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    • 2. 发明授权
    • Reforming with an improved platinum-containing catalyst
    • 用改进的含铂催化剂重整
    • US4319984A
    • 1982-03-16
    • US237721
    • 1981-02-24
    • Regis J. PelletRalph J. Bertolacini
    • Regis J. PelletRalph J. Bertolacini
    • B01J23/656B01J37/04C10G35/09C10G35/06
    • B01J23/6567B01J37/04C10G35/09
    • There is disclosed a catalyst, which catalyst comprises a physical particle-form mixture of a Component A and a Component B, said Component A comprising at least one Group VIII noble metal deposed on a solid catalyst support material providing acidic catalytic sites and said Component B comprising rhenium or a compound of rhenium deposed on a solid catalyst support material, said catalyst having been prepared by thoroughly blending finely-divided particles of Component A and Component B to provide a thoroughly-blended composite, said finely-divided particles having a particle diameter that is less than 100 mesh (150 microns), and forming said composite into particles having a size that is greater than 100 mesh (150 microns) and being suitable for use in a hydrocarbon conversion reaction zone.The catalyst can be employed in a process for the reforming of a hydrocarbon stream, which process comprises contacting said stream in a reaction zone under reforming conditions and in the presence of hydrogen with said catalyst.
    • 公开了一种催化剂,该催化剂包含组分A和组分B的物理颗粒形式的混合物,所述组分A包含至少一种第八族贵金属,其位于提供酸性催化位点的固体催化剂载体材料上,所述组分B 所述催化剂是通过将组分A和组分B的细碎颗粒充分混合而制备的,以提供充分混合的复合材料,所述细碎颗粒具有颗粒直径 小于100目(150微米),并将所述复合物形成为尺寸大于100目(150微米)的颗粒,并且适用于烃转化反应区。 该催化剂可用于烃流重整的方法中,该方法包括在重整条件下和氢气存在下,将所述物流在反应区中与所述催化剂接触。
    • 3. 发明授权
    • Reforming with an improved platinum-containing catalyst
    • 用改进的含铂催化剂重整
    • US4302358A
    • 1981-11-24
    • US86707
    • 1979-10-22
    • Regis J. PelletRalph J. Bertolacini
    • Regis J. PelletRalph J. Bertolacini
    • B01J23/656B01J27/13B01J37/04C10G35/09B01J27/08B01J23/64B01J27/10
    • C10G35/09B01J23/6567B01J37/04
    • There is disclosed a catalyst, which catalyst comprises a physical particle-form mixture of a Component A and a Component B, said Component A comprising at least one Group VIII noble metal deposed on a solid catalyst support material providing acidic catalytic sites and said Component B comprising rhenium or a compound of rhenium deposed on a solid catalyst support material, said catalyst having been prepared by thoroughly blending finely-divided particles of Component A and Component B to provide a thoroughly-blended composite, said finely-divided particles having a particle diameter that is less than 100 mesh (150 microns), and forming said composite into particles having a size that is greater than 100 mesh (150 microns) and being suitable for use in a hydrocarbon conversion reaction zone.The catalyst can be employed in a process for the reforming of a hydrocarbon stream, which process comprises contacting said stream in a reaction zone under reforming conditions and in the presence of hydrogen with said catalyst.
    • 公开了一种催化剂,该催化剂包含组分A和组分B的物理颗粒形式的混合物,所述组分A包含至少一种第八族贵金属,其位于提供酸性催化位点的固体催化剂载体材料上,所述组分B 所述催化剂是通过将组分A和组分B的细碎颗粒充分混合而制备的,以提供充分混合的复合材料,所述细碎颗粒具有颗粒直径 小于100目(150微米),并将所述复合物形成为尺寸大于100目(150微米)的颗粒,并且适用于烃转化反应区。 该催化剂可用于烃流重整的方法中,该方法包括在重整条件下和氢气存在下,将所述物流在反应区中与所述催化剂接触。
    • 4. 发明授权
    • Reforming catalyst containing a group VIII noble metal, a group VIII
non-noble metal, and gallium on separate support particles
    • 含有VIII族贵金属,VIII族非贵金属和镓的单独载体颗粒上的重整催化剂
    • US4469812A
    • 1984-09-04
    • US533145
    • 1983-09-16
    • Cecelia M. SorrentinoRegis J. PelletRalph J. Bertolacini
    • Cecelia M. SorrentinoRegis J. PelletRalph J. Bertolacini
    • B01J23/89B01J37/04C10G35/09B01J21/04B01J23/62B01J23/82B01J27/08
    • B01J23/896B01J37/04C10G35/09
    • The catalyst comprises a physical particle-form mixture of a Component A, a Component B, and a Component C, said Component A comprising at least one Group VIII noble metal, preferably platinum, deposed on a solid catalyst support material providing acidic catalytic sites, said Component B comprising a small amount of a non-noble metal of Group VIII selected from cobalt, nickel, and mixtures thereof, preferably cobalt, on a solid catalyst support material providing acidic catalytic sites, said Component C comprising a small amount of gallium deposed on a solid catalyst support material providing acidic catalytic sites, and said catalyst having been prepared by thoroughly and intimately blending finely-divided particles of said Components A, B, and C to provide a thoroughly-blended composite.The catalyst can be employed suitably in a hydrocarbon conversion process. In particular, the catalyst can be employed in a process for the reforming of a hydrocarbon stream, which process comprises contacting said stream in a reforming zone under reforming conditions and in the presence of hydrogen with said catalyst. The process can be used advantageously to reform a hydrocarbon stream that contains up to 80 ppm sulfur.
