Reforming/dehydrocyclization catalysts
    5.
    发明授权
    Reforming/dehydrocyclization catalysts 失效
    重整/脱氢环化催化剂

    公开(公告)号:US5098877A

    公开(公告)日:1992-03-24

    申请号:US625273

    申请日:1990-12-10

    IPC分类号: B01J29/85 C10G35/06

    摘要: Reforming and dehydrocyclization catalysts and processes are disclosed wherein reforming catalysts comprise a Group VIII metal and at least one medium pore non-zeolitic molecular sieve characterized in the calcined form by an adsorption of isobutane of at least 2 percent by weight at a partial pressure of 500 torr and a temperature of 20.degree. C. and characterized by an adsorption of triethylamine less than about 5 percent by weight at a partial pressure of 2.6 torr and a temperature of 22.degree. C. In one embodiment the catalyst includes a Group VII metal on a halogenated carrier.

    摘要翻译: 公开了重整和脱氢环化催化剂和方法,其中重整催化剂包含第VIII族金属和至少一种中孔非沸石分子筛,其特征在于煅烧形式,通过在500分压下吸附至少2重量%的异丁烷 托尔,温度为20℃,其特征在于在2.6托的分压和22℃的温度下吸附小于约5重量%的三乙胺。在一个实施方案中,催化剂包括在第 卤化载体。

    Reforming/dehydrocyclization catalysts
    8.
    发明授权
    Reforming/dehydrocyclization catalysts 失效
    重整/脱氢环化催化剂

    公开(公告)号:US5520796A

    公开(公告)日:1996-05-28

    申请号:US305529

    申请日:1994-09-13

    摘要: Reforming is effected with a combination of a primary supported noble-metal catalyst and a catalyst containing one or more medium pore non-zeolite molecular sieves (MP-NZMS). The latter reforming and dehydrocyclization comprise a Group VIII metal and at least one bound MP-NZMS characterized in the calcined form by an adsorption of isobutane of at least 2 percent by weight at a partial pressure of 500 torr and a temperature of 20.degree. C. and characterized by an adsorption of triethylamine less than about 5 percent by weight at a partial pressure of 2.6 torr and a temperature of 22.degree. C., The MP-NZMS catalyst binder preferably is alumina and/or silica, and the Group VIII metal preferably is platinum.

    摘要翻译: 通过主负载的贵金属催化剂和含有一种或多种中孔非沸石分子筛(MP-NZMS)的催化剂的组合进行重整。 后一种重整和脱氢环化包括第VIII族金属和至少一种结合的MP-NZMS,其特征在于煅烧形式,通过在500托的分压和20℃的温度下吸附至少2重量%的异丁烷。 其特征在于在2.6托的分压和22℃的温度下吸附小于约5重量%的三乙胺.MMP-NZMS催化剂粘合剂优选是氧化铝和/或二氧化硅,优选的是Ⅷ族金属 是铂金。

    Reforming/dehydrocyclization catalysts
    9.
    发明授权
    Reforming/dehydrocyclization catalysts 失效
    重整/脱氢环化催化剂

    公开(公告)号:US5346611A

    公开(公告)日:1994-09-13

    申请号:US86961

    申请日:1993-07-02

    IPC分类号: B01J29/85 C10G35/06 C07C2/52

    摘要: Reforming and dehydrocyclization catalysts and processes are disclosed wherein reforming catalysts comprise a Group VIII metal and at least one bound medium pore non-zeolitic molecular sieve characterized in the calcined form by an adsorption of isobutane of at least 2 percent by weight at a partial pressure of 500 torr and a temperature of 20.degree. C. and characterized by an adsorption of triethylamine less than about 5 percent by weight at a partial pressure of 2.6 torr and a temperature of 22.degree. C. The binder preferably is alumina and/or silica, and the Group VIII metal preferably is platinum.

    摘要翻译: 公开了重整和脱氢环化催化剂和方法,其中重整催化剂包含第Ⅷ族金属和至少一种结合的中孔非沸石分子筛,其特征在于煅烧形式的吸附异丁烷为至少2重量%,分压为 500托和温度为20℃,特征在于在2.6托分压和22℃的温度下吸附小于约5重量%的三乙胺。粘合剂优选为氧化铝和/或二氧化硅,和 VIII族金属优选为铂。

    Reforming/dehydrocyclization catalysts
    10.
    发明授权
    Reforming/dehydrocyclization catalysts 失效
    重整/脱氢环化催化剂

    公开(公告)号:US5225071A

    公开(公告)日:1993-07-06

    申请号:US855301

    申请日:1992-03-23

    IPC分类号: B01J29/85 C10G35/06

    摘要: Reforming and dehydrocyclization catalysts and processes are disclosed wherein reforming catalysts comprise a Group VIII metal and at least one medium pore non-zeolitic molecular sieve characterized in the calcined form by an adsorption of isobutane of at least 2 percent by weight at a partial pressure of 500 torr and a temperature of 20.degree. C. and characterized by an adsorption of triethylamine less than about 5 percent by weight at a partial pressure of 2.6 torr and a temperature of 22.degree. C. In one embodiment the catalyst includes a Group VII metal on a halogenated carrier.

    摘要翻译: 公开了重整和脱氢环化催化剂和方法,其中重整催化剂包含第VIII族金属和至少一种中孔非沸石分子筛,其特征在于煅烧形式,通过在500分压下吸附至少2重量%的异丁烷 托尔,温度为20℃,其特征在于在2.6托的分压和22℃的温度下吸附小于约5重量%的三乙胺。在一个实施方案中,催化剂包括在第 卤化载体。