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    • 1. 发明申请
    • Catalytic system and process for the production of hydrogen
    • 催化系统和生产氢气的方法
    • US20040152790A1
    • 2004-08-05
    • US10768103
    • 2004-02-02
    • ENI S.p.A.SNAMPROGETTI S.p.A.
    • Ugo CornaroDomenico Sanfilippo
    • C07C027/06
    • B01J23/83B01J23/005B01J23/745B01J23/78B01J23/80B01J35/08C01B3/063Y02E60/36
    • Catalytic system for the production of hydrogen consisting of an active component based on iron and a micro-spheroidal carrier based on alumina and represented by the following formula nullFex1Mx2Qx3Dx4Alx5nullOy wherein xi with inull1.5 represent the atomic percentages assuming values which satisfy the equation nullxinull100. y is the value required by the oxidation number with which the components are present in the formulate, x1 is the atomic percentage with which Fe is present in the formulate and ranges from 5 to 80, preferably from 20 to 50, M is Cr and/or Mn, x2 ranges from 0 to 30, preferably from 0 to 10, Q is La, Lanthanides (with Ce particularly preferred), Zr or a combination thereof, x3 ranges from 0 to 30, preferably from 0 to 10, D is Mg, Ca, Ba, Co, Ni, Cu, Zn or combinations thereof, x4 ranges from 0 to 35, preferably from 5 to 25, x5 is the atomic percentage with which Al is present in the formulate and ranges from 20 to 95, preferably from 50 to 80.
    • 用于生产基于铁的活性组分和基于氧化铝的微球形载体的氢的催化体系,由下式[Fex1Mx2Qx3Dx4Alx5] Oy表示,其中i = 1.5的xi表示原子百分比,假定满足式 Sigmaxi = 100。 y是组分存在于配方中的氧化数所需的值,x1是配制物中Fe存在的原子百分数,范围为5至80,优选为20至50,M为Cr和/ 或Mn,x2为0〜30,优选为0〜10,Q为La,镧系元素(特别优选Ce),Zr或其组合,x3为0〜30,优选为0〜10,D为Mg ,Ca,Ba,Co,Ni,Cu,Zn或其组合,x4的范围为0至35,优选5至25,x5是配位体中Al存在的原子百分比,范围为20至95,优选 从50到80。
    • 5. 发明申请
    • Process for obtaining a
    • 通过烯烃或其混合物的低聚获得柴油切割燃料的方法
    • US20020183576A1
    • 2002-12-05
    • US10109660
    • 2002-04-01
    • SNAMPROGETTI S.p.A.
    • Cristina FlegoCarlo PeregoMario Marchionna
    • C07C002/12
    • C10G50/00C10G2400/04
    • Process for obtaining a nulldiesel cutnull fuel having a CN cetane number equal to or greater than 48 and a content of aromatics lower than 0.4% by weight starting from olefins or their mixtures, characterized in that it comprises the following steps: oligomerizing said olefins having from 2 to 10 carbon atoms in the presence of synthetic zeolites containing silicon, titanium and aluminum oxides, having a molar ratio SiO2/Al2O3 ranging from 100 to 300, a molar ratio SiO2/TiO2 greater than 41 and a extraframework titanium oxide content which is zero or less than 25% with respect to the whole titanium oxide present, at a temperature ranging from 180 to 300null C., at a pressure greater than 40 atm and a WHSV space velocity equal to or greater than 1 hnull1, in order to obtain a stream essentially consisting of oligomerized C5-C24 hydrocarbons; distilling the stream obtained from the oligomerization in order to separate a C12-C24 hydrocarbon stream from a C5-C12 hydrocarbon stream; hydrogenating the separated C12-C24 hydrocarbon stream.
    • 获得CN十六烷值等于或大于48的“柴油切割”燃料和烯烃或其混合物开始的低于0.4重量%的芳烃含量的方法,其特征在于其包括以下步骤:使所述烯烃低聚 在含有硅,钛和氧化铝的合成沸石存在下具有2至10个碳原子,摩尔比为SiO 2 / Al 2 O 3的摩尔比为100-300,SiO 2 / TiO 2的摩尔比大于41,以及外部结构的二氧化钛含量 相对于存在的整个氧化钛,在180-300℃的温度,大于40atm的压力和等于或大于1h -1的WHSV空速下,为零或小于25% 以获得基本上由低聚C5-C24烃组成的物流; 蒸馏从低聚获得的物流,以分离C 12 -C 24烃物流与C5-C12烃物流; 氢化分离的C12-C24烃流。