Crystalline silicate zeolite beta of improved stability
    3.
    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

    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。

    Zeolite beta with improved regeneration characteristics
    4.
    发明授权
    Zeolite beta with improved regeneration characteristics 失效
    沸石β具有改进的再生特性

    公开(公告)号:US4840929A

    公开(公告)日:1989-06-20

    申请号:US218438

    申请日:1988-07-11

    IPC分类号: B01J29/70 B01J29/74

    摘要: The present invention describes a method for preparing a noble metal Zeolite Beta containing catalyst with improved platinum redispersion characteristics. The method includes using a mineral acid to extract the framework aluminum from the zeolite and forming the catalyst particles without the use of inorganic oxide binders.

    摘要翻译: 本发明描述了一种制备具有改进的铂再分散特性的贵金属沸石β的催化剂的方法。 该方法包括使用无机酸从沸石中提取骨架铝并在不使用无机氧化物粘合剂的情况下形成催化剂颗粒。

    Nitrogen resistant paraffin hydroisomerization catalysts
    5.
    发明授权
    Nitrogen resistant paraffin hydroisomerization catalysts 失效
    耐氮石蜡加氢异构化催化剂

    公开(公告)号:US4814543A

    公开(公告)日:1989-03-21

    申请号:US138749

    申请日:1987-12-28

    摘要: The present invention includes a process and catalyst composition for paraffinic isomerization of a hydrocarbon feedstock which has a paraffin content having no more than 20 carbon atoms per molecule. The feedstock is contacted with a crystalline aluminosilicate zeolite catalyst having pore openings defined by: (1) a ratio of sorption of n-hexane to o-xylene, on a volume percent basis, of greater than about 3, which sorption is determined at a P/P.sub.o of 0.1 and at a temperature of 50.degree. C. for n-hexane and 80.degree. C. for o-xylene and (2) by the ability of selectively cracking 3-methylpentane (3MP) in preference to the doubly branched 2,3-dimethylbutane (DMB) at 1000.degree. F. and 1 atmosphere pressure from a 1/1/1 weight ratio mixture of n-hexane/3-methyl-pentane/2,3-dimethylbutane, with the ratio of rate constants k.sub.3MP/ k.sub.DMB determined at a temperature of 1000.degree. F. being in excess of about 2, e.g., ZSM-22, ZSM-23, AXM-35 and mixtures thereof, in combination with a Group VIII metal, and having a zeolite SiO.sub.2 /Al.sub.2 O.sub.3 ratio of at least about 20:1 at a temperature and pressure suitable for isomerization.

    摘要翻译: 本发明包括用于烃原料的链烷烃异构化的方法和催化剂组合物,其具有每分子具有不超过20个碳原子的链烷烃含量。 原料与具有孔开口的结晶铝硅酸盐沸石催化剂接触,所述沸石催化剂的定义如下:(1)正丁烷与邻二甲苯的吸附比例,以体积百分数计,大于约3,该吸附在 P / Po为0.1,温度为50℃,正己烷和80℃为邻二甲苯,(2)选择性裂解3-甲基戊烷(3MP)优于双支链2 ,三甲基丁烷(DMB)在1000°F和1大气压下,由正己烷/ 3-甲基戊烷/ 2,3-二甲基丁烷的1/1/1重量比混合物与速率常数比例k3MP / kDMB在1000°F的温度下测定为超过约2,例如ZSM-22,ZSM-23,AXM-35及其混合物,与VIII族金属组合,并具有SiO 2 / Al 2 O 3沸石 在适于异构化的温度和压力下至少约20:1的比例。

    Integrated low pressure aromatization process
    7.
    发明授权
    Integrated low pressure aromatization process 失效
    集成低压芳构化工艺

    公开(公告)号:US5037529A

    公开(公告)日:1991-08-06

    申请号:US459403

    申请日:1989-12-29

    IPC分类号: C10G59/02

    CPC分类号: C10G59/02

    摘要: High purity benzene and high octane alkylaromatic gasoline can be obtained via a dual stage reforming process utilizing a non-acidic Group VIII metal containing microporous crystalline silicate catalyst in the first stage followed by first stage effluent treatment over acidic zeolite catalyst operating under conditions in the second stage to upgrade the first stage effluent in RON, in aromatic content or both.

    摘要翻译: 高纯度苯和高辛烷值的烷基芳烃汽油可以通过双阶段重整方法获得,该方法利用在第一阶段中使用含非极性Ⅷ族金属的微孔结晶硅酸盐催化剂,然后在第二阶段的条件下在酸性沸石催化剂上进行第一阶段流出物处理 在RON,芳香含量或两者都升级第一阶段流出物的阶段。

    Aromatization process
    8.
    发明授权
    Aromatization process 失效
    芳香化过程

    公开(公告)号:US4861932A

    公开(公告)日:1989-08-29

    申请号:US140274

    申请日:1987-12-31

    IPC分类号: C07C5/41 C10G35/095 C10G59/02

    摘要: A process for converting a C.sub.2 -C.sub.12 paraffinic hydrocarbon feed to aromatics comprising passing the feed through a first conversion zone wherein the feed contacts a noble metal/low acidity medium pore size zeolite catalyst, and then passing the resulting hydrocarbon mixture through a second conversion zone wherein the resulting hydrocarbon mixture contacts a medium pore size acidic zeolite catalyst.

    摘要翻译: 将C2-C12链烷烃进料转化为芳族化合物的方法,包括使进料通过第一转化区,其中进料接触贵金属/低酸度介质孔径沸石催化剂,然后使所得烃混合物通过第二转化区 其中所得烃类混合物与中等孔径的酸性沸石催化剂接触。

    Apparatus for FCC process with catalyst separation
    9.
    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

    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
    10.
    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

    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。