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    • 22. 发明专利
    • Carbon monoxide conversion process
    • 碳一氧化碳转化过程
    • JPS59152204A
    • 1984-08-30
    • JP2347783
    • 1983-02-15
    • Hiroshima Gas KkMitsubishi Heavy Ind Ltd
    • ATSUKAWA MASUMINISHIMOTO KOREHIKOSHIMOMURA MASAHITOMANTSUKA YASUSHISAITOU MASAHIROMIHO TADANOBUKANEMITSU TOSHINORI
    • C01B3/16
    • Y02P20/129
    • PURPOSE: To convert a CO-rich reformed gas obtained by the reforming of petroleum to a harmless gaseous mixture of H
      2 and CO
      2 , by mixing the reformed gas with steam and passing the mixture through a monolithic catalyst having a specific structure, thereby reacting CO with steam.
      CONSTITUTION: Petroleum (a), etc. is reformed to a CO-rich gas for city gas by by reforming process 1, and the reformed gas (b) is cooled by the waste-heat recoverer 11. At the same time, the water (g) is heated by the waste-heat recoverer 11. At the same time, the water (g) is heated by the waste-heat recoverer 11 to steam (f), and supplied to a parallel-flow catalytic reactor 3 in the form of a mixed gas C containing 1W4mol of steam based on 1mol of CO. The parallel-flow catalytic reactor contains a monolithic catalyst having a hollow structure comprising two or more catalyst plates placed vertically in parallel, or flow paths 15 made of the catalyst and having triangular, square or polygonal cross-section, curved (e.g. circular or wavy) cross-section or a combination of the curved cross-section and straight cross-section. The residence time of the mixed gas in the catalyst is 0.5W10sec, and the CO in the reformed gas is oxidized with steam to obtain a gaseous mixture of H
      2 and CO
      2 .
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:通过将重整气体与蒸汽混合,将石油重整得到的富含CO的重整气体转化为无害的H 2和CO 2混合气体,将混合物通过具有特定结构的整体式催化剂,使CO与 蒸汽。 构成:通过重整工序1将石油(a)等改造成为城市燃气的富含CO的气体,重整气体(b)由废热回收器11冷却。同时,水 (g)被废热回收器11加热。同时,将水(g)由废热回收器11加热至蒸汽(f),并将其供应到平行流式催化反应器3 形成含有1mol CO的1-4mol蒸汽的混合气体C.平行流催化反应器包含具有中空结构的整体式催化剂,该中空结构包括两个或多个垂直平行放置的催化剂板,或由 催化剂,并且具有三角形,正方形或多边形横截面,弯曲(例如圆形或波浪形)横截面或弯曲横截面和直线横截面的组合。 混合气体在催化剂中的停留时间为0.5-10秒,重整气体中的CO被蒸汽氧化,得到H 2和CO 2的气体混合物。
    • 29. 发明专利
    • Method of liquefying coal
    • 液化方法
    • JPS61123696A
    • 1986-06-11
    • JP24315784
    • 1984-11-20
    • Mitsubishi Heavy Ind Ltd
    • SERA TOSHIKUNISHIMOMURA MASAHITOMASUMOTO HIROMIKAJIMOTO HIKOKUSU
    • C10G1/06C10G1/04
    • PURPOSE: To carry out efficiently coal liquefaction with a high degree of softening and a small amount of evolved H
      2 gas, by subjecting slurry of a hydrogen donating liquefaction solvent and coal to a liquefying reaction at low pressure in a short time, distilling a specific fraction away from the reaction product, and subjecting the fraction to the liquefying reaction again.
      CONSTITUTION: Slurry of the hydrogen donating liquefying solvent 2 and the coal 1 is subjected to a solvolysis liquefaction reaction in the reactor 6 in a short time without using a catalyst and H
      2 . A fraction at 450°C
      + is taken out from the reaction product 9 by the vacuum distillation column 10, the solvent 2 is newly added to the fraction, and the fraction is subjected to the solvolysis liquefaction reaction by the preheater 5' and the liquefaction reactor 6' again. The prepared liquefied material is sent to the vapor-liquid separator 7', where a gas and water are removed from it, the liquefied material is mixed with the liquefied reaction product 11, and fed to the liquefying process of the following stage.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:通过在短时间内将供氢液化溶剂和煤的液体在低压下进行液化反应,通过高效软化和少量逸出的H 2气体高效地进行煤液化,蒸馏出特定部分 远离反应产物,并再次使该馏分进行液化反应。 构成:供氢液化溶剂2和煤1的浆料在短时间内在反应器6中进行溶剂解液化反应,而不使用催化剂和H 2。 通过真空蒸馏塔10从反应产物9中取出450℃的馏分,将新的溶剂2加入到馏分中,并将该馏分用预热器5'进行溶剂解液化反应, 和液化反应器6'。 将制备好的液化物质送入气液分离器7',在其中从中除去气体和水,液化物与液化反应产物11混合,并送入下一阶段的液化过程。
    • 30. 发明专利
    • Catalyst for converting carbon monoxide
    • 用于转化一氧化碳的催化剂
    • JPS61101247A
    • 1986-05-20
    • JP22059684
    • 1984-10-22
    • Mitsubishi Heavy Ind Ltd
    • OBAYASHI YOSHIAKISHIMOMURA MASAHITO
    • C01B3/16B01J23/86C01B3/12
    • Y02P20/52
    • PURPOSE: To reduce cost and to impart activity not inferior to that of an iron oxide/chromium oxide type pellet catalyst, by molding a mixture consisting of iron oxide, chromium oxide and a molding aid into a monolithic shape to form a carbon monoxide converting catalyst.
      CONSTITUTION: Iron oxide and chromium oxide are used as effective catalytic components and one or more of an org. substance such as methyl cellulose, vinyl acetate, polyethylene oxide, polyacrylamide, polyvinyl alcohol or starch, one or more of an inorg. substance such as a glass fiber, a carbon fiber, a metal fiber or a kaoline fiber or a mixture of the aforementioned org. and inorg. substances is used as a molding aid at the time of the molding of a catalyst to be added to said catalytic components to perform mixing and kneading. Subsequently, the resulting mixture is molded into a monolithic shape to obtain a carbon monoxide converting catalyst.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:为了降低成本并赋予不劣于氧化铁/铬氧化物型颗粒催化剂的活性,通过将由氧化铁,氧化铬和成型助剂组成的混合物成型为整体形状以形成一氧化碳转化催化剂 。 构成:氧化铁和氧化铬被用作有效的催化组分和一个或多个组织。 物质如甲基纤维素,乙酸乙烯酯,聚环氧乙烷,聚丙烯酰胺,聚乙烯醇或淀粉,一种或多种惰性物质。 物质如玻璃纤维,碳纤维,金属纤维或高岭土纤维或上述组合物的混合物。 和inorg。 在成型催化剂时,将物质用作模塑助剂以加入到所述催化剂组分中以进行混合和捏合。 随后,将所得混合物模制成整体形状以获得一氧化碳转化催化剂。