Aromatics processing catalysts
    3.
    发明授权
    Aromatics processing catalysts 失效
    芳烃加工催化剂

    公开(公告)号:US4312790A

    公开(公告)日:1982-01-26

    申请号:US140343

    申请日:1980-04-14

    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.

    摘要翻译: 一种制备芳族化合物加工催化剂的方法,其包括将贵金属与有效类型的沸石的成员或成员结合,其结合发生在沸石结晶之后,但在最终催化剂颗粒形成之前,即挤出成颗粒。 所述有用类别的沸石的特征在于二氧化硅与氧化铝的摩尔比为至少12,约束指数在约1至12的范围内。

    Aromatics processing catalysts
    4.
    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.

    Aromatics processing
    6.
    发明授权
    Aromatics processing 失效
    芳香加工

    公开(公告)号:US4385195A

    公开(公告)日:1983-05-24

    申请号:US296601

    申请日:1981-08-26

    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.

    摘要翻译: 一种制备芳族化合物加工催化剂的方法,其包括将贵金属与有效类型的沸石的成员或成员结合,其结合发生在沸石结晶之后,但在最终催化剂颗粒形成之前,即挤出成颗粒。 所述有用类别的沸石的特征在于二氧化硅与氧化铝的摩尔比为至少12,约束指数在约1至12的范围内。

    Conversion of synthesis gas with iron-containing catalyst
    7.
    发明授权
    Conversion of synthesis gas with iron-containing catalyst 失效
    用含铁催化剂转化合成气

    公开(公告)号:US4293446A

    公开(公告)日:1981-10-06

    申请号:US129551

    申请日:1980-03-12

    IPC分类号: B01J29/46 B01J29/76 B01J29/34

    摘要: A method is disclosed for the conversion of synthesis gas to a liquid hydrocarbon product having a boiling range of less than 400.degree. F. at a 90% overhead utilizing a novel catalyst prepared from a water-insoluble organic iron compound. The novel method involves contacting synthesis gas with a single particle catalyst containing iron, a crystalline acidic aluminosilicate zeolite having a silica-to-alumina ratio of at least 12, a pore size greater than about 5 Angstrom units, and a constraint index of about 1 to 12, and a matrix. The catalyst does not contain promoters.

    摘要翻译: 公开了一种使用由水不溶性有机铁化合物制备的新型催化剂,以90%塔顶转化合成气至沸点范围小于400°F的液体烃产物的方法。 该新方法包括使合成气与含铁的单一颗粒催化剂接触,二氧化硅与氧化铝之比至少为12的结晶酸性硅铝酸盐沸石,孔径大于约5埃单位,约束指数约为1 到12,和矩阵。 催化剂不含助催化剂。

    Conversion of synthesis gas with cobalt-containing fluid catalyst
    8.
    发明授权
    Conversion of synthesis gas with cobalt-containing fluid catalyst 失效
    用含钴流体催化剂转化合成气

    公开(公告)号:US4207248A

    公开(公告)日:1980-06-10

    申请号:US970299

    申请日:1978-12-18

    摘要: A method is disclosed for the conversion of synthesis gas to a liquid hydrocarbon product having a boiling point range maximum of less than 400.degree. F. at a 90% overhead and being a predominantly olefinic product. The novel method involves contacting synthesis gas with a single particle catalyst containing cobalt, a crystalline acidic aluminosilicate zeolite having a silica-to-alumina ratio of at least 12, a pore size greater than about 5 Angstrom units, and a constraint index of about 1 to 12, and a siliceous matrix. The catalyst does not contain promoters and the alumina content of the matrix is severely restricted.

    摘要翻译: 公开了一种在90%塔顶馏分将合成气转化为沸点范围最大小于400°F的液体烃产物并且主要是烯烃产物的方法。 该新方法包括使合成气与含有钴的单一颗粒催化剂接触,二氧化硅与氧化铝之比至少为12的结晶酸性硅铝酸盐沸石,孔径大于约5埃单位,约束指数约为1 至12,和硅质基质。 催化剂不含助催化剂,并且基体的氧化铝含量受到严格限制。