Catalytic dewaxing of light and heavy oils in dual parallel reactors
    6.
    发明授权
    Catalytic dewaxing of light and heavy oils in dual parallel reactors 失效
    双重并联反应器中轻油和重油的催化脱蜡

    公开(公告)号:US4605488A

    公开(公告)日:1986-08-12

    申请号:US733339

    申请日:1985-05-13

    CPC分类号: C10G65/00 C10G45/64 C10G65/16

    摘要: Relatively heavy and relatively light lube chargestocks are dewaxed in two parallel, separate reactors. The reactor used for dewaxing the relatively light chargestock contains a crystallize zeolite having pore openings defined by: (1) a ratio of sorption of n-hexane to o-xylene, on a volume percent basis, of greater than 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., natural and synthetic ferrierite, ZSM-22, ZSM-23, ZSM-35 and mixtures thereof. The reactor used for dewaxing the relatively heavy chargestock contains a crystalline aluminosilicate zeolite having pore openings defined by: (1) a ratio of sorption of n-hexane to o-xylene, on a volume percent basis, or less than 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, (2) the abiilty 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 less than about 2, and (3) a Constraint Index value of greater than about 1, e.g., ZSM-5, ZSM-11, ZSM-5/ZSM-11 intermediate and mixtures thereof.

    摘要翻译: 在两个平行的单独的反应器中,相对较重和相对较轻的润滑剂进料脱蜡。 用于脱蜡相对轻的原料的反应器包含具有孔开口的结晶沸石,其定义为:(1)正己烷与邻二甲苯的吸附比(以体积百分数计)大于3,该吸附确定 在P / Po为0.1,温度为50℃,正己烷和80℃为邻二甲苯,(2)通过选择性裂解3-甲基戊烷(3MP)的能力优于双 支链的2,3-二甲基丁烷(DMB),1/1重量比的正己烷/ 3-甲基 - 戊烷/ 2,3-二甲基丁烷混合物的1个大气压,比率 在1000°F的温度下测定的常数k3MP / kDMB超过约2,例如天然和合成镁碱沸石,ZSM-22,ZSM-23,ZSM-35及其混合物。 用于脱蜡相对较重的原料的反应器含有具有孔开口的结晶硅铝酸盐沸石,其定义为:(1)正己烷与邻二甲苯的吸附比,基于体积百分比或小于3,该吸附是 在P / Po为0.1,温度为50℃,正己烷和80℃为邻二甲苯时测定,(2)优选选择性裂解3-甲基戊烷(3MP),优于双 支链的2,3-二甲基丁烷(DMB),1/1重量比的正己烷/ 3-甲基 - 戊烷/ 2,3-二甲基丁烷混合物的1个大气压,比率 在1000°F的温度下测定的常数k3MP / KDMB小于约2,(3)大于约1的约束指数值,例如ZSM-5,ZSM-11,ZSM-5 / ZSM-11 中间体及其混合物。

    EMM-3, new crystalline microporous material
    10.
    发明授权
    EMM-3, new crystalline microporous material 有权
    EMM-3,新型结晶微孔材料

    公开(公告)号:US07255849B2

    公开(公告)日:2007-08-14

    申请号:US10863125

    申请日:2004-06-08

    IPC分类号: C01B37/04 C01B37/08

    摘要: EMM-3 (ExxonMobil Material number 3) is a new crystalline microporous material with a framework of tetrahedral atoms connected by atoms capable of bridging the tetrahedral atoms, the tetrahedral atom framework being defined by the interconnections between the tetrahedrally coordinated atoms in its framework. EMM-3 can be prepared in aluminophosphate (AlPO) and metalloaluminophosphate (MeAPO) compositions with the hexamethonium template. It has a unique X-ray diffraction pattern, which identifies it as a new material. EMM-3 is stable to calcination in air, absorbs hydrocarbons, and is catalytically active for hydrocarbon conversion.

    摘要翻译: EMM-3(埃克森美孚材料3号)是一种新的结晶微孔材料,其四面体原子框架由能够桥接四面体原子的原子连接,四面体原子框架由其框架中的四面体配位原子之间的互连定义。 可以在具有六甲铵模板的磷酸铝(AlPO)和金属铝磷酸盐(MeAPO)组合物中制备EMM-3。 它具有独特的X射线衍射图,将其识别为新材料。 EMM-3在空气中煅烧稳定,吸收烃,对烃转化具有催化活性。