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    • 1. 发明授权
    • Method for producing hydrocarbons by Fischer-Tropsch process
    • 通过费 - 托法生产烃的方法
    • US06924316B2
    • 2005-08-02
    • US10476131
    • 2002-06-17
    • Osamu IwamotoShigenori NakashizuKinjiro SaitoTakashi Suzuki
    • Osamu IwamotoShigenori NakashizuKinjiro SaitoTakashi Suzuki
    • B01J23/656B01J35/00B01J35/02B01J35/10B01J37/02C10G2/00C07C27/00
    • C10G2/333B01J23/6562B01J35/0026B01J35/023B01J35/10B01J35/1014B01J35/1019B01J37/0205
    • A method for producing hydrocarbons, comprising: (I) subjecting to a reduction treatment a catalyst comprising a carrier having provided thereon: 0.1 to 10% by mass of at least one metal selected from an alkali metal, an alkaline earth metal, a rare earth metal and the Group III in the periodic table and 1 to 30% by mass of ruthenium, each based on the catalyst weight, the carrier comprising an aluminum oxide and a manganese oxide having an average number of charges of manganese of exceeding Mn2+, and the catalyst having a specific surface area of from 60 to 350 m2/g and a bulk density of from 0.8 to 1.8 g/ml; (II) dispersing the catalyst in liquid hydrocarbons in a concentration of from 1 to 50 w/v %; and (III) bringing the catalyst into contact with a gas mixture comprising hydrogen and carbon monoxide at a pressure of from 1 to 10 MPa, and (i) at a reaction temperature of from 170 to 300° C. under such conditions that carbon dioxide is substantially absent, or (ii) at a reaction temperature of from 200 to 350° C. under such conditions that carbon dioxide coexists in an amount of from 0.5 to 50% based on the total pressure of the hydrogen and the carbon monoxide.
    • 一种碳氢化合物的制造方法,其特征在于,含有:(I)还原处理含有载体的催化剂:0.1〜10质量%的选自碱金属,碱土金属,稀土 金属和周期表中的III族和1〜30质量%的钌,各自以催化剂重量计,载体包含氧化铝和氧化锰,其平均锰电荷数超过Mn < 2 +,比表面积为60〜350m 2 / g,堆积密度为0.8〜1.8g / ml的催化剂; (II)将催化剂分散在浓度为1至50w / v%的液体烃中; 和(III)使催化剂与包含氢气和一氧化碳的气体混合物在1至10MPa的压力下接触,和(i)在170-300℃的反应温度下,在二氧化碳 基本上不存在,或(ii)在200-350℃的反应温度下,在二氧化碳基于氢气和一氧化碳的总压力共存0.5至50%的量的条件下。
    • 4. 发明授权
    • Catalyst compositions for hydrotreating of hydrocarbon oils and process
for manufacturing the same.
    • 用于加氢处理烃油的催化剂组合物及其制造方法。
    • US5444033A
    • 1995-08-22
    • US254424
    • 1994-06-06
    • Kazushi UsuiShigenori NakashizuKentarou Ishida
    • Kazushi UsuiShigenori NakashizuKentarou Ishida
    • B01J23/85B01J35/00C10G45/08B01J21/02B01J23/00
    • B01J23/85B01J35/0006C10G45/08B01J35/0086
    • A catalyst composition for hydrotreating of hydrocarbon oils is disclosed. The composition comprises a Group VIB metal in an amount of 5-30% by weight, as oxide, and a Group VIII metal in an amount of 1-10% by weight, as oxide, wherein said Group VIB metal and said Group VIII metal are distributed with a concentration gradient which becomes higher from the surface toward the center of a catalyst particle according to the formulas, 0.9>h.sub.2 /h.sub.1 .gtoreq.0, wherein h.sub.1 is the Group VIB metal concentration at the center of the catalyst particle and h.sub.2 at the outermost surface of the catalyst particle, and 0.9>h.sub.4 /h.sub.3 .gtoreq.0, wherein h.sub.3 is the Group VIII metal concentration at the center of the catalyst particle and h.sub.4 at the outermost surface of the catalyst particle. The catalyst composition can be used for hydrodesulfurization, hydrodenitrification, hydrodemetalization, and hydrocracking of topping or vacuum distillates and residues, as well as hydrotreatments for the refining of such fractions as kerosene, gas oil, wax, and lubricating oil. It exhibits a high activity for a prolonged period of time. Processes for manufacturing the catalyst composition are also disclosed.
