Process for producing, jointly or otherwise, monoalkyl aromatic compounds, dialkyl aromatic compounds and trialkyl aromatic compounds
    1.
    发明授权
    Process for producing, jointly or otherwise, monoalkyl aromatic compounds, dialkyl aromatic compounds and trialkyl aromatic compounds 有权
    单烷基芳族化合物,二烷基芳族化合物和三烷基芳族化合物共同或以其他方式生产的方法

    公开(公告)号:US06627781B1

    公开(公告)日:2003-09-30

    申请号:US09671295

    申请日:2000-09-27

    IPC分类号: C07C264

    摘要: Process for the production of at least one compound that is selected from among monoalkyl aromatic compounds, dialkyl aromatic compounds and trialkyl aromatic compounds by alkylation or transalkylation of an aromatic compound by at least one alkylating agent that is selected from among the olefins, whereby the process is characterized in that it is carried out in one or two stages, involving two reaction zones in series, whereby one of these two zones can be switched off so as to be able, depending on whether or not one of the zones is switched off, to meet the demand either of the three types of mono, di- and trialkyl aromatic compounds, or two of these types or a single one of the types of mono- or di- or trialkyl aromatic compounds.

    摘要翻译: 通过至少一种选自烯烃的烷基化剂烷基化或烷基化芳族化合物来生产至少一种选自单烷基芳族化合物,二烷基芳族化合物和三烷基芳族化合物的化合物的方法,其中该方法 其特征在于它在一个或两个阶段中进行,包括串联的两个反应区域,由此可以关闭这两个区域中的一个,以便能够根据其中一个区域是否关闭, 以满足三种类型的单,二和三烷基芳族化合物或这些类型中的两种或单 - 或二 - 或三烷基芳族化合物的单一类型的需求。

    Process for producing oils with a high viscosity index
    2.
    发明授权
    Process for producing oils with a high viscosity index 失效
    生产具有高粘度指数的油的方法

    公开(公告)号:US06783661B1

    公开(公告)日:2004-08-31

    申请号:US09644605

    申请日:2000-08-24

    IPC分类号: C01G4702

    CPC分类号: C10G67/02

    摘要: A process for producing oils with high viscosity indices from oil distillates or effluents from a conversion unit comprises the following steps: a) catalytic hydrotreatment of the feed in the presence of hydrogen and a non zeolitic catalyst; b) fractionation of at least a portion of the effluent from step a) or step d) described below to an oil residue; c) fractionation by thermal diffusion of at least a portion of the oil residue obtained from step b) into oil fractions with different compositions and viscosity indices. Step b) can be preceded by a step d) for hydrocracking the effluent obtained from step a) in the presence of hydrogen and a zeolitic catalyst.

    摘要翻译: 用于生产来自转化单元的油馏出物或流出物的具有高粘度指数的油的方法包括以下步骤:a)在氢气和非沸石催化剂存在下催化加氢处理进料; b)将至少一部分 来自下述步骤a)或步骤d)的流出物至油残余物; c)通过将从步骤b)获得的至少一部分油残余物的热扩散分馏成具有不同组成和粘度指数的油馏分。步骤b) 可以在步骤d)之前,在氢气和沸石催化剂的存在下加氢裂化从步骤a)获得的流出物。

    Synthetic oil with a high viscosity number and a low pour point
    3.
    发明授权
    Synthetic oil with a high viscosity number and a low pour point 有权
    具有高粘度数和低倾点的合成油

    公开(公告)号:US06491809B1

    公开(公告)日:2002-12-10

    申请号:US09671294

    申请日:2000-09-27

    IPC分类号: C10M10506

    CPC分类号: C10M105/02 C10M105/06

    摘要: Synthetic oil that contains wholly or partly of dialkylbenzenes and/or partially or totally hydrogenated dialkylbenzenes. The synthetic oil according to the invention can also be used as an oil base or oil base additive and comprises at least one dialkylbenzene and/or at least one partially or totally hydrogenated dialkylbenzene and meets the general chemical formula: R1—A—R2 in which R1 and R2 represent alkyl groups and A is a benzene core and/or a cyclohexane core and/or a cyclohexene core and/or a cyclohexadiene core and is characterized in that it contains between 1 and 20% by weight or ortho isomers and in that at least one of the alkyl groups is attached for the most part to group A by carbon 2 of the aliphatic chain. The two alkyl groups are preferably attached for the most part to group A by carbon 2 of the aliphatic chain.

    摘要翻译: 含有全部或部分二烷基苯和/或部分或完全氢化的二烷基苯的合成油。 根据本发明的合成油还可以用作油基或油基添加剂,并且包含至少一种二烷基苯和/或至少一种部分或全部氢化的二烷基苯,并且满足以下通式:其中R 1和R 2表示烷基 基团和A是苯核心和/或环己烷核心和/或环己烯核心和/或环己二烯核心,其特征在于其含有1至20重量%或邻位异构体,并且其中至少一个 烷基通过脂族链的碳2大部分连接到基团A上。 两个烷基优选通过脂族链的碳2连接到大部分为基团A。

    NU-85 zeolite catalyst and a process for improving the pour point of
feeds containing paraffins
    7.
    发明授权
    NU-85 zeolite catalyst and a process for improving the pour point of feeds containing paraffins 失效
    NU-85沸石催化剂和改善含有链烷烃的进料的倾点的方法

    公开(公告)号:US6153548A

    公开(公告)日:2000-11-28

    申请号:US104362

    申请日:1998-06-25

    摘要: The invention concerns a process for improving the pour point of a feed comprising paraffins containing more than 10 carbon atoms, in which process the feed to be treated is brought into contact with a catalyst comprising NU-85 zeolite and at least one hydro-dehydrogenating element, at a temperature which is in the range 170.degree. C. to 500.degree. C., a pressure in the range 1 to 250 bar and an hourly space velocity in the range 0.05 to 100 h.sup.-1, in the presence of hydrogen in a proportion of 50 to 2000 l/l of feed. The oils obtained have good pour points and high viscosity indices (VI). The process is also applicable to gas oils and other feeds requiring a reduction of pour point. The invention also concerns a NU-85 zeolite from which a portion of elements T (Al, Ga, Fe or B) have been removed and which has an Si/T atomic ratio of at least 18.

