Hydrocarbon upgrading process
    1.
    发明授权
    Hydrocarbon upgrading process 失效
    碳氢化合物升级过程

    公开(公告)号:US4042490A

    公开(公告)日:1977-08-16

    申请号:US428638

    申请日:1973-12-26

    摘要: A process for converting mixtures of C.sub.6 to C.sub.30 n-paraffin and n-paraffin by-products to substantially pure n-paraffin which comprises catalytically hydrogenating the mixture at a temperature of from about 600.degree. to 750.degree. F. in the presence of a Group VIII metal on alumina catalyst where the catalyst contains from about 0.05 to 2.0 weight percent of an alkali metal oxide or alkaline earth metal oxide or thallous oxide. The catalyst can additionally contain a Group VIB or VIIB metal.

    摘要翻译: 将C6至C30正链烷烃和正链烷烃副产物的混合物转化为基本上纯的正链烷烃的方法,该方法包括在组合存在下在约600至750°F的温度下催化氢化混合物 Ⅷ金属在氧化铝催化剂上,其中催化剂含有约0.05至2.0重量%的碱金属氧化物或碱土金属氧化物或氧化铊。 催化剂还可以含有VIB族或VIIB族金属。

    Secondary alcohol process
    2.
    发明授权
    Secondary alcohol process 失效
    二级酒精过程

    公开(公告)号:US3966828A

    公开(公告)日:1976-06-29

    申请号:US532352

    申请日:1974-12-13

    IPC分类号: C07C9/00 C07C29/52 C07C29/12

    CPC分类号: C07C9/00

    摘要: A process for converting mixtures of C.sub.6 to C.sub.30 n-paraffin and n-paraffin by-products to substantially pure n-paraffin which comprises catalytically hydrogenating the mixture at a temperature of from about 600.degree. to 750.degree.F. in the presence of a Group VIII metal on alumina catalyst, and from about 10 to 5,000 parts per million of nitrogen present as ammonia or an organonitrogen compound. The catalyst can additionally contain a Group VIB or VIIB metal.

    摘要翻译: 将C6至C30正链烷烃和正链烷烃副产物的混合物转化为基本上纯的正链烷烃的方法,该方法包括在组合存在下在约600至750°F的温度下催化氢化混合物 VIII金属,氧化铝催化剂上的金属,以及作为氨或有机氮化合物存在的约10至5,000ppm的氮。 催化剂还可以含有VIB族或VIIB族金属。

    Process for producing secondary alkyl primary amines from n-paraffin
    4.
    发明授权
    Process for producing secondary alkyl primary amines from n-paraffin 失效
    从正链烷烃制备仲烷基伯胺的方法

    公开(公告)号:US4025561A

    公开(公告)日:1977-05-24

    申请号:US652582

    申请日:1976-01-26

    摘要: A process for converting mixtures of C.sub.6 to C.sub.30 n-paraffin and n-paraffin by-products to substantially pure n-paraffin which comprises catalytically hydrogenating the mixture at a temperature of from about 600.degree. to 750.degree. F. in the presence of a Group VIII metal on alumina catalyst where the catalyst contains from about 0.05 to 2.0 weight percent of an alkali metal oxide or alkaline earth metal oxide or thallous oxide. The catalyst can additionally contain a Group VIB or VIIB metal.

    摘要翻译: 将C6至C30正链烷烃和正链烷烃副产物的混合物转化为基本上纯的正链烷烃的方法,该方法包括在组合存在下在约600至750°F的温度下催化氢化混合物 Ⅷ金属在氧化铝催化剂上,其中催化剂含有约0.05至2.0重量%的碱金属氧化物或碱土金属氧化物或氧化铊。 催化剂还可以含有VIB族或VIIB族金属。

    Method of producing n-paraffin oximes
    6.
    发明授权
    Method of producing n-paraffin oximes 失效
    生产正链烷肟的方法

