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    • 2. 发明授权
    • Catalytic process for dewaxing hydrocarbon feedstocks
    • 用于脱蜡烃原料的催化方法
    • US5332490A
    • 1994-07-26
    • US952037
    • 1992-09-28
    • Robert J. Taylor, Jr.Pei-Shing E. DaiRandall H. PettyJoseph A. Durkin
    • Robert J. Taylor, Jr.Pei-Shing E. DaiRandall H. PettyJoseph A. Durkin
    • C10G45/64C10G47/20
    • C10G45/64C10G2400/10
    • A process for hydrodewaxing a hydrocarbon feedstock boiling above about 350.degree. F. by contacting the feedstock and hydrogen at a hydrogen pressure of from about 300 to about 2000 psig at a temperature of 400.degree. to 900.degree. F. and at a space velocity of about 0.1 to about 10.0 LHSV with a catalyst comprising about 0.1 to about 23 wt. % of an oxide of a Group VIII metal, such as nickel, or an oxide of a Group VIB metal, such as molybdenum; supported on a porous alumina support containing about 50 to about 85 wt. % of a crystalline alumino-silicate zeolite of the ZSM-5 type based on the weight of the support. The catalyst is further characterized by having greater than 60% of the pore volume between 45-600 Angstroms in the 70-200 Angstrom range. The process is especially useful for dewaxing lubricating oil basestocks.
    • 通过使原料和氢气在约300至约2000psig的氢气压力下在400-900°F的温度和大约的空间速度下接触原料和氢气,将沸点高于约350°F的烃原料加氢脱蜡的方法。 0.1至约10.0LHSV,催化剂包含约0.1至约23重量% %的Ⅷ族金属的氧化物,例如镍,或ⅥB族金属的氧化物如钼; 负载在含有约50至约85重量%的多孔氧化铝载体上。 %的基于载体重量的ZSM-5型结晶铝硅酸盐沸石。 该催化剂的特征还在于在70-200埃范围内具有大于60%的孔体积在45-600埃之间。 该方法对于脱蜡润滑油基础油料特别有用。
    • 6. 发明授权
    • Hydrotreatment process employing catalyst with specified pore size
distribution
    • 使用具有规定孔径分布的催化剂的加氢处理方法
    • US4941964A
    • 1990-07-17
    • US168095
    • 1988-03-14
    • Pei-Shing E. DaiDavid E. Sherwood, Jr.Burton H. BartleyRandall H. Petty
    • Pei-Shing E. DaiDavid E. Sherwood, Jr.Burton H. BartleyRandall H. Petty
    • B01J35/10C10G45/08
    • C10G45/08B01J35/1019B01J35/1042B01J35/1061B01J35/108
    • A process for the hydrotreatment of a sulfur and metal-containing hydrocarbon feed comprises contacting said feed with hydrogen and a catalyst in a manner such that the catalyst is maintained at isothermal conditions and is exposed to a uniform quality of feed, where said catalyst has a composition comprising 3.0-5.0 wt. % of an oxide of a Group VIII metal, 14.5-24.0 wt. % of an oxide of a Group VIB metal and 0-2.0 wt. % of an oxide of phosphorus supported on a porous alumina support, and said catalyst is further characterized by having a total surface area of 150-210 m.sup.2 /g and a total pore volume of 0.50-0.75 cc/g with a pore diameter distribution such that micropores having diameters of 100-160A constitute 70-85% of the total pore volume of said catalyst and macropores having diameters of greater than 250A constitute 5.5-22.0% of the total pore volume of said catalyst. The process of the instant invention is particularly effective in achieving desired levels of hydrodesulfurization in the fraction of hydrotreated/hydrocracked petroleum resid product having a boiling point greater than 1000.degree. F.
    • 用于加氢处理含硫和含金属的烃进料的方法包括使所述进料与氢气和催化剂以使得催化剂保持在等温条件并暴露于均匀质量的进料的方式接触,其中所述催化剂具有 组合物包含3.0-5.0重量% %的VIII族金属的氧化物,14.5-24.0wt。 %VIB族金属的氧化物和0-2.0wt。 负载在多孔氧化铝载体上的磷氧化物的%,并且所述催化剂的特征还在于总表面积为150-210m 2 / g,总孔体积为0.50-0.75cc / g,孔直径分布如 直径为100-160A的微孔构成所述催化剂的总孔体积的70-85%,直径大于250A的大孔构成所述催化剂总孔体积的5.5-22.0%。 本发明的方法在沸点大于1000°F的加氢处理/加氢裂化石油渣产物馏分中达到所需加氢脱硫水平特别有效。
    • 9. 发明授权
    • Wax conversion process
    • 蜡转化过程
    • US5370788A
    • 1994-12-06
    • US992669
    • 1992-12-18
    • Pei-Shing E. DaiJoseph A. DurkinBobby R. Martin
    • Pei-Shing E. DaiJoseph A. DurkinBobby R. Martin
    • B01J23/85B01J35/10C10G45/60C10G73/38C10G47/20
    • B01J23/85B01J35/1019B01J35/1038B01J35/1066B01J35/108C10G2400/10
    • Charge waxy hydrocarbon is converted to lube oil base stock by hydrotreating in the presence of catalyst characterized by its ability to convert a waxy hydrocarbon distillate of high pour point to a hydrocarbon product of reduced pour point and high viscosity index, suitable for use as a lube oil base stock, which comprises a support containing about 2-50 w % silica and 50-98 w % alumina, bearing 2-10 w % of a non-noble Group VIII metal, as metal, metal oxide, or metal sulfide, about 8-20 w % of a Group VI-B metal, as metal, metal oxide, or metal sulfide, less than 0.5% halogen; and 0-2 w % of phosphorus, the atom ratio of Group VIII metal to Group VI-B metal being about 0.3-2:1, said catalyst being characterized by a micropore mode of about 60-130 .ANG. diameter, a Total Surface Area of about 150-300 m.sup.2 /g, a Total Pore Volume of about 0.45-0.9 cc/g and a Pore Volume of pores with pore diameter >500 .ANG. of about 0.02-0.25 cc/g.
    • 通过在催化剂存在下加氢处理将蜡状碳氢化合物转化为润滑油基础油,其特征在于其将高倾点的蜡质烃馏分转化成具有降低倾点和高粘度指数的烃产物的能力,适合用作润滑剂 油基原料,其包含含有约2-50重量%二氧化硅和50-98重量%氧化铝的载体,其含有2-10重量%的非贵金属Ⅷ族金属作为金属,金属氧化物或金属硫化物,约 8-20重量%的VI-B族金属,金属,金属氧化物或金属硫化物,小于0.5%的卤素; 和0-2w%的磷,第Ⅷ族金属与Ⅵ-B族金属的原子比为约0.3-2:1,所述催化剂的特征在于微孔模式为约60-130直径,总表面积 约150-300m 2 / g,总孔体积为约0.45-0.9cc / g,孔径>500的孔的孔体积为约0.02-0.25cc / g。