    • 公开了一种用于加氢处理烃油的催化剂组合物。 组合物包含5-30重量%的氧化物的ⅤB族金属和1-10重量%的Ⅷ族金属作为氧化物,其中所述VIB族金属和所述VIII族金属 以0.9> h2 / h1> / = 0的方式从催化剂颗粒的表面朝向中心变得更高的浓度梯度分布,其中h1是催化剂颗粒中心处的VIB族金属浓度, h2在催化剂颗粒的最外表面,0.9> h4 / h3> = 0,其中h3是催化剂颗粒中心处的Ⅷ族金属浓度,在催化剂颗粒的最外表面是h4。 催化剂组合物可用于加氢脱硫,加氢脱氮,加氢脱矿,顶部或真空馏分和残余物的加氢裂化,以及用于精馏煤油,瓦斯油,蜡和润滑油等馏分的加氢处理。 它长时间展现出高活性。 还公开了制备催化剂组合物的方法。
    • 5. 发明授权
    • Catalyst composition for hydrogenation of heavy hydrocarbon oil and
process for producing the catalyst
    • 用于重质烃油氢化的催化剂组合物和用于生产催化剂的方法
    • US4981832A
    • 1991-01-01
    • US374805
    • 1989-07-03
    • Kinya TawaraKazuyoshi KudohKazushi UsuiTomohiro YoshinariShigenori Nakashizu
    • Kinya TawaraKazuyoshi KudohKazushi UsuiTomohiro YoshinariShigenori Nakashizu
    • B01J23/88B01J23/883B01J35/02B01J35/10C10G45/04C10G45/06C10G45/08
    • B01J35/10B01J23/883C10G45/04B01J35/1042B01J35/1061B01J35/108
    • A catalyst composition for the hydrogenation of heavy hydrocarbon oil, where the catalyst composition comprises at least one active ingredient for hydrogenation supported on a porous alumina carrier and has the following characteristics: (1) the total volume of the pores therein is from 0.4 to 1.0 ml/g; (2) the mean pore diameter of pores having a pore diameter of from 5 to 400 .ANG. is from 60 to 140 .ANG.; (3) the volume of pores having a pore size within .+-.25% of the mean pore diameter of pores having a pore diameter of from 5 to 400 .ANG. is from 60 to 98% of the volume of pores having a pore diameter of from 5 to 400 .ANG.; (4) the volume of pores having a pore diameter of from 400 to 5000 .ANG. is from 2 to 9% of the total volume of the entire pores; (5) the ratio (mm.sup.2 /mm.sup.3) of the outer surface area of a molded catalyst powder to the volume thereof is from 4 to 8; and (6) all points in the interior of the molded catalyst particle are positioned within 0.05 to 0.6 mm from the outer surface thereof. A process for producing the catalyst composition is also disclosed. Further, a process for hydrogenating heavy hydrocarbon oil, which comprises contacting the heavy hydrocarbon oil with the catalyst composition in the presence of hydrogen is disclosed.
    • 一种用于重质烃油氢化的催化剂组合物,其中催化剂组合物包含至少一种负载在多孔氧化铝载体上的用于氢化的活性成分,并具有以下特征:(1)其中的孔的总体积为0.4-1.0 ml / g; (2)孔径为5至400埃的孔的平均孔径为60至140纳米; (3)孔径为孔径为5〜400的孔的平均孔径的+/- 25%以内的孔的体积为孔径为孔的体积的60〜98% 从5到400 ANGSTROM; (4)孔径为400〜5000的孔的体积为整个孔的总体积的2〜9% (5)成型催化剂粉末的外表面积与其体积的比(mm2 / mm3)为4〜8; 和(6)模塑催化剂颗粒内部的所有点位于距其外表面0.05至0.6mm的范围内。 还公开了一种制备催化剂组合物的方法。 此外,公开了一种用于氢化重质烃油的方法,其包括在氢气存在下使重质烃油与催化剂组合物接触。