系 包括第一烷基化系统,其适于接收第一输出流并且接触第一输出流与其中设置的第一烷基化催化剂和烷基化剂以形成第二输出流。

    Treatment of alkylation catalyst poisons
    4.
    发明申请
    Treatment of alkylation catalyst poisons 审中-公开
    烷基化催化剂毒物的处理

    公开(公告)号:US20060194991A1

    公开(公告)日:2006-08-31

    申请号:US11326666

    申请日:2006-01-07

    IPC分类号: C07C2/00

    CPC分类号: C07C2/66 C07C6/126 C07C15/073

    摘要: Alkylation processes are described herein. The alkylation process generally includes contacting an input stream including benzene with an alkylation catalyst and an alkylating agent to form an alkylation output stream including ethylbenzene. The alkylation process further includes contacting at least a portion of the alkylation output stream with a transalkylation catalyst and a benzene source to form a transalkylation output stream, wherein the benzene source is selected to minimize the amount of alkylation catalyst poisons contacting the alkylation catalyst.

    摘要翻译: 烷基化方法在本文中描述。 烷基化方法通常包括使包含苯的输入流与烷基化催化剂和烷基化剂接触以形成包括乙苯的烷基化输出流。 烷基化方法还包括使烷基化输出流的至少一部分与烷基转移催化剂和苯源接触以形成烷基转移输出流,其中选择苯源以使与烷基化催化剂接触的烷基化催化剂毒物的量最小化。

    Treatment of Alkylation Catalyst Poisons
    7.
    发明申请
    Treatment of Alkylation Catalyst Poisons 审中-公开
    烷基化催化剂毒物的处理

    公开(公告)号:US20090023966A1

    公开(公告)日:2009-01-22

    申请号:US12243377

    申请日:2008-10-01

    IPC分类号: C07C2/00

    CPC分类号: C07C2/66 C07C6/126 C07C15/073

    摘要: Alkylation processes are described herein. The alkylation process generally includes contacting an input stream including benzene with an alkylation catalyst and an alkylating agent to form an alkylation output stream including ethylbenzene. The alkylation process further includes contacting at least a portion of the alkylation output stream with a transalkylation catalyst and a benzene source to form a transalkylation output stream, wherein the benzene source is selected to minimize the amount of alkylation catalyst poisons contacting the alkylation catalyst.

    摘要翻译: 烷基化方法在本文中描述。 烷基化方法通常包括使包含苯的输入流与烷基化催化剂和烷基化剂接触以形成包括乙苯的烷基化输出流。 烷基化方法还包括使烷基化输出流的至少一部分与烷基转移催化剂和苯源接触以形成烷基转移输出流,其中选择苯源以使与烷基化催化剂接触的烷基化催化剂毒物的量最小化。