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    • 4. 发明授权
    • Method for the production of hydrocarbon fuels with ultra-low sulfur content
    • 用于生产超低硫含量的烃类燃料的方法
    • US06673236B2
    • 2004-01-06
    • US09940485
    • 2001-08-29
    • Maria StanciulescuMichio Ikura
    • Maria StanciulescuMichio Ikura
    • C10G2700
    • C10G27/14C10G27/12C10G67/12
    • The present invention provides a method for producing hydrocarbon fuels with ultra-low levels of sulfur. The method involves catalytic oxidation of the sulfurous compounds within the hydrocarbon fuel, followed by extraction of the oxidized (and polarized) sulfurous compounds using a polar solvent. The present invention teaches the involvement of ethanol during catalytic oxidation. In this way, the oxidation catalyst has a dual-role in the oxidation process: firstly the catalyst directly oxidizes the sulfurous compounds, and secondly the oxidation catalyst converts of a small portion of the alcohol to the corresponding peroxy acid, which also helps to drive the oxidation process.
    • 本发明提供一种生产具有超低含量硫的烃燃料的方法。 该方法包括在烃燃料内的亚硫酸化合物的催化氧化,然后使用极性溶剂萃取氧化的(和极化的)亚硫酸化合物。 本发明教导了乙醇在催化氧化过程中的参与。 以这种方式,氧化催化剂在氧化过程中具有双重作用:首先催化剂直接氧化亚硫​​酸化合物,其次氧化催化剂将一小部分醇转化为相应的过氧酸,这也有助于驱动 氧化过程。
    • 6. 发明申请
    • PRODUCTION OF HIGH-CETANE DIESEL PRODUCT
    • 生产高档柴油产品
    • US20130220881A1
    • 2013-08-29
    • US13819474
    • 2010-09-03
    • Michio Ikura
    • Michio Ikura
    • C10L10/12
    • C10L10/12B01J21/063B01J23/6482B01J35/04B01J37/0215C10G27/14C10G2300/1055C10G2300/202C10G2300/307C10G2300/44C10G2400/04C10L1/08
    • Exemplary embodiments of the invention provide a process of increasing the cetane number rating of a diesel oil feedstock. The process involves reacting a diesel fuel feedstock in liquid form with ozone in gaseous form in the presence of an alcohol having two or more carbon atoms and at least one polar solvent different from the alcohol, thereby forming an ozonated diesel oil containing oxidized byproducts, wherein the alcohol and said polar solvent are employed in amounts totaling no more than about 10 vol. % of the feedstock. The oxidized byproducts are then separated from the ozontated diesel oil to produce a hydrocarbon product of increased cetane number rating relative to the feedstock oil. The product can be used as a diesel fuel or as a diesel fuel extender mixed with conventional diesel fuel of low cetane number.
    • 本发明的示例性实施方案提供了增加柴油原料的十六烷值等级的方法。 该方法包括在具有两个或多个碳原子的醇和至少一种不同于醇的极性溶剂的存在下,使液体形式的柴油燃料原料与气态臭氧反应,从而形成含有氧化副产物的臭氧化柴油,其中 醇和所述极性溶剂的用量总计不超过约10体积%。 %的原料。 然后将氧化的副产物与臭氧柴油分离以产生相对于原料油增加的十六烷值等级的烃产物。 该产品可用作柴油燃料或与低十六烷值的常规柴油混合的柴油燃料增量剂。
    • 7. 发明授权
    • Deashing of heavy hydrocarbon residues
    • 重烃残渣脱水
    • US5120428A
    • 1992-06-09
    • US711031
    • 1991-06-06
    • Michio IkuraNorman E. CookeMarc HalevyMartin E. Weber
    • Michio IkuraNorman E. CookeMarc HalevyMartin E. Weber
    • C10G31/08
    • C10G31/08
    • A process is described for removing mineral or ash constituents from heavy hydrocarbon residues, such as those resulting from coal-oil coprocessing, residue hydrocracking or coal liquifaction. The process comprises the steps of: (a) intimately mixing the ash-containing heavy hydrocarbon oil residue with a surfactant and a pH-conditioned aqueous solution under high shear mixing conditions to disperse the ash-containing residue in the aqueous phase thereby creating a fine oil-in-water emulsion, (b) adding a strong oxidizing agent to the emulsion to thereby break the emulsion and release the ash into the aqueous phase and (c) separating the ash-containing aqueous phase from the oil phase. The HLB method for characterizing the emulsion forming activity of a surface active material is described in M. J. Rosen, Surfactants and Interfacial Phenomena, John Wiley & Sons, New York (1989), incorporated herein by reference.
