Process for producing para-xylene
    3.
    发明授权
    Process for producing para-xylene 失效
    生产对二甲苯的方法

    公开(公告)号:US07683233B2

    公开(公告)日:2010-03-23

    申请号:US11894187

    申请日:2007-08-20

    IPC分类号: C07C7/13

    CPC分类号: C07C7/13 C07C15/08

    摘要: In a process for producing a para-xylene enriched product from a gaseous mixture comprising at least para-xylene, meta-xylene and ortho-xylene, the gaseous mixture is contacted with an adsorbent capable of selectively adsorbing para-xylene and comprising a crystalline molecular sieve having an average crystal size between about 0.5 micron and about 20 microns. The contacting is conducted at a temperature and pressure such that at least part of the para-xylene in the mixture is adsorbed by the adsorbent to produce a para-xylene-depleted effluent stream. The para-xylene is then desorbed from said adsorbent and collected to form a para-xylene enriched stream. The adsorption and desorption steps are repeated for a plurality of cycles, such that the time between successive contacting steps is no more than 10 seconds.

    摘要翻译: 在从至少包含对二甲苯,间二甲苯和邻二甲苯的气体混合物生产对二甲苯富集产物的方法中,气态混合物与能够选择性吸附对二甲苯并且包含结晶分子 平均晶体尺寸在约0.5微米至约20微米之间的筛子。 接触在温度和压力下进行,使得混合物中的至少部分对二甲苯被吸附剂吸附,以产生对二甲苯贫乏的流出物流。 然后将对二甲苯从所述吸附剂中解吸并收集以形成对二甲苯富集流。 吸附和解吸步骤重复多个循环,使得连续接触步骤之间的时间不超过10秒。

    Process for producing para-xylene
    4.
    发明申请
    Process for producing para-xylene 失效
    生产对二甲苯的方法

    公开(公告)号:US20080071126A1

    公开(公告)日:2008-03-20

    申请号:US11894187

    申请日:2007-08-20

    IPC分类号: C07C15/08

    CPC分类号: C07C7/13 C07C15/08

    摘要: In a process for producing a para-xylene enriched product from a gaseous mixture comprising at least para-xylene, meta-xylene and ortho-xylene, the gaseous mixture is contacted with an adsorbent capable of selectively adsorbing para-xylene and comprising a crystalline molecular sieve having an average crystal size between about 0.5 micron and about 20 microns. The contacting is conducted at a temperature and pressure such that at least part of the para-xylene in the mixture is adsorbed by the adsorbent to produce a para-xylene-depleted effluent stream. The para-xylene is then desorbed from said adsorbent and collected to form a para-xylene enriched stream. The adsorption and desorption steps are repeated for a plurality of cycles, such that the time between successive contacting steps is no more than 10 seconds.

    摘要翻译: 在从至少包含对二甲苯,间二甲苯和邻二甲苯的气体混合物生产对二甲苯富集产物的方法中,气态混合物与能够选择性吸附对二甲苯并且包含结晶分子 平均晶体尺寸在约0.5微米至约20微米之间的筛子。 接触在温度和压力下进行,使得混合物中的至少部分对二甲苯被吸附剂吸附,以产生对二甲苯贫乏的流出物流。 然后将对二甲苯从所述吸附剂中解吸并收集以形成对二甲苯富集流。 吸附和解吸步骤重复多个循环,使得连续接触步骤之间的时间不超过10秒。

    Hydrotreating process with improved hydrogen management
    8.
    发明授权
    Hydrotreating process with improved hydrogen management 有权
    加氢处理工艺改善了氢气管理

    公开(公告)号:US08518244B2

    公开(公告)日:2013-08-27

    申请号:US11795547

    申请日:2006-01-23

    IPC分类号: C10G45/02

    CPC分类号: C10G45/04

    摘要: This invention relates to an improved hydrotreating process for removing sulfur from naphtha and distillate feedstreams. This improved process utilizes a hydrotreating zone, an acid gas removal zone, and a pressure swing adsorption zone having a total cycle time of less than about 30 seconds for increasing the concentration of hydrogen utilized in the process.

    摘要翻译: 本发明涉及用于从石脑油和馏出物进料流中除去硫的改进的加氢处理方法。 该改进的方法利用加氢处理区,酸性气体去除区和总循环时间小于约30秒的变压吸附区,以增加在该方法中使用的氢的浓度。

    HYDROTREATING PROCESS WITH IMPROVED HYDROGEN MANAGEMENT
    10.
    发明申请
    HYDROTREATING PROCESS WITH IMPROVED HYDROGEN MANAGEMENT 有权
    具有改进氢气管理的加氢过程

    公开(公告)号:US20100108571A1

    公开(公告)日:2010-05-06

    申请号:US11795547

    申请日:2006-01-23

    IPC分类号: C10G45/04

    CPC分类号: C10G45/04

    摘要: This invention relates to an improved hydrotreating process for removing sulfur from naphtha and distillate feedstreams. This improved process utilizes a hydrotreating zone, an acid gas removal zone, and a pressure swing adsorption zone having a total cycle time of less than about 30 seconds for increasing the concentration of hydrogen utilized in the process.

    摘要翻译: 本发明涉及用于从石脑油和馏出物进料流中除去硫的改进的加氢处理方法。 该改进的方法利用加氢处理区,酸性气体去除区和总循环时间小于约30秒的变压吸附区,以增加在该方法中使用的氢的浓度。