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    • 31. 发明专利
    • Method for manufacturing catalytic cracking catalyst
    • 制备催化裂化催化剂的方法
    • JP2012061408A
    • 2012-03-29
    • JP2010207135
    • 2010-09-15
    • Cosmo Oil Co LtdJapan Petroleum Energy Centerコスモ石油株式会社一般財団法人石油エネルギー技術センター
    • SAKA YUJICHIYODA NORIHITO
    • B01J29/08C10G11/05
    • PROBLEM TO BE SOLVED: To provide a method for manufacturing a catalytic cracking catalyst of hydrocarbon oil having high cracking activity and capable of manufacturing FCC gasoline having a high octane number.SOLUTION: The method for manufacturing the catalytic cracking catalyst includes a process for preparing an aqueous slurry containing zeolite having a sodalite cage structure, a silica sol, monobasic aluminum phosphate and a clayey mineral in a predetermined ratio, a spray drying process for spray-drying the aqueous slurry obtained in the aqueous slurry preparing process at a predetermined temperature, a washing process for washing the product obtained in the spray drying process, and a drying process for drying the product after the washing process. A heat treatment process for heat-treating the product obtained in the spray drying process at a predetermined temperature for predetermined time is contained between the spray drying process and the washing process for washing the product obtained in the spray drying process.
    • 要解决的问题:提供一种制造具有高裂化活性的烃油的催化裂化催化剂的方法,并且能够制造具有高辛烷值的FCC汽油。 解决方案:催化裂化催化剂的制造方法包括以规定比例制备含有钠盐笼结构的沸石的含水浆料,二氧化硅溶胶,一磷酸铝和粘土矿物的方法,喷雾干燥法 将在水性浆料制备方法中获得的含水浆料在预定温度下进行喷雾干燥,洗涤在喷雾干燥过程中获得的产物的洗涤过程,以及在洗涤过程之后干燥产物的干燥过程。 在喷雾干燥过程和用于洗涤在喷雾干燥过程中获得的产物的洗涤过程之间包含用于在预定温度下在喷雾干燥过程中获得的产物热处理预定时间的热处理方法。 版权所有(C)2012,JPO&INPIT
    • 33. 发明专利
    • Membrane separation type reactor, membrane separation type hydrogen production apparatus and method for producing hydrogen
    • 膜分离型反应器,膜分离型氢生产装置​​及其生产方法
    • JP2011195393A
    • 2011-10-06
    • JP2010065087
    • 2010-03-19
    • Japan Petroleum Energy CenterJx Nippon Oil & Energy CorpJx日鉱日石エネルギー株式会社一般財団法人石油エネルギー技術センター
    • MAEDA TAKASHINEGISHI EIJIOGAWA MINORU
    • C01B3/38B01D53/22B01D69/10B01D71/02C01B3/56
    • Y02P20/52
    • PROBLEM TO BE SOLVED: To provide a membrane separation type reactor which enables to perform efficient steam reforming reaction and efficient separation and purification of hydrogen with a hydrogen separation membrane in the same reactor, resulting in production of hydrogen with compactness and in high yield.SOLUTION: The membrane separation type reactor 1 includes a hydrogen separation membrane tube 2 having a hydrogen separation membrane on an outer surface thereof, an inner tube 3 disposed on the outside of the hydrogen separation membrane tube 2, an intermediate tube 4 disposed on the outside of the inner tube 3, and an outer tube 5 disposed on the outside of the intermediate tube 4, wherein the space between the hydrogen separation membrane tube 2 and the inner tube 3 communicates with the space between the inner tube 3 and the intermediate tube 4 at one end of the membrane separation type reactor 1, the space between the inner tube 3 and the intermediate tube 4 communicates with the space between the intermediate tube 4 and the outer tube 5 at the other end of the membrane separation type reactor 1, the space between the intermediate tube 4 and the outer tube 5 is packed with a steam reforming catalyst, and the space between the hydrogen separation membrane tube 2 and the inner tube 3 is packed with a steam reforming catalyst or a shift reaction catalyst.
    • 要解决的问题:提供一种膜分离型反应器,其能够在同一反应器中使用氢分离膜进行有效的蒸汽重整反应和有效的氢分离和纯化,从而产生具有致密性和高产率的氢。 膜分离型反应器1包括在其外表面具有氢分离膜的氢分离膜管2,设置在氢分离膜管2的外侧的内管3,设置在氢分离膜管2的外侧的中间管4 内管3和设置在中间管4的外侧的外管5,其中氢分离膜管2和内管3之间的空间与内管3和中间管4之间的空间连通, 膜分离型反应器1的一端,内管3和中间管4之间的空间连通 在隔膜式反应器1的另一端处的中间管4和外管5之间的空间,中间管4和外管5之间的空间填充有蒸汽重整催化剂,并且氢气之间的空间 分离膜管2和内管3填充有蒸汽重整催化剂或转移反应催化剂。
    • 37. 发明专利
    • Method for producing catalyst for decomposing hydrocarbon oil, and method for decomposing hydrocarbon oil
    • 用于生产用于分解油料的催化剂的方法,以及用于分解油气的方法
    • JP2013193026A
    • 2013-09-30
    • JP2012062418
    • 2012-03-19
    • Jx Nippon Oil & Energy CorpJx日鉱日石エネルギー株式会社Japan Petroleum Energy Center一般財団法人石油エネルギー技術センター
    • FURUTA TOMOHITOTORAI MASATAKA
    • B01J23/30B01J37/04B01J37/08C10G11/04C10G11/20C10G47/32
    • PROBLEM TO BE SOLVED: To provide a method for producing a catalyst for decomposing hydrocarbon oil, which is a catalyst used in decomposing the hydrocarbon oil in the presence of water, containing a composite metal oxide as a catalytically active component and high in mechanical strength and stability in a reaction system, and to provide a method for decomposing the hydrocarbon oil using the catalyst for decomposing the hydrocarbon oil, prepared using the producing method.SOLUTION: A method is provided for producing a catalyst for decomposing hydrocarbon oil, used for decomposing the hydrocarbon oil, wherein the catalyst for decomposing the hydrocarbon oil includes a composite metal oxide. The method for producing the catalyst for decomposing the hydrocarbon oil includes a mixing step of preparing a mixture of the composite metal oxide and an acidic solution containing zinc, and a baking step of baking the mixture to prepare the catalyst for decomposing the hydrocarbon oil. A method for decomposing the hydrocarbon oil includes bringing the hydrocarbon oil into contact with the catalyst for decomposing the hydrocarbon oil in the presence of water to decompose the hydrocarbon oil.
    • 要解决的问题:提供一种用于分解烃油的方法,所述催化剂是用于在水存在下分解烃油的催化剂,其含有复合金属氧化物作为催化活性成分并且机械强度高, 稳定性,并且提供使用使用该制造方法制备的烃油分解用催化剂来分解烃油的方法。解决方案:提供一种用于分解烃油的催化剂的制造方法,其用于分解烃油 烃油,其中用于分解烃油的催化剂包括复合金属氧化物。 制造用于分解烃油的催化剂的方法包括制备复合金属氧化物和含锌的酸性溶液的混合物的混合步骤,以及烘烤步骤以制备用于分解烃油的催化剂。 分解烃油的方法包括使烃油与用于在水存在下分解烃油的催化剂接触以分解烃油。