NAPHTHALENE ALKYLATION PROCESS USING MIXED H/NH3 FORM CATALYST
    1.
    发明公开
    NAPHTHALENE ALKYLATION PROCESS USING MIXED H/NH3 FORM CATALYST 失效
    混合H / NH3型催化剂的萘烷化工艺

    公开(公告)号:EP0737175A1

    公开(公告)日:1996-10-16

    申请号:EP95906670.0

    申请日:1994-12-19

    IPC分类号: C07C2 B01J29 B01J37 C07B61 C07C15

    摘要: Long chain alkyl substituted naphthalenes are produced by alkylating naphthalene with an olefin or other alkylating agent with at least 6, and usually 12 to 20 carbon atoms, in the presence of an alkylation catalyst comprising a zeolite having both ammonium and protonic species associated with the exchangeable sites of the zeolite. The zeolite is usually a large pore size zeolite such as USY. The presence of both ammonium and protonic species increases selectivity for production of long chain mono-alkyl substituted naphthalenes in preference to more highly substituted products.

    摘要翻译: 长链烷基取代的萘是通过用含至少6个,通常12〜20个碳原子的烯烃或其它烷基化试剂将萘烷基化而制得的,所述烷基化催化剂包含与交换剂相关的具有铵和质子物质的沸石 沸石的位置。 沸石通常是大孔径沸石,如USY。 与更高度取代的产物相比,铵和质子物质两者的存在都提高了生产长链单烷基取代的萘的选择性。

    NAPHTHALENE ALKYLATION PROCESS USING H/NH3 FORM USY ZEOLITE CATALYST
    4.
    发明授权
    NAPHTHALENE ALKYLATION PROCESS USING H/NH3 FORM USY ZEOLITE CATALYST 失效
    用H / NH3型沸石催化剂催化萘烷化反应

    公开(公告)号:EP0737175B1

    公开(公告)日:2001-03-14

    申请号:EP95906670.5

    申请日:1994-12-19

    摘要: Long chain alkyl substituted naphthalenes are produced by alkylating naphthalene with an olefin or other alkylating agent with at least 6, and usually 12 to 20 carbon atoms, in the presence of an alkylation catalyst comprising a zeolite having both ammonium and protonic species associated with the exchangeable sites of the zeolite. The zeolite is usually a large pore size zeolite such as USY. The presence of both ammonium and protonic species increases selectivity for production of long chain mono-alkyl substituted naphthalenes in preference to more highly substituted products.

    摘要翻译: 长链烷基取代的萘是通过用含至少6个,通常12〜20个碳原子的烯烃或其它烷基化试剂将萘烷基化而制得的,所述烷基化催化剂包含与交换剂相关的具有铵和质子物质的沸石 沸石的位置。 沸石通常是大孔径沸石,如USY。 与更高度取代的产物相比,铵和质子物质两者的存在都提高了生产长链单烷基取代的萘的选择性。

    CATALYTIC CONVERSION WITH MCM-58
    6.
    发明公开
    CATALYTIC CONVERSION WITH MCM-58 失效
    催化转化与MCM-58

    公开(公告)号:EP0823936A1

    公开(公告)日:1998-02-18

    申请号:EP96912807.0

    申请日:1996-04-15

    IPC分类号: C10G11 B01J29

    摘要: A process is provided for converting feedstock hydrocarbon compounds to product hydrocarbon compounds having a lower molecular weight than feedstock hydrocarbon compounds over a catalyst composition which comprises MCM-58 or a mixture of MCM-58 and another, e.g., intermediate- or large-pore, molecular sieve component. An embodiment of the present invention comprises an improved catalytic cracking process to produce high octane gasoline and lower molecular weight olefins, e.g. propylene.

    摘要翻译: 提供了一种用于将原料烃化合物转化成具有比原料烃化合物低的分子量的产物烃化合物的方法,所述催化剂组合物包含MCM-58或MCM-58与另一种例如中孔或大孔的混合物, 分子筛组分。 本发明的一个实施方案包括改进的催化裂化工艺以生产高辛烷值汽油和低分子量烯烃, 丙烯。