    摘要翻译: 本发明涉及改进含有多于10个碳原子的链烷烃的进料的倾点的方法,在该方法中待处理的进料与包含NU-85沸石和至少一种氢脱氢元素的催化剂接触 在170〜500℃的范围内,在1〜250巴的范围内的压力和0.05〜100h -1的小时空间速度,在 比例为50〜2000 l / l的饲料。 所得油具有良好的倾点和高粘度指数(VI)。 该方法也适用于需要降低倾点的瓦斯油和其他进料。 本发明还涉及一种NU-85沸石,其中元素T(Al,Ga,Fe或B)的一部分已被除去,并且Si / T原子比至少为18。

    Catalyst based on modified NU-87 zeolite and a process for improving the
pour point of feeds containing paraffins
    8.
    发明授权
    Catalyst based on modified NU-87 zeolite and a process for improving the pour point of feeds containing paraffins 失效
    基于改性NU-87沸石的催化剂和改善含有链烷烃的进料的倾点的方法

    公开(公告)号:US6036846A

    公开(公告)日:2000-03-14

    申请号:US103522

    申请日:1998-06-24

    IPC分类号: B01J29/70 C10G45/64 C10G47/02

    摘要: The invention concerns a process for improving the pour point of a feed comprising paraffins containing more than 10 carbon atoms, in which process the feed to be treated is brought into contact with a catalyst comprising an NU-87 zeolite comprising silicon and at least one clement T selected from the group formed by Al, Fe, Ga and B, from which at least a portion of clement T has been removed, and having a global Si/T ratio of over 20, the catalyst also containing at least one hydro-dehydrogenating element. The process is carried out at a temperature which is in the range 170.degree. C. to 500.degree. C., a pressure in the range 1 to 250 bar and at an hourly space velocity in the range 0.05 to 100 h.sup.-1, in the presence of hydrogen in a proportion of 50 to 2000 l/l of feed. The oils obtained have good pour points and high viscosity indices (VI). The process is also applicable to gas oils and other feeds requiring a reduction of pour point. The catalyst is also claimed.

    摘要翻译: 本发明涉及改进含有多于10个碳原子的链烷烃的进料的倾点的方法,在该方法中,待处理的进料与包含含有硅的NU-87沸石和至少一种烯键的催化剂接触 T选自由Al,Fe,Ga和B形成的基团,其中至少一部分化合物T已被除去,并且具有超过20的全局Si / T比,催化剂还含有至少一种加氢脱氢 元件。 该方法在170℃至500℃的温度,1至250巴的压力和0.05至100小时-1的小时空间速度下进行,在 以50至2000升/升饲料的比例存在氢气。 所得油具有良好的倾点和高粘度指数(VI)。 该方法也适用于需要降低倾点的瓦斯油和其他进料。 还要求催化剂。

    Process for converting heavy petroleum fractions including an ebulliated bed for producing middle distillates with a low sulfur content
    10.
    发明授权
    Process for converting heavy petroleum fractions including an ebulliated bed for producing middle distillates with a low sulfur content 有权
    用于转化重质石油馏分的方法,包括用于生产低硫含量的中间馏分的沸腾床

    公开(公告)号:US07390393B2

    公开(公告)日:2008-06-24

    申请号:US11505285

    申请日:2006-08-17

    IPC分类号: C10G45/00

    CPC分类号: C10G49/007 C10G2400/06

    摘要: The invention relates to a process for treating heavy petroleum feedstocks for producing a gas oil fraction that has a sulfur content of less than 50 ppm and most often 10 ppm that includes the following stages: a) ebulliated-bed catalytic hydrocracking, b) separation from hydrogen sulfide of a distillate fraction that includes a gas oil fraction and a heavier fraction than the gas oil, c) hydrotreatment of said distillate fraction, and d) separation of a gas oil fraction with less than 50 ppm of sulfur. Make-up hydrogen, preferably all make-up hydrogen, is to stage c). Advantageously, the heavier fraction from step (b) is subjected to catalytic cracking. The invention also relates to an installation that can be used for implementing this process.

    摘要翻译: 本发明涉及一种处理重质石油原料的方法,用于生产硫含量小于50ppm,最常为10ppm的瓦斯油馏分,其包括以下步骤:a)沸腾床催化加氢裂化,b) 馏出物馏分的硫化氢,其包含粗柴油馏分和比瓦斯油更重的馏分,c)加氢处理所述馏出物馏分,以及d)分离具有小于50ppm硫的粗柴油馏分。 补充氢,优选所有化妆氢,都是阶段c)。 有利地,来自步骤(b)的较重馏分经受催化裂化。 本发明还涉及可用于实现该过程的安装。