Hydrotreating olefin stream with complete destruction of oxygenates
    5.
    发明授权
    Hydrotreating olefin stream with complete destruction of oxygenates 有权
    加氢处理烯烃流完全破坏含氧化合物

    公开(公告)号:US06548721B1

    公开(公告)日:2003-04-15

    申请号:US09862897

    申请日:2001-05-22

    IPC分类号: C07C502

    摘要: Disclosed is a process for completely destroying oxygenates in a feed stream. The feed stream of oxygenates typically includes olefins and it is reacted with hydrogen over a catalyst comprising a top row of Group VIII metal and a Group VI-B metal. Olefins are essentially completely saturated and any sulfur compounds present in the feed are completely converted to hydrogen sulfide. A preferred catalyst includes 2 to 5 wt-% nickel, 5 to 15 wt-% molybdenum, at least 5.5 wt-% sulfur, less than 0.05 wt-% phosphorus and no more than 0.3 wt-% silicon. The catalyst has low acidity and therefore does not promote the cracking of desired oligomeric products. The deoxygenation process is preferably a saturation process that follows an oligomerization process in which light olefins are oligomerized to heavy olefins. The saturation catalyst preferably has lower acidity which causes minimal cracking of desired oligomeric products. However, by optimally raising the temperature of the outlet of the saturation reaction zone, excessively heavy oligomers can be cracked down to desirable heavy oligomers.

    摘要翻译: 公开了一种在进料流中完全破坏含氧化合物的方法。 含氧化合物的进料流通常包括烯烃,并且其与氢气在包含第一排VIII族金属和VI-B族金属的催化剂上反应。 烯烃基本上完全饱和,并且进料中存在的任何硫化合物完全转化成硫化氢。 优选的催化剂包括2至5重量%的镍,5至15重量%的钼,至少5.5重量%的硫,小于0.05重量%的磷和不超过0.3重量%的硅。 催化剂具有低酸度,因此不促进所需低聚产物的裂化。 脱氧方法优选是在轻烯烃低聚至重质烯烃的低聚方法之后的饱和方法。 饱和催化剂优选具有较低的酸度,这导致所需低聚产物的最小裂化。 然而,通过最佳地提高饱和反应区的出口的温度,过量的低聚物可以被裂化成所需的重低聚物。

    Ni/Cu absorbent/catalyst for desulfurization and isomerization of
n-paraffins
    10.
    发明授权
    Ni/Cu absorbent/catalyst for desulfurization and isomerization of n-paraffins 失效
    用于正链烷烃脱硫和异构化的Ni / Cu吸收剂/催化剂

    公开(公告)号:US4886935A

    公开(公告)日:1989-12-12

    申请号:US238779

    申请日:1988-08-31

    摘要: A hydrocarbon-containing feedstock is desulfurized so as to contain less than 5, and preferably less than 2 ppmw of sulfur, in the first stage of a two-stage process. In the second stage, the feedstock is contacted with an isomerization catalyst useful for promoting n-paraffin isomerization reactions. A dual-function catalyst containing both Group VIII and Group IB metals and effective for simultaneously absorbing sulfur and isomerizing a hydrocarbon feedstock may be employed in the first stage. Alternatively, the dual-function catalyst may be employed in both the first and second stages. Alternatively still, the dual-function catalyst may be used to treat a feedstock containing n-paraffins in a single stage isomerization process.

    摘要翻译: 在两阶段工艺的第一阶段,含烃原料被脱硫以便含有少于5%,优选小于2ppmw的硫。 在第二阶段中,原料与可用于促进正链烷烃异构化反应的异构化催化剂接触。 可以在第一阶段中使用含有VIII族和IB族金属并且有效同时吸收硫和异构化烃原料的双功能催化剂。 或者,双功能催化剂可以用于第一和第二阶段。 或者,双功能催化剂可用于在单级异构化方法中处理含有正链烷烃的原料。