Process for catalytic hydrotreatment of heavy hydrocarbons, in fixed or
moving bed, with injection of a metal compound into the charge
    5.
    发明授权
    Process for catalytic hydrotreatment of heavy hydrocarbons, in fixed or moving bed, with injection of a metal compound into the charge 失效
    催化加氢处理重质烃,固定或移动床的方法,将金属化合物注入电荷

    公开(公告)号:US4655905A

    公开(公告)日:1987-04-07

    申请号:US791002

    申请日:1985-10-24

    CPC分类号: C10G49/02 C10G49/00

    摘要: The invention relates to a process for catalytic treatment of heavy hydrocarbons, in a fixed or moving bed, over a catalyst containing an alumina carrier and at least one catalytic metal or compound of metal from groups VB, VI B and VIII of the periodic classification of elements, characterized by the direct injection into the charge, continuously or periodically, of at least one metal compound selected from the group consisting of halides, oxyhalides, oxides, polyacids and polyacid salts of metals from groups VI B, VII B and VIII, before introducing the charge into the hydrotreatment zone.

    摘要翻译: 本发明涉及一种在固定或移动床中催化处理重质烃的方法,该催化剂含有氧化铝载体和至少一种催化金属或金属的化合物,所述催化剂金属或金属化合物来自第VB,VIB和VIII族的定期分类 元素,其特征在于,连续或周期地直接注入选自VIB,VIIB和VIII族的金属的卤化物,卤氧化物,氧化物,多元酸和多酸盐中的至少一种金属化合物,之前 将电荷引入加氢处理区。

    Catalysts for catalytic hydroreforming or for producing aromatic
hydrocarbons
    9.
    发明授权
    Catalysts for catalytic hydroreforming or for producing aromatic hydrocarbons 失效
    用于催化加氢成型或生产芳烃的催化剂

    公开(公告)号:US4239652A

    公开(公告)日:1980-12-16

    申请号:US53156

    申请日:1979-06-29

    摘要: Catalyst for a process of hydroreforming or aromatic hydrocarbon production, comprising an alumina carrier, at least one noble metal of the platinum family, antimony, a metal selected from gallium, indium and thallium and halogen, said catalyst being used in a series of successive reaction zones as a moving bed, transferred from one reaction zone to the next, from the last reaction zone to a regeneration zone and from the latter to the first reaction zone, said process being preferably conducted at a temperature from 510.degree. to 600.degree. C. and under a pressure from 1 to 18 kg/cm.sup.2.

    摘要翻译: 用于加氢精制或芳烃生产方法的催化剂,包括氧化铝载体,至少一种铂族贵金属,锑,选自镓,铟和铊和卤素的金属,所述催化剂用于一系列连续反应 作为移动床的区域,从一个反应区转移到下一个反应区,从最后一个反应区转移到再生区,从后一个反应区转移到第一个反应区,所述方法优选在510-600℃的温度下进行。 并在1至18kg / cm2的压力下进行。