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    • 1. 发明专利
    • Hydrocarbon converting catalyst
    • 碳氢转化催化剂
    • JPS59150539A
    • 1984-08-28
    • JP2290183
    • 1983-02-16
    • Res Assoc Residual Oil Process
    • SHIOIRI TOMONORIINO TAKASHI
    • B01J21/10B01J29/06B01J29/08C10G11/00C10G11/05C10G47/16
    • C10G11/05B01J21/10B01J29/06B01J29/088B01J2229/42
    • PURPOSE: To obtain a catalyst having high metal resistance and developing excellent catalytic capacity, by combining crystalline aluminosilicate zeolite, an alumina/magnesia matrix and the magnesia in said matrix.
      CONSTITUTION: 3W40wt% (on the basis of a whole catalyst) of crystalline aluminosilicate and 60W90wt% of an alumina/magnesia matrix are contained and the magnesia content in the alumina/magnesia matrix is adjusted to 2W50wt%. This catalyst is used as a catalytic cracking catalyst having such high metal resistance that the production amounts of hydrogen and coke can be suppressed without reducing the yields of gasoline and an intermediate distillate fraction in cracking heavy oil containing 0.5ppm or more of heavy metals such as nickel, vanadium or iron. In addition, in the same way as a conventional hydrocarbon converting catalyst, it can be effectively used in the catalytic cracking, the hydrocraking, the alkylation, the polymerization, the hydro-demetallization and the isomerization of usual hydrocarbon or the disproportionation of toluene.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:通过将结晶硅铝酸盐沸石,氧化铝/氧化镁基质和所述基质中的氧化镁结合,得到具有高金属电阻和显影优异催化能力的催化剂。 构成:含有3-40wt%(基于全部催化剂)的结晶硅铝酸盐和60-90wt%的氧化铝/氧化镁基质,氧化铝/氧化镁基质中的氧化镁含量调节至2-50wt%。 该催化剂用作具有如此高的金属电阻的催化裂化催化剂,可以抑制氢和焦炭的产生量,而不降低汽油的产率和中等馏出物馏分,该重馏分含有0.5ppm以上的重金属,例如 镍,钒或铁。 此外,以与常规烃转化催化剂相同的方式,它可以有效地用于催化裂化,加氢裂化,烷基化,聚合,常规烃的氢脱金属和异构化或甲苯的歧化。
    • 2. 发明专利
    • Fluidized catalytic cracking method of heavy oil
    • 重油的流化催化裂化方法
    • JPS59149985A
    • 1984-08-28
    • JP2290283
    • 1983-02-16
    • Res Assoc Residual Oil Process
    • SHIOIRI TOMONORIINO TAKASHI
    • C10G11/00B01J29/70C10G11/02C10G11/05C10G11/18
    • PURPOSE: To suppress the generation of dry gas and coke without lowering the yield of a light distillate fraction, by subjecting heavy oil containing an Ni and V-containing distillation residue to fluidized catalytic cracking in the presence of a specific catalyst.
      CONSTITUTION: Heavy oil containing a distillation residue containing Ni and V in a total amount of 0.5ppm or more is subjected to fluidized catalytic cracking in the presence of a catalyst prepared by containing matrix of which the magnesia content is 2W5wt%. By this method, hydrogen increased by the metal accumulated on the catalyst and the yield of coke are suppressed and the loads of a gas compressor which is a member of the distillation equipment of a cracking product and an air blower for supplying air for burning the coke on the catalyst are reduced while the yield of a pref. liquid product is increased and the yield of a light distillate fraction reaches 50% or more.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:通过在特定的催化剂存在下使含有Ni和V的蒸馏残渣的重油进行流化催化裂化,抑制干燥气体和焦炭的产生而不降低轻馏分的产率。 构成:含有总计为0.5ppm以上的Ni和V的蒸馏残渣的重油在通过含有氧化镁含量为2-5wt%的基质制备的催化剂存在下进行流化催化裂化。 通过这种方法,由催化剂上积聚的金属增加氢,抑制焦炭产率,作为裂化产物的蒸馏设备的成员的气体压缩机和用于燃烧焦炭的空气的鼓风机的负载 在催化剂上减少,而产率为 液体产物增加,轻馏分馏分的产率达到50%以上。