    • 催化剂包含组分A,组分B和组分C的物理颗粒形式的混合物,所述组分A包含至少一种第八族贵金属,优选铂,其沉积在提供酸性催化位点的固体催化剂载体材料上, 所述组分B包含少量选自钴,镍及其混合物,优选钴的非贵金属的第Ⅷ族,在提供酸性催化位点的固体催化剂载体材料上,所述组分C包含少量镓, 在提供酸性催化位点的固体催化剂载体材料上,并且所述催化剂通过将所述组分A,B和C的细碎颗粒彻底和紧密地混合以提供充分混合的复合材料制备。 催化剂可以在烃转化方法中适当地使用。 特别地,催化剂可以用于烃流重整的方法中,该方法包括在重整条件下和氢气存在下将所述物流在重整区中与所述催化剂接触。 该方法可有利地用于重整含有高达80ppm硫的烃流。
    • 5. 发明授权
    • Reforming with a catalyst containing a Group VIII noble metal, a Group
VIII non-noble metal, and gallium on separate support particles
    • 使用含有VIII族贵金属,VIII族非贵金属和镓的催化剂在分开的载体颗粒上重整
    • US4482449A
    • 1984-11-13
    • US595278
    • 1984-03-30
    • Cecelia M. SorrentinoRegis J. PelletRalph J. Bertolacini
    • Cecelia M. SorrentinoRegis J. PelletRalph J. Bertolacini
    • B01J23/89B01J37/04C10G35/09C10G35/085
    • C10G35/09B01J23/896B01J37/04
    • The catalyst comprises a physical particle-form mixture of a Componet A, a Component B, and a Component C, said Component A comprising at least one Group VIII noble metal, preferably platinum, deposed on a solid catalyst support material providing acidic catalytic sites, said Component B comprising a small amount of a non-noble metal of Group VIII selected from cobalt, nickel, and mixtures thereof, preferably cobalt, on a solid catalyst support material providing acidic catalytic sites, said Component C comprising a small amount of gallium deposed on a solid catalyst support material providing acidic catalytic sites, and said catalyst having been prepared by thoroughly and intimately blending finely-divided particles of said Component A, B, and C to provide a thoroughly-blended composite.The catalyst can be employed suitably in a hydrocarbon conversion process. In particular, the catalyst can be employed in a process for the reforming of a hydrocarbon stream, which process comprises contacting said stream in a reforming zone under reforming conditions and in the presence of hydrogen with said catalyst. The process can be used advantageously to reform a hydrocarbon stream that contains up to 80 ppm sulfur.
    • 所述催化剂包括组分A,组分B和组分C的物理颗粒形式的混合物,所述组分A包含至少一种第八族贵金属,优选铂,其沉积在提供酸性催化位点的固体催化剂载体材料上, 所述组分B包含少量选自钴,镍及其混合物,优选钴的非贵金属的第Ⅷ族,在提供酸性催化位点的固体催化剂载体材料上,所述组分C包含少量镓, 在提供酸性催化位点的固体催化剂载体材料上,并且所述催化剂通过将所述组分A,B和C的细碎颗粒彻底和紧密地混合以提供充分混合的复合材料制备。 催化剂可以在烃转化方法中适当地使用。 特别地,催化剂可以用于烃流重整的方法中,该方法包括在重整条件下和氢气存在下将所述物流在重整区中与所述催化剂接触。 该方法可有利地用于重整含有高达80ppm硫的烃流。
    • 7. 发明授权
    • Reforming with an improved platinum-containing catalyst
    • 用改进的含铂催化剂重整
    • US4353814A
    • 1982-10-12
    • US108177
    • 1979-12-28
    • Regis J. PelletRalph J. BertolaciniDonna L. Lysholm
    • Regis J. PelletRalph J. BertolaciniDonna L. Lysholm
    • B01J37/04C10G35/09B01J27/06B01J27/10
    • B01J37/04C10G35/09
    • There is disclosed a catalyst, which catalyst comprises a physical particle-form mixture of a Component A and a Component B, said Component A comprising one or more Group VIII noble metals and a combined halogen deposed on a refractory inorganic oxide and said Component B comprising a metal from Group IVB or Group VB of the Periodic Table of Elements and a combined halogen deposed on a refractory inorganic oxide. Such catalyst is suitable for use in a hydrocarbon conversion reaction zone.The catalyst can be employed in a process for the reforming of a hydrocarbon stream, which process comprises contacting said stream in a reaction zone under reforming conditions and in the presence of hydrogen with said catalyst. The catalyst is not presulfided. A preferred process comprises contacting a hydrocarbon stream that contains a substantial amount of sulfur.
    • 公开了一种催化剂,该催化剂包含组分A和组分B的物理颗粒形式的混合物,所述组分A包含一种或多种第VIII族贵金属和被置于耐火无机氧化物上的组合卤素,所述组分B包含 元素周期表第IVB族或第VB族的金属,以及沉积在耐火无机氧化物上的组合卤素。 这种催化剂适用于烃转化反应区。 该催化剂可用于烃流重整的方法中,该方法包括在重整条件下和氢气存在下,将所述物流在反应区中与所述催化剂接触。 催化剂未预硫化。 优选的方法包括使含有大量硫的烃流接触。