Benzene conversion over ZSM-5
    2.
    发明授权
    Benzene conversion over ZSM-5 失效
    苯转化ZSM-5

    公开(公告)号:US4926000A

    公开(公告)日:1990-05-15

    申请号:US213755

    申请日:1988-06-30

    申请人: Roger A. Morrison

    发明人: Roger A. Morrison

    IPC分类号: C07C2/00

    摘要: Benzene reacts with itself to produce liquid aromatic compounds having more than 6 carbon atoms, in the presence of zeolite characterized as a medium pore size and having an activity defined by an alpha value of at least 50.

    摘要翻译: 在具有中等孔径并且具有由α值至少为50定义的活性的沸石的存在下,苯与其自身反应产生具有多于6个碳原子的液体芳族化合物。

    Catalyst for the production of aromatic compounds
    6.
    发明授权
    Catalyst for the production of aromatic compounds 失效
    催化剂用于生产芳香族化合物

    公开(公告)号:US3953366A

    公开(公告)日:1976-04-27

    申请号:US504573

    申请日:1974-09-09

    申请人: Roger A. Morrison

    发明人: Roger A. Morrison

    摘要: Improvements in the aromatization of hydrocarbons and in the alkylation of aromatic rings effected by contacting appropriate hydrocarbon feed streams with a ZSM-5 type of catalyst at prescribed temperature, pressure and space velocity conditions to convert the feed as required and desired, which improvements go to minimizing the production of polycyclic aromatics, particularly naphthalenes in the process and reducing coking of the catalyst during aromatization and/or alkylation by using as the catalyst a ZSM-5 type of crystalline aluminosilicate zeolite which has rhenium values deposited thereon and therein by ion exchange techniques.

    摘要翻译: 通过在规定的温度,压力和空间速度条件下将合适的烃进料流与ZSM-5型催化剂接触来改进烃的芳构化和芳族化合物的烷基化,以根据需要和期望转化进料,这些改进转化为 在芳构化和/或烷基化过程中使多环芳烃特别是萘的生产最小化,并且通过使用在其上沉积有铼值的离子交换技术的ZSM-5型结晶硅铝酸盐沸石作为催化剂,在芳构化和/或烷基化期间减少催化剂的焦化 。

    Hydrocarbon conversion process
    7.
    发明授权
    Hydrocarbon conversion process 失效
    烃转化过程

    公开(公告)号:US5397457A

    公开(公告)日:1995-03-14

    申请号:US203185

    申请日:1994-02-25

    IPC分类号: C10G47/18

    CPC分类号: C10G47/18

    摘要: A hydrocarbon fraction, preferably in the kerosene boiling range containing a substantial proportion of C.sub.9 + hydrocarbons is contacted with an n-paraffin fraction, such as n-pentane, over a catalyst of acidic functionality, such as Pd/zeolite beta, under conditions of hydrocracking sufficient to convert the feed to lower boiling range materials of high octane number. The n-paraffin cofeed promotes isomerization and suppresses production of n-paraffins.

    摘要翻译: 在氢化裂化条件下,在酸性官能团的催化剂如Pd /沸石β上,将含有大部分C 9+烃的烃馏分优选与正链烷烃馏分如正戊烷接触。 足以将进料转化为高辛烷值的较低沸点材料。 正链烷烃共进料促进异构化并抑制正链烷烃的生产。

    Xylene isomerization
    10.
    发明授权
    Xylene isomerization 失效
    二甲苯异构化

    公开(公告)号:US4236996A

    公开(公告)日:1980-12-02

    申请号:US43395

    申请日:1979-05-25

    IPC分类号: B01J29/40 C07C5/27 C10G35/04

    摘要: Isomerization of xylenes in admixture with ethylbenzene by contact with a zeolite catalyst such as ZSM-5 is improved by use of zeolite which has been steamed at high temperature to reduce activity, the reaction being at a temperature above about 700.degree. F. At these conditions, conversion of ethylbenzene follows a different reaction path which permits high conversion of ethylbenzene to benzene without loss of xylenes of disproportionation.

    摘要翻译: 通过与沸石催化剂如ZSM-5的接触将二甲苯异构化与乙苯混合,通过使用已经在高温下蒸煮以降低活性的沸石,反应在高于约700°F的温度下得到改善。在这些条件下 ,乙苯的转化遵循不同的反应途径,其允许乙苯高效转化为苯而不损失歧化二甲苯。