Secondary alcohol process
    1.
    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

    CPC classification number: C07C9/00

    Abstract: 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.

    Abstract translation: 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 in paraffin oxime production
    2.
    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

    CPC classification number: C07C9/00 Y10S204/903

    Abstract: 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.

    Abstract translation: 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
    3.
    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

    CPC classification number: C07C9/00 C07C7/163

    Abstract: 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.

    Abstract translation: 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。

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