Molecular sieve agglomerates with improved transport properties
    61.
    发明授权
    Molecular sieve agglomerates with improved transport properties 失效
    具有改善的输送性能的分子筛结块

    公开(公告)号:US5168084A

    公开(公告)日:1992-12-01

    申请号:US519972

    申请日:1990-05-07

    摘要: Molecular sieve agglomerates exhibiting reduced pore mouth blockage and decreased diffusivity resistance to the internal sieve pores result from coating, prior to addition of a binding agent to the sieve, the molecular sieve particles with an organic polymer, fixing the polymer to the sieve surface so that it exhibits no migratory tendencies and subsequently removing the coating by combustion during calcination of the formed agglomerate. Such agglomerates showed enhanced activity and selectivity in typical refining processes such as dewaxing and fluid catalytic cracking.

    摘要翻译: 分子筛附聚物表现出减少的孔口阻塞和降低的对内部筛孔的扩散性的抵抗力是在将粘合剂加入到筛子中之前涂覆的,分子筛颗粒与有机聚合物固定在筛子表面上,使得 它表现出没有迁移倾向,随后在形成的附聚物煅烧期间通过燃烧除去涂层。 这种附聚物在典型的精制方法如脱蜡和流化催化裂化中显示出增强的活性和选择性。

    Reforming with a catalyst containing a Group VIII noble metal, a Group
VIII non-noble metal, and gallium on separate support particles
    62.
    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 失效
    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

    公开(公告)号:US4482449A

    公开(公告)日:1984-11-13

    申请号:US595278

    申请日:1984-03-30

    摘要: 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.

    摘要翻译: 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。

    Skeletal isomerization of n-olefins to iso-olefins on binded ferrierite
zeolites
    63.
    发明授权
    Skeletal isomerization of n-olefins to iso-olefins on binded ferrierite zeolites 失效
    在结合的镁碱沸石沸石上正构烯烃异构化成异烯烃

    公开(公告)号:US5510560A

    公开(公告)日:1996-04-23

    申请号:US112921

    申请日:1993-08-30

    IPC分类号: C07C5/27 C07C5/22

    CPC分类号: C07C5/2775 C07C2529/06

    摘要: The method of converting n-butylenes to isobutylene by a skeletal isomrization reaction wherein said reaction is carried out at a temperature of between 300.degree. C. and 650.degree. C., under a pressure of between 0.1 and 100 atmospheres and a space velocity of said n-butylenes of between 0.1 and 40 WHSV using a cagalyst comprising a zeolite binder selected frm the group consisting of alumina, silica, silica-alumina, clay and a combination thereof, said catalyst having a pore size of at least about 4.5 angstroms and the pore size structure is characteried by intersecting 10-member ring and 8-member ring channels.

    摘要翻译: 通过骨架均化反应将正丁烯转化为异丁烯的方法,其中所述反应在约100℃至100℃之间的压力下在300℃和650℃之间的温度下进行,所述反应在所述 使用包含选自由氧化铝,二氧化硅,二氧化硅 - 氧化铝,粘土及其组合组成的组的沸石粘合剂的囊状物的0.1至40WHSV的正丁烯,所述催化剂的孔径至少为约4.5埃, 孔径结构的特征是10个环和8个环通道相交。

    Reforming with an improved platinum-containing catalyst

    公开(公告)号:US4401558A

    公开(公告)日:1983-08-30

    申请号:US318554

    申请日:1981-11-05

    CPC分类号: B01J37/04 C10G35/09

    摘要: 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.

    Reforming with an improved platinum-containing catalyst
    65.
    发明授权
    Reforming with an improved platinum-containing catalyst 失效
    用改进的含铂催化剂重整

    公开(公告)号:US4353814A

    公开(公告)日:1982-10-12

    申请号:US108177

    申请日:1979-12-28

    CPC分类号: B01J37/04 C10G35/09

    摘要: 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.

    摘要翻译: 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。

    Catalyst and process
    66.
    发明授权
    Catalyst and process 失效
    催化剂和工艺

    公开(公告)号:US4298461A

    公开(公告)日:1981-11-03

    申请号:US92569

    申请日:1979-11-08

    摘要: A hydrocarbon conversion catalyst comprising at least one platinum-group metal deposited on a composite comprising (I) alumina and (II) rhenium deposited on silica. The catalyst eliminates the need for presulfiding treatment required by conventional rhenium-promoted catalyst in reforming service, without comparative loss in reforming performance.

    摘要翻译: 一种烃转化催化剂,其包含沉积在包含沉积在二氧化硅上的(I)氧化铝和(II)铼)的复合材料上的至少一种铂族金属。 该催化剂不需要在重整操作中常规的铼促进催化剂所需的预硫化处理,而在重整性能上没有相应的损失。

    Reforming with an improved rhenium-containing catalyst
    67.
    发明授权
    Reforming with an improved rhenium-containing catalyst 失效
    用改进的含铼催化剂重整

    公开(公告)号:US4261811A

    公开(公告)日:1981-04-14

    申请号:US27909

    申请日:1979-04-06

    CPC分类号: C10G35/09 B01J23/6567

    摘要: An improved process for the reforming of a hydrocarbon stream, which process comprises contacting said hydrocarbon stream under reforming conditions and in the presence of hydrogen with a catalyst which comprises platinum, rhenium, a small amount of palladium, and combined halogen on a refractory inorganic oxide, such as an alumina, and which has not been presulfided. The improvement comprises a rhenium-containing catalyst which has not been presulfided and which contains a small amount of palladium, i.e., about 0.05 wt. % to about 1 wt. % palladium. The feedstock being reformed can contain up to about 50 ppm sulfur.

    摘要翻译: 一种用于烃流重整的改进方法,该方法包括在重整条件下和氢存在下使所述烃流与包含铂,铼,少量钯和在耐火无机氧化物上的组合卤素的催化剂接触 ,例如氧化铝,并且尚未预硫化。 该改进包括未被预硫化并含有少量钯的含铼催化剂,即约0.05wt。 %至约1wt。 %钯。 重整的原料可以含有高达约50ppm的硫。