Aromatics processing catalysts
    61.
    再颁专利
    Aromatics processing catalysts 失效
    芳烃加工催化剂

    公开(公告)号:USRE31919E

    公开(公告)日:1985-06-18

    申请号:US526257

    申请日:1983-08-25

    IPC分类号: B01J29/44 B01J29/74

    摘要: A method of preparing aromatics processing catalysts which comprises incorporating a noble metal with a member or members of a useful class of zeolites, with such incorporation occurring after zeolite crystallization, but prior to final catalyst particle formation, i.e. extrusion into particles. Said useful class of zeolites is characterized by a silica to alumina mole ratio of at least 12 and a Constraint Index in the approximate range of 1 to 12.

    Process for syngas conversions to liquid hydrocarbon products utilizing
ZSM-45 zeolite
    62.
    发明授权
    Process for syngas conversions to liquid hydrocarbon products utilizing ZSM-45 zeolite 失效
    使用ZSM-45沸石合成气转化为液态烃产物的方法

    公开(公告)号:US4523047A

    公开(公告)日:1985-06-11

    申请号:US631684

    申请日:1984-07-16

    IPC分类号: C07C1/04 C10G11/05 C07C1/06

    摘要: The liquid carrier in a Fischer-Tropsch synthesis slurry reactor system is periodically or continually separated and subjected to cracking and isomerization in the presence of suitable catalysts. The treated carrier is returned to the reactor system and the accumulation of high viscosity paraffin in the reactor slurry is minimized. Suitable catalysts include a mixture of cracking and isomerization catalysts. Zeolite ZSM-45 is a novel constituent of the catalyst system.

    摘要翻译: 费 - 托合成淤浆反应器系统中的液体载体周期性地或连续地分离,并在合适的催化剂存在下进行裂化和异构化。 经处理的载体返回到反应器系统中,反应器浆料中高粘度石蜡的积聚最小化。 合适的催化剂包括裂化和异构化催化剂的混合物。 沸石ZSM-45是催化剂体系的新成分。

    Process for syngas conversions to liquid hydrocarbon products utilizing
zeolite Beta
    64.
    发明授权
    Process for syngas conversions to liquid hydrocarbon products utilizing zeolite Beta 失效
    使用沸石β的合成气转化为液体烃产物的方法

    公开(公告)号:US4471145A

    公开(公告)日:1984-09-11

    申请号:US536067

    申请日:1983-09-26

    IPC分类号: C07C1/04 C10G11/05 C07C1/06

    摘要: The liquid carrier in a Fischer-Tropsch synthesis slurry reactor system is periodically or continually separated and subjected to cracking and isomerization in the presence of suitable catalysts. The treated carrier is returned to the reactor system and the accumulation of high viscosity paraffin in the reactor slurry is minimized. Suitable catalysts include a mixture of cracking and isomerization catalysts. Zeolite Beta is the novel constituent of the catalyst system.

    摘要翻译: 费 - 托合成淤浆反应器系统中的液体载体周期性地或连续地分离,并在合适的催化剂存在下进行裂化和异构化。 经处理的载体返回到反应器系统中,反应器浆料中高粘度石蜡的积聚最小化。 合适的催化剂包括裂化和异构化催化剂的混合物。 沸石β是催化剂体系的新成分。

    Catalytic cracking
    66.
    发明授权
    Catalytic cracking 失效
    催化裂化

    公开(公告)号:US4416765A

    公开(公告)日:1983-11-22

    申请号:US408109

    申请日:1982-08-16

    摘要: Octane and overall product quality improvement in catalytic cracking processes utilizing an essentially entirely amorphous cracking catalyst can be attained by using instead a catalyst comprising a minor amount, e.g. from about 0.01 to about 25 weight percent, of a class of crystalline zeolites characterized by a silica to alumina mole ratio greater than about 12 and a constraint index of about 1 to 12. The crystalline zeolites may be added to the conventional amorphous cracking catalyst in the cracking process by way of adding a separate additive composition in an amount which provides the zeolite component of the additive composition in said minor amount of the total catalyst in the cracking process.

    摘要翻译: 使用基本上完全无定形裂化催化剂的催化裂化方法的辛烷值和总体产品质量改进可以通过使用代替如下的催化剂来实现: 约0.01至约25重量%的一类结晶沸石,其特征在于二氧化硅与氧化铝的摩尔比大于约12,约束指数为约1至12。结晶沸石可以加入常规无定形裂解催化剂中 通过在裂化过程中以提供添加剂组合物的沸石组分在所述少量总催化剂中的量添加单独的添加剂组合物来进行裂化过程。