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    Dispersed catalyst cracking with methanol as a coreactant
    1.
    发明授权
    Dispersed catalyst cracking with methanol as a coreactant 失效
    用甲醇作为共反应剂分散催化剂裂解

    公开(公告)号：US4627911A

    公开(公告)日：1986-12-09

    申请号：US815660

    申请日：1985-12-30

    申请人： Nai Y. Chen ,  Thomas F. Degnan, Jr.

    发明人： Nai Y. Chen ,  Thomas F. Degnan, Jr.

    IPC分类号： C10G11/05 ,  C07C1/24 ,  C10G47/16

    CPC分类号： C10G11/05

    摘要： A catalytic cracking process is described in which methanol is a coreactant with gas oil in combination with a small amount (catalyst/oil 0.01) of a dispersed, very fine, and highly active catalyst powder, such as ZSM-5B. The methanol is preferably admixed with the catalyst before admixture with the oil in order to protect the catalyst from adsorption of poisonous compounds (e.g., nitrogenous compounds) during the initial stages of the reaction, particularly if the methanol is insoluble in a non-polar hydrocarbon feed. The premixed materials are fed into a riser reactor. The residence time in the reactor is 6-15 seconds. Preferably, the catalyst is not regenerated. The quantity of methanol is maintained so that its exothermic reaction is approximately heat balanced with the endothermic catalytic cracking reaction.

    摘要翻译： 描述了催化裂化方法，其中甲醇是与少量（催化剂/油0.01）的分散的，非常细的和高活性的催化剂粉末如ZSM-5B组合的助燃油的共反应物。 在与油混合之前，甲醇优选与催化剂混合，以便在反应的初始阶段保护催化剂免受有毒化合物（例如含氮化合物）的吸附，特别是如果甲醇不溶于非极性烃 饲料。 将预混材料进料到提升管反应器中。 反应器中的停留时间为6-15秒。 优选地，催化剂不再生。 维持甲醇的量，使其放热反应与吸热催化裂化反应近似热平衡。

    Apparatus for FCC process with catalyst separation
    6.
    发明授权
    Apparatus for FCC process with catalyst separation 失效
    FCC催化分离装置

    公开(公告)号：US4971766A

    公开(公告)日：1990-11-20

    申请号：US437064

    申请日：1989-11-16

    申请人： Nai Y. Chen ,  Billy K. Huh ,  Thomas E. Degnan

    发明人： Nai Y. Chen ,  Billy K. Huh ,  Thomas E. Degnan

    IPC分类号： C10G11/18

    CPC分类号： C10G11/18

    摘要： An FCC or fluidized catalytic cracking process and apparatus for converting heavy metals laden crudes is disclosed. The heavy feed, conventional catalyst and an additive or vanadium getter contact the feed in a riser reactor. The additive is segregated from conventional FCC catalyst upstream of the conventional FCC regenerator. An elutriating, upflow riser reactor may be used with a coarse, rapidly settling getter. A fine, slowly settling getter may be used, with getter segregation achieved by using an elutriating cyclone on the riser outlet, an elutriating catalyst stripper, a sieve, or the like. The spent getter may be used once through, regenerated in a separate getter regenerator, or used as a source of fuel. Alumina and sponge coke are preferred getters.

    摘要翻译： 公开了一种FCC或流化催化裂化方法和用于转化重金属负载原油的装置。 重料，常规催化剂和添加剂或钒吸附剂在提升管反应器中接触进料。 该添加剂与常规FCC再生器上游的常规FCC催化剂分离。 淘汰式上升式提升管式反应器可与粗，快速沉降的吸气剂一起使用。 可以使用细的缓慢沉降的吸气剂，通过在提升管出口，淘洗催化剂汽提器，筛子等上使用淘洗旋风来实现吸气剂分离。 废吸气剂可以一次使用，在单独的吸气剂再生器中再生，或用作燃料来源。 氧化铝和海绵焦炭是优选的吸气剂。

    Catalyst for dewaxing hydrocarbon feedstock
    7.
    发明授权
    Catalyst for dewaxing hydrocarbon feedstock 失效
    用于脱蜡烃原料的催化剂

    公开(公告)号：US4877581A

    公开(公告)日：1989-10-31

    申请号：US239257

    申请日：1988-09-01

    申请人： Nai Y. Chen ,  Dennis E. Walsh

    发明人： Nai Y. Chen ,  Dennis E. Walsh

    IPC分类号： B01J29/44 ,  B01J29/74 ,  C10G45/64

    CPC分类号： C10G45/64 ,  B01J29/44

    摘要： A paraffin conversion process for hydroisomerizing a nitrogen and wax-containing hydrocarbon feedstock comprising contacting the feedstock with a catalyst including a ZSM-11 zeolite characterized by an alpha value from about 10 to 50, in combination with a Group VIII metal hydrogenation-dehydrogenation component of platinum or palladium at a temperature of about 400.degree. F. to about 850.degree. F. and at a pressure of from about 200 to about 2000 psig.

    摘要翻译： 一种用于使含氮和含蜡的烃原料加氢异构化的链烷烃转化方法，包括使原料与包含Z值为约10至50的α值的ZSM-11沸石的催化剂结合，与第VIII族金属加氢脱氢组分 铂或钯，温度为约400°F至约850°F，压力为约200至约2000psig。

    Crystalline silicate zeolite beta of improved stability
    9.
    发明授权
    Crystalline silicate zeolite beta of improved stability 失效
    结晶硅酸盐沸石β具有改善的稳定性

    公开(公告)号：US4789656A

    公开(公告)日：1988-12-06

    申请号：US070170

    申请日：1987-07-02

    申请人： Nai Y. Chen ,  Sharon B. McCullen

    发明人： Nai Y. Chen ,  Sharon B. McCullen

    IPC分类号： B01J29/74 ,  C10G45/64 ,  B01J29/32

    CPC分类号： C10G45/64 ,  B01J29/7415

    摘要： A process is described for preparing a binder-free Zeolite Beta containing catalyst which has a highly dispersed noble metal incorporated into the framework. The process comprises steaming Zeolite Beta, followed by noble metal incorporation and calcination. The present invention is also directed to an improved calcination process.

    摘要翻译： 描述了一种制备不含无粘结剂的含沸石沸石的催化剂的方法，该催化剂具有掺入框架中的高度分散的贵金属。 该方法包括蒸煮沸石β，然后进行贵金属掺入和煅烧。 本发明还涉及一种改进的煅烧方法。

    Hydroprocessing catalyst and process
    10.
    发明授权
    Hydroprocessing catalyst and process 失效
    加氢催化剂和工艺

    公开(公告)号：US4756822A

    公开(公告)日：1988-07-12

    申请号：US31807

    申请日：1987-03-30

    申请人： Nai Y. Chen ,  Tracy J. Huang

    发明人： Nai Y. Chen ,  Tracy J. Huang

    IPC分类号： B01J29/86 ,  C10G47/16

    CPC分类号： B01J29/86 ,  C10G47/16

    摘要： This invention provides a novel hydrocracking catalyst composition that contains Zeolite Beta having a framework boron content, a solid source of alumina, and a hydrogenation component. It further provides a low-pressure hydrocracking process that uses such composition.

    摘要翻译： 本发明提供一种新型加氢裂化催化剂组合物，其包含具有骨架硼含量的沸石β，氧化铝的固体源和氢化组分。 它还提供了使用这种组合物的低压加氢裂化方法。