    公开(公告)号:US3993554A

    公开(公告)日:1976-11-23

    申请号:US652585

    申请日:1976-01-26

    摘要: A process for converting mixtures of C.sub.6 to C.sub.30 n-paraffin and n-paraffin by-products to substantially pure n-paraffin which comprises catalytically hydrogenating the mixture at a temperature of from about 600.degree. to 750.degree. F. in the presence of a Group VIII metal on alumina catalyst where the catalyst contains from about 0.05 to 2.0 weight percent of an alkali metal oxide or alkaline earth metal oxide or thallous oxide. The catalyst can additionally contain a Group VIB or VIIB metal. The n-paraffin is photochemically reacted with a gaseous nitrosating agent to form paraffin oximes and by-products and the by-products are recycled for catalytic hydrogenation.

    摘要翻译: 将C6至C30正链烷烃和正链烷烃副产物的混合物转化为基本上纯的正链烷烃的方法,该方法包括在组合存在下在约600至750°F的温度下催化氢化混合物 Ⅷ金属在氧化铝催化剂上,其中催化剂含有约0.05至2.0重量%的碱金属氧化物或碱土金属氧化物或氧化铊。 催化剂还可以含有VIB族或VIIB族金属。 将正链烷烃与气态亚硝化剂光化学反应以形成链烷烃肟和副产物,副产物被再循环用于催化氢化。

    Hydrocarbon upgrading process in paraffin oxime production
    7.
    发明授权
    Hydrocarbon upgrading process in paraffin oxime production 失效
    石蜡肟生产中的烃改质工艺

    公开(公告)号:US3956090A

    公开(公告)日:1976-05-11

    申请号:US532353

    申请日:1974-12-13

    IPC分类号: C07C9/00 B01J1/10

    CPC分类号: C07C9/00 Y10S204/903

    摘要: A process for converting mixtures of C.sub.6 to C.sub.30 n-paraffin and n-paraffin by-products to substantially pure n-paraffin which comprises catalytically hydrogenating the mixture at a temperature of from about 600.degree. to 750.degree.F. in the presence of a Group VIII metal on alumina catalyst, and from about 10 to 5,000 parts per million of nitrogen present as ammonia or an organonitrogen compound. The catalyst can additionally contain a Group VIB or VIIB metal.

    摘要翻译: 将C6至C30正链烷烃和正链烷烃副产物的混合物转化为基本上纯的正链烷烃的方法,该方法包括在组合存在下在约600至750°F的温度下催化氢化混合物 VIII金属,氧化铝催化剂上的金属,以及作为氨或有机氮化合物存在的约10至5,000ppm的氮。 催化剂还可以含有VIB族或VIIB族金属。

    Hydrocarbon upgrading process
    8.
    发明授权
    Hydrocarbon upgrading process 失效
    碳氢化合物升级过程

    公开(公告)号:US3949012A

    公开(公告)日:1976-04-06

    申请号:US428508

    申请日:1973-12-26

    IPC分类号: C07C7/163 C07C9/00 C07C5/02

    CPC分类号: C07C9/00 C07C7/163

    摘要: A process for converting mixtures of C.sub.6 to C.sub.30 n-paraffin and n-paraffin by-products to substantially pure n-paraffin which comprises catalytically hydrogenating the mixture at a temperature of from about 600.degree. to 750.degree.F. in the presence of a Group VIII metal on alumina catalyst, and from about 10 to 5,000 parts per million of nitrogen present as ammonia or an organonitrogen compound. The catalyst can additionally contain a Group VIB or VIIB metal.

    摘要翻译: 将C6至C30正链烷烃和正链烷烃副产物的混合物转化为基本上纯的正链烷烃的方法,该方法包括在组合存在下在约600至750°F的温度下催化氢化混合物 VIII金属,氧化铝催化剂上的金属,以及作为氨或有机氮化合物存在的约10至5,000ppm的氮。 催化剂还可以含有VIB族或VIIB族金属。