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    • 1. 发明授权
    • Catalyst based on a molecular sieve and a process for selective hydroisomerisation of long linear and/or slightly branched paraffins using that catalyst
    • 基于分子筛的催化剂和使用该催化剂的长线性和/或稍微支化的链烷烃的选择性加氢异构化的方法
    • US06198015B1
    • 2001-03-06
    • US09034350
    • 1998-03-04
    • Christian MarcillyEric BenazziNathalie George-Marchal
    • Christian MarcillyEric BenazziNathalie George-Marchal
    • C07C513
    • C10G45/64B01J29/46
    • The invention concerns a process for selective hydroisomerization of compounds with an n-alkane chain containing more than 10 carbon atoms, in which the compound to be treated is brought into contact with a catalyst comprising at least one hydro-dehydrogenating element and at least one molecular sieve having a one- or two-dimensional pore network, the accessible pore openings of which are delimited by 10 oxygen atoms, and a distance termed the bridging distance between the pores of less then 0.70 nm, and the zeolite is such that a catalyst which undergoes a standard n-heptadecane isomerization test has, for a conversion of 95%, a selectivity of at least 70% for isomerized products, and the catalyst contains at least 5% by weight of at least one hydro-dehydrogenating element selected from the group formed by non noble GVIII metals, GVIB metals, and niobium, and the catalyst preferably contains phosphorous. The sieve is preferably a NU-10, NU-23, NU-87, EU-13 or Theta-1 zeolite.
    • 本发明涉及一种使含有多于10个碳原子的正烷烃链选择性加氢异构化的方法,其中待处理化合物与包含至少一个加氢脱氢元素的催化剂和至少一个分子 具有一维或二维孔网的筛,其可及孔的开口由10个氧原子界定,并且称为孔之间的桥接距离小于0.70nm的距离,并且沸石使得催化剂 进行标准的正十七烷异构化试验对于异构化产物具有至少70%的选择性为95%的转化率,并且催化剂含有至少5重量%的至少一种选自组中的加氢脱氢元件 由非贵金属GVIII金属,GVIB金属和铌形成,并且催化剂优选含有磷。筛优选为NU-10,NU-23,NU-87,EU-13或Theta-1沸石。
    • 3. 发明授权
    • Process for improving the pour point, and a catalyst based on at least one MTT, Ton or Fer zeolite
    • 改善倾点的方法,以及基于至少一种MTT,Ton或Fer沸石的催化剂
    • US06235960B1
    • 2001-05-22
    • US09310181
    • 1999-05-12
    • Eric BenazziSlavik KasztelanNathalie George-Marchal
    • Eric BenazziSlavik KasztelanNathalie George-Marchal
    • C07C513
    • C10G45/64B01J29/67B01J29/7284B01J29/7292B01J29/7484B01J29/7492B01J29/7884B01J29/7892B01J35/1061B01J35/1085B01J2229/26B01J2229/42
    • A process for improving the pour point of a feed comprising paraffins containing more than 10 carbon atoms, in which the feed to be treated is brought into contact with a catalyst comprising at least one zeolite with structure type MTT, TON or FER or any possible combination of these three, at least one hydro-dehydrogenating element selected from elements from group VIB and group VIII of the periodic table, at least one deposited promoter element (boron, silicon, phosphorous), optionally at least one group VIIA element, optionally at least one group VIIB element, at a temperature in the range 170° C. to 500° C., a pressure in the range 1 to 250 bars and at an hourly space velocity in the range 0.05 to 100 h−1, in the presence of hydrogen in an amount 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 in pour point. The invention also relates to a catalyst containing silicon and to its use for converting hydrocarbon-containing feeds.
    • 一种用于改进含有多于10个碳原子的链烷烃的进料的倾点的方法,其中待处理的进料与包含至少一种结构类型为MTT,TON或FER的沸石或任何可能的组合的催化剂接触 这些三种中的至少一种选自元素周期表第VIB族和第VIII族元素的至少一种加氢脱氢元素,至少一种沉积的促进元素(硼,硅,磷),任选至少一种VIIA族元素,任选至少 一组VIIB元素,在170℃至500℃的温度范围内,压力范围为1至250巴,时间空间速度为0.05至100小时-1,在存在 量为50至2000升/升的进料的氢。 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它进料。本发明还涉及含硅的催化剂及其用于转化含烃物料的用途。