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The desulfurization catalytic converter of the heavy oil, being the catalytic converter which it hydrogenates desulfurizes the desulfurization mannered null normal pressure

机译:重油的脱硫催化转化器是加氢脱硫的催化转化器,以脱硫方式达到零常压。

摘要

PROBLEM TO BE SOLVED: To obtain a hydrodesulfurization catalyst capable of removing a sulfur compound in a heavy oil fraction over a long period of time with high efficiency, to provide a manufacturing method therefor, and a method for hydrodesulfurization using the catalyst.;SOLUTION: The catalyst carries at least 8-25 mass% of one kind of metal selected from the group 6 elements of the Periodic Table on a catalyst basis in terms of the oxide, at least 1-8 mass% of one kind of metal selected from the group 8 elements of the Periodic Table, 0.5-6 mass% of phosphorus, and 1-14 mass% of carbon on the catalyst basis on an alumina carrier. Physical properties of the catalyst after baked at 500°C are as follows: the specific surface area is 180-330 m2/g, the pore volume is 0.4-0.7 ml/g, and the average pore diameter is 7-12 nm. A solution containing the above components is carried on the alumina carrier, and is dried at 200°C or lower. The raw material oil is contacted with the catalyst on the condition that 4-18 MPa of the hydrogen partial pressure, 320-410°C of the temperature, and 0.1-4.0 h-1 of the liquid space velocity are satisfied.;COPYRIGHT: (C)2004,JPO
机译:解决的问题:为了获得能够在长时间内高效地除去重油馏分中的硫化合物的加氢脱硫催化剂,提供其制造方法以及使用该催化剂的加氢脱硫的方法。以氧化物为基准,所述催化剂携带至少8-25质量%的选自元素周期表的第6族元素的金属,以氧化物计,至少1-8质量%的选自所述元素周期表中的一种金属。在氧化铝载体上,以催化剂为基准,元素周期表的第8族元素,0.5-6质量%的磷和1-14质量%的碳。 500℃焙烧后催化剂的物理性能如下:比表面积为180-330m 2 / g,孔体积为0.4-0.7ml / g,平均孔直径是7-12 nm。包含上述成分的溶液被承载在氧化铝载体上,并在200℃或更低的温度下干燥。在氢分压为4-18 MPa,温度为320-410℃,液体空间为0.1-4.0 h -1 的条件下,使原料油与催化剂接触。速度令人满意。;版权所有:(C)2004,日本特许厅

著录项

  • 公开/公告号JP4047044B2

    专利类型

  • 公开/公告日2008-02-13

    原文格式PDF

  • 申请/专利权人 コスモ石油株式会社;

    申请/专利号JP20020092686

  • 发明设计人 廣瀬 敏之;中嶋 伸昌;

    申请日2002-03-28

  • 分类号B01J31/34;B01J35/10;C10G45/08;

  • 国家 JP

  • 入库时间 2022-08-21 20:18:39

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