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    • 1. 发明授权
    • Manufacturing process of diesel gas oil with high cetane number and low sulfur
    • 具有高十六烷值和低硫的柴油机油的制造工艺
    • US06264827B1
    • 2001-07-24
    • US09384179
    • 1999-08-27
    • Hajime OkazakiKatuhiko IshikawaMichiaki AdachiToshio Waku
    • Hajime OkazakiKatuhiko IshikawaMichiaki AdachiToshio Waku
    • C10G4500
    • C10G65/04
    • A manufacturing process of a diesel gas oil with a high cetane number and a low sulfur, where the cetane number thereof is at least 45, the sulfur content thereof is less than 350 ppm, and the storage stability is superior, from a petroleum distillate oil with a low cetane number and a high sulfur content is provided. The process includes a first stage of contacting hydrogen with a petroleum distillate oil with a particular low cetane number, a particular high sulfur content, and a particular boiling point, in the presence of a catalyst of a porous solid acid carrier carrying a particular hydrogenation-active metals at a particular temperature and pressure to obtain a hydrogenated oil with a cetane number of at least 45 and a sulfur content of less than 350 ppm; and a second stage of contacting the obtained hydrogenated oil with hydrogen in the presence of a catalyst of a porous carrier carrying a hydrogenation-active metal at a particular temperature and pressure to obtain a hydrogenated oil with a superior storage stability without changing the cetane number and the sulfur content.
    • 一种具有高十六烷值和低硫的柴油瓦斯油的制造方法,其十六烷值至少为45,硫含量小于350ppm,储存稳定性优于石油馏出油 具有低十六烷值和高硫含量。 该方法包括在载体上具有特定氢化反应的多孔固体酸载体的催化剂存在下,使氢与具有特定低十六烷值,特定高硫含量和特定沸点的石油馏出油接触的第一阶段, 在特定温度和压力下的活性金属,以获得十六烷值至少为45且硫含量低于350ppm的氢化油; 和在特定温度和压力下,在承载氢化活性金属的多孔载体的催化剂存在下,使所得氢化油与氢接触的第二阶段,以获得具有优异储存稳定性的氢化油,而不改变十六烷值, 硫含量。
    • 2. 发明授权
    • Method of removing acetylenes from C.sub.4 -hydrocarbon mixture
containing butadiene
    • 从含有丁二烯的C4-烃混合物中除去乙炔的方法
    • US4247725A
    • 1981-01-27
    • US31253
    • 1979-04-18
    • Tadashi OhmoriKatuhiko Ishikawa
    • Tadashi OhmoriKatuhiko Ishikawa
    • B01J23/00C07C1/00C07C7/167C07C11/00C07C67/00
    • C07C7/167
    • There is provided a method of selectively hydrogenating acetylenes in a C.sub.4 -hydrocarbon mixture containing butadiene for removing said acetylenes wherein a hydrogen containing gas and the liquid C.sub.4 -hydrocarbon mixture are continuously fed through the upper portion of a reactor filled with catalyst particles carrying one or more precious metals selected from the Group VIII elements of the Periodic Table, the hydrogen containing gas is present in the reactor forming a substantially continuous phase at the hydrogen partial pressure of less than 1.5 kg/cm.sup.2.a, while the C.sub.4 -hydrocarbon mixture is allowed to flow down over the surfaces of the catalyst particles in the liquid form and to react at 5 to 80.degree. C., and the reaction mixture is withdrawn through the bottom of the reactor.
    • 提供了一种在含有丁二烯的C4-烃混合物中选择性氢化乙炔以除去所述乙炔的方法,其中含氢气体和液体C 4 - 烃混合物通过填充有载有一种或多种催化剂颗粒的催化剂颗粒的反应器的上部连续进料, 选自元素周期表第VIII族元素的更贵贵金属,反应器中存在含氢气体,其氢分压小于1.5kg / cm 2,形成基本上连续的相,而C4-烃混合物为 允许以液体形式向下流过催化剂颗粒的表面,并在5至80℃下反应,并将反应混合物通过反应器的底部排出。
    • 3. 发明授权
    • Process for the production of low-sulfur diesel gas oil
    • 生产低硫柴油瓦斯油的工艺
    • US5316658A
    • 1994-05-31
    • US914847
    • 1992-07-15
    • Masaru UshioTamio NakanoMinoru HatayamaKatuhiko IshikawaMasaru Sato
    • Masaru UshioTamio NakanoMinoru HatayamaKatuhiko IshikawaMasaru Sato
    • B01J23/85C10G45/04C10G65/04F02B3/06
    • C10G65/04C10G2400/04F02B3/06
    • A process for the production of a low-sulfur diesel gas oil having a sulfur content of 0.05% by weight or lower and having a Saybolt color number of -10 or higher, from a petroleum distillate having a sulfur content of 0.1 to 2.0% by weight and having an inferior color and inferior oxidation stability comprises contacting the petroleum distillate with hydrogen in the presence of a hydro-treating catalyst which has at least one metal supported on said porous carrier, at a temperature of 350.degree. to 450.degree. C., and a pressure of 45 to 100 kg/cm.sup.2 in the first step to thereby produce materials having a sulfur content of 0.05% by weight or lower, and contacting further the materials issued from the first step with hydrogen in the presence of a hydro-treating catalyst which has at least one metal supported on said porous carrier, at a temperature of 200.degree. to 300.degree. C., and a pressure of 45 to 100 kg/cm.sup.2 in the second step to thereby produce the finished low-sulfur diesel gas oil.
    • 一种硫含量为0.05重量%以下,Saybolt色数为-10以上的低硫柴油瓦斯油,其硫含量为0.1〜2.0%的石油馏分,由 重量较差,具有较差的颜色和较差的氧化稳定性包括在350℃至450℃的温度下,在至少一种负载在所述多孔载体上的金属的氢化处理催化剂存在下使石油馏分与氢气接触, 并且在第一步中的压力为45-100kg / cm2,从而制备硫含量为0.05重量%以下的材料,并在第一步骤中发出的材料与氢气在氢化处理 催化剂,其在至少一种负载在所述多孔载体上的金属,在200℃至300℃的温度和45至100kg / cm 2的压力下在第二步骤中,从而生产成品的低硫柴油机油 。