会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 7. 发明申请
    • PROCESS FOR THE PRODUCTION OF XYLENESE AND LIGHT OLEFINS
    • 生产XYLENESE和光油的方法
    • WO2013169463A1
    • 2013-11-14
    • PCT/US2013/037207
    • 2013-04-18
    • EXXONMOBIL CHEMICAL PATENTS INC.
    • IACCINO, Larry, L.DAVIS, Stephen, M.OU, John, D. Y.ZHENG, Xiaobo
    • C10G11/02C10G11/18
    • C10G11/00C10G9/00C10G45/58C10G45/64C10G45/68C10G47/00C10G65/12C10G69/04C10G69/06
    • In a hydrocarbon upgrading process, a hydrocarbon feed is treated in at least one of a steam cracker, catalytic cracker, coker, hydrocracker, and reformer under suitable conditions to produce a first stream comprising olefinic and aromatic hydrocarbons. A second stream composed mainly of C 4 + olefinic and aromatic hydrocarbons is recovered from the first stream and is fed together with a methylating agent to a reaction zone containing a catalyst under reaction conditions including a temperature of about 450°C to about 700°C, such that aromatics components in the second stream undergo dealkylation, trans alkylation and/or methylation and aliphatic components undergo cracking and aromatization to produce a third stream having an increased xylene content compared with said second stream and a C 3 - olefin by-product. The C 3 - olefin by-product is recovered and para- xylene is removed from at least part of said third stream.
    • 在烃改质方法中,在合适条件下,在蒸汽裂化器,催化裂化器,焦化器,加氢裂化器和重整器中的至少一种中处理烃进料以产生包含烯烃和芳族烃的第一流。 主要由C 4 +烯烃和芳烃组成的第二料流从第一料流中回收,并在含有约450℃至约700℃的温度的反应条件下与甲基化剂一起加入含有催化剂的反应区, 第二流中的芳烃组分经历脱烷基化,反式烷基化和/或甲基化,并且脂肪族组分经历裂化和芳构化以产生与所述第二料流和C3-烯烃副产物相比具有增加的二甲苯含量的第三料流。 回收C3-烯烃副产物,并从至少部分所述第三料流中除去对二甲苯。