    • 描述了从重质烃残渣中除去矿物或灰分成分的方法,例如由煤 - 油协同处理,残渣加氢裂化或煤液化产生的那些。 该方法包括以下步骤:(a)在高剪切混合条件下,将含灰分的重质烃油残余物与表面活性剂和pH调节的水溶液充分混合,以将灰分残留物分散在水相中,从而产生细微的 水包油乳液,(b)向乳液中加入强氧化剂,从而破坏乳液并将灰分释放到水相中,(c)将含灰分的水相与油相分离。 用于表征表面活性材料的乳液形成活性的HLB方法描述在M.J.Rosen,Surfactants and Interfacial Phenomena,John Wiley&Sons,New York(1989)中,其通过引用并入本文。
    • 9. 发明申请
    • Production of biodiesel from triglycerides via a thermal route
    • 通过热路线从甘油三酸酯生产生物柴油
    • US20070144060A1
    • 2007-06-28
    • US11638348
    • 2006-12-14
    • Michio Ikura
    • Michio Ikura
    • C10L1/18
    • C11C3/003C10G3/40C10G2300/1014C10G2300/1018C10G2300/807C10L1/026C11C3/00Y02E50/13Y02P30/20
    • A method is presented for producing biodiesel from a triglyceride feedstock. The feedstock is pretreated by thermal cracking or rapid pyrolysis to convert triglycerides to form a middle distillate fraction rich in fatty acids. The middle distillate fraction is then esterified the in the presence of an alcohol and a catalyst to produce a biodiesel stream. The biodiesel stream can be treated with a basic solution to convert unesterified free fatty acids to non-foaming metallic soaps, which can be removed by known means. A method is also provided for producing a biodiesel/naphtha mixture, in which a triglyceride feedstock is pretreated by thermal cracking or rapid pyrolysis to produce a middle distillate fraction, a naphtha stream and a gas stream. The naphtha stream and the middle distillate fraction are then esterified to produce a mixed biodiesel/naphtha stream, which can be treated with a basic solution to convert unesterified free fatty acids to non-foaming metallic soaps, which are then removed by known means.
    • 提出了从甘油三酯原料生产生物柴油的方法。 原料通过热裂解或快速热解预处理以转化甘油三酯以形成富含脂肪酸的中间馏分。 然后将中间馏分馏分在醇和催化剂的存在下酯化,生成生物柴油流。 可以用碱性溶液处理生物柴油流,以将未酯化的游离脂肪酸转化为不发泡金属皂,其可以通过已知方法除去。 还提供了一种用于生产生物柴油/石脑油混合物的方法,其中通过热裂解或快速热解预处理甘油三酯原料以产生中间馏分馏分,石脑油流和气流。 然后将石脑油流和中间馏分馏分酯化以产生混合的生物柴油/石脑油流,其可用碱性溶液处理以将未酯化的游离脂肪酸转化为非发泡金属皂,然后通过已知方法除去。
    • 10. 发明授权
    • Oil/coal coprocessing in which agglomerated coal forms part of feedstock
    • 油/煤协同加工,其中附聚煤形成原料的一部分
    • US5350430A
    • 1994-09-27
    • US190984
    • 1994-02-03
    • Richard D. ColemanFloyd N. TollThomas W. McCrackenC. Edward CapesMichio Ikura
    • Richard D. ColemanFloyd N. TollThomas W. McCrackenC. Edward CapesMichio Ikura
    • C10G47/00C10L5/06C10L9/00
    • C10L5/06C10G47/00
    • An improved process is described for agglomerating ground coal in which a bridging oil is used as the agglomerating vehicle. This bridging oil is a mixture of a heavy gas oil obtained from coal/oil coprocessing and a heavy hydrocarbon oil, such as bitumen or heavy oil, preferably mixed in the proportion of about 23-40% heavy hydrocarbon oil and 60-77% heavy gas oil. The agglomerated product is mixed with additional heavy oil or bitumen and it becomes the feedstock to a coal/oil coprocessor, with heavy gas oil being formed as one of the product streams. At least part of this heavy gas oil product stream is recycled to the agglomeration stage as the heavy gas oil component of the bridging oil. This agglomeration procedure has the advantage of providing an agglomerate of excellent quality, while carrying out the agglomeration in a short time at ambient temperature and using less than 10% by weight of bridging oil.
    • 描述了一种改进的方法,用于将其中使用桥连油的研磨煤作为附聚载体。 这种桥连油是从煤/油协同加工和重质烃油(例如沥青或重油)获得的重质瓦斯油的混合物,优选以约23-40%重质烃油和60-77%重量的比例混合 瓦斯油。 聚集的产物与另外的重油或沥青混合,并且它成为煤/油协同处理器的原料,重质瓦斯油形成为产物流之一。 该重质瓦斯油产品流的至少一部分作为桥联油的重质瓦斯油组分再循环至附聚阶段。 这种附聚方法的优点是提供优异品质的附聚物,同时在环境温度下在短时间内进行聚集并使用小于10重量%的桥连油。