Process for manufacturing lubricating base oil with high monocycloparaffins and low multicycloparaffins
    2.
    发明申请
    Process for manufacturing lubricating base oil with high monocycloparaffins and low multicycloparaffins 有权
    制造具有高单环烷烃和低多环烷烃的润滑油基油的方法

    公开(公告)号:US20050133409A1

    公开(公告)日:2005-06-23

    申请号:US10744870

    申请日:2003-12-23

    IPC分类号: C10G45/64 C10G73/38

    摘要: A process for manufacturing a lubricating base oil by: a) performing Fischer-Tropsch synthesis on syngas to provide a product stream; b) isolating from said product stream a substantially paraffinic wax feed having less than about 30 ppm total nitrogen and sulfur, and less than about 1 wt % oxygen; c) dewaxing said feed by hydroisomerization dewaxing using a shape selective intermediate pore size molecular sieve comprising a noble metal hydrogenation component, wherein the hydroisomerization temperature is between about 600° F. (315° C.) and about 750° F. (399° C.), to produce an is dimerized oil; and d) hydrofinishing said isomerized oil to produce a lubricating base oil having specific desired properties.

    摘要翻译: 一种制造润滑油基础油的方法,该方法是:a)在合成气上进行费 - 托合成以提供产物流; b)从所述产物流中分离具有小于约30ppm总氮和硫以及小于约1重量%氧的基本上石蜡的蜡进料; c)使用包含贵金属氢化组分的形状选择性中孔分子筛通过加氢异构化脱蜡来脱蜡所述进料,其中加氢异构化温度在约600°F(315℃)至约750°F(399° C.),以产生二聚油; 和d)加氢精制所述异构化油以产生具有特定所需性能的润滑基础油。

    Process for reducing the pour point and viscosity of fischer-tropsch wax
    5.
    发明申请
    Process for reducing the pour point and viscosity of fischer-tropsch wax 审中-公开
    降低费 - 托蜡的倾点和粘度的方法

    公开(公告)号:US20050131082A1

    公开(公告)日:2005-06-16

    申请号:US10735431

    申请日:2003-12-12

    CPC分类号: C10G9/00 C10G2/32 C10G57/00

    摘要: An integrated process for lowering the pour point of Fischer-Tropsch derived wax which comprises (a) collecting separately from a Fischer-Tropsch unit a Fischer-Tropsch wax and a Fischer-Tropsch condensate; (b) pyrolyzing the Fischer-Tropsch wax in a thermal cracking zone under thermal cracking conditions pre-selected to achieve a cracking conversion of the paraffins molecules present in the Fischer-Tropsch wax of at least 10 percent; (c) recovering from the thermal cracking zone a low pour point Fischer-Tropsch derived wax and a Fischer-Tropsch derived overhead product; and (d) mixing at least a portion of the Fischer-Tropsch derived overhead product recovered in step (c) and at least a portion of the Fischer-Tropsch condensate collected in step (a) with at least a portion of the low pour point Fischer-Tropsch derived wax in the proper proportion to produce a Fischer-Tropsch derived waxy product having a pour point equal to or below about 40 degrees C.

    摘要翻译: 一种用于降低费 - 托衍生蜡的倾点的综合方法,其包括(a)从费 - 托单元分别收集费 - 托蜡和费 - 托冷凝物; (b)在预先选择的热裂解条件下在热裂解区中热解费 - 托蜡以实现费 - 托蜡中存在的链烷烃分子的至少10%的裂化转化; (c)从热裂解区回收低倾点费 - 托衍生的蜡和费 - 托衍生的塔顶产物; 和(d)将步骤(c)中回收的费 - 托衍生的塔顶馏出物的至少一部分与步骤(a)中收集的费 - 托冷凝物的至少一部分混合至少部分低倾点 费托衍生的蜡以合适的比例产生具有等于或低于约40℃的倾点的费 - 托衍生的蜡质产物。

    Production of high quality lubricant bright stock
    6.
    发明申请
    Production of high quality lubricant bright stock 审中-公开
    生产高品质润滑油光亮股

    公开(公告)号:US20050051463A1

    公开(公告)日:2005-03-10

    申请号:US10659012

    申请日:2003-09-09

    IPC分类号: C10G65/12

    摘要: A process for producing a lubricant bright stock from a very heavy feed obtained from a petroleum crude is disclosed. The bright stock produced by the present process has a reduced cloud point and better oxidation stability relative to bright stocks prepared by conventional methods. The process comprises the steps of providing a petroleum residuum-derived stream; separating the residuum-derived stream at a distillation cut point in the range of 1150° F. to 1300° F., into a heavy fraction and at least one light fraction; hydrocracking the at least one light fraction under conditions to reduce the concentration of sulfur and nitrogen to suitable levels for hydroisomerization dewaxing; and dewaxing at least a portion of the hydrocracked stream under hydroisomerization conditions to produce a lubricant bright stock.

    摘要翻译: 公开了从由石油原油获得的非常重的原料生产润滑剂光亮原料的方法。 本方法生产的光亮料相对于通过常规方法制备的光亮油墨具有降低的浊点和更好的氧化稳定性。 该方法包括以下步骤:提供来自石油残渣的流; 将在1150°F至1300°F范围内的蒸馏切割点的残渣衍生物流分离成重馏分和至少一种轻馏分; 在将硫和氮的浓度降低到加氢异构化脱蜡的合适水平的条件下加氢裂化至少一种轻馏分; 并在加氢异构化条件下将至少一部分加氢裂化物流脱蜡以产生润滑剂光亮原料。