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    • 2. 发明授权
    • Catalytic dewaxing of light and heavy oils in dual parallel reactors
    • 双重并联反应器中轻油和重油的催化脱蜡
    • US4605488A
    • 1986-08-12
    • US733339
    • 1985-05-13
    • Arthur W. ChesterWilliam E. GarwoodJames C. Vartuli
    • Arthur W. ChesterWilliam E. GarwoodJames C. Vartuli
    • C10G65/10B01J29/00B01J29/40B01J29/65C10G45/64C10G65/00C10G65/16C10G73/02C10G65/18C10G65/12C10G67/02
    • C10G65/00C10G45/64C10G65/16
    • 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.
    • 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。
    • 8. 发明授权
    • Conversion of synthesis gas to high octane predominantly olefinic naphtha
    • 合成气转化为高辛烷值主要是烯烃石脑油
    • US4172843A
    • 1979-10-30
    • US926987
    • 1978-07-21
    • Francis G. DwyerWilliam E. Garwood
    • Francis G. DwyerWilliam E. Garwood
    • B01J29/40B01J29/46C07C1/04
    • B01J29/46B01J29/40C07C1/044B01J2229/26B01J2229/42C07C2529/072
    • An improved method is disclosed for converting synthesis gas to hydrocarbon mixtures wherein the syngas is contacted with a special catalyst comprising a crystalline zeolite having a silica-to-alumina ratio of greater than 200 (including zeolites containing essentially no alumina) and an (R.sub.2 O+ M.sub.2 /.sub.n O): SiO.sub.2 ratio of less than 1.1:1 where M is a metal other than a metal of Group IIIA, n is the valence of said metal, and R is an alkyl ammonium radical, said organosilicate being characterized by a specified x-ray diffraction pattern. In a specific embodiment of this invention, synthesis gas is contacted with a catalyst comprising an intimate mixture of said crystalline zeolite catalyst and iron-containing, Fischer-Tropsch catalyst to produce a liquid hydrocarbon product having a boiling range of less than 400.degree. F. at a 90 percent overhead and being a predominantly olefinic product, wherein the structure of the olefins is substantially branched chain with internally-positioned double bonds.
    • 公开了一种用于将合成气转化为烃混合物的改进方法,其中合成气与包含二氧化硅与氧化铝之比大于200的结晶沸石(包括基本上不含氧化铝的沸石)和(R2O + M2 / nO):SiO 2比小于1.1:1,其中M是除IIIA族金属以外的金属,n是所述金属的化合价,R是烷基铵基团,所述有机硅酸盐的特征在于指定的x- 射线衍射图。 在本发明的具体实施方案中,使合成气与包含所述结晶沸石催化剂和含铁的费 - 托催化剂的紧密混合物的催化剂接触,以产生沸点低于400°F的液体烃产物。 在90%的开销下,并且主要是烯烃产物,其中烯烃的结构基本上是支链的,内部定位的双键。