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首页> 外文期刊>Fuel Processing Technology >Dependence of onset time for mesophase formation on operating parameters during catalytic hydroconversion of Athabasca vacuum residue
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Dependence of onset time for mesophase formation on operating parameters during catalytic hydroconversion of Athabasca vacuum residue

机译:阿萨巴斯卡减压渣油催化加氢转化过程中中间相形成开始时间与操作参数的关系

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During the catalytic hydroconversion of vacuum residue fractions of bitumen or petroleum, the formation of mesophase can lead to fouling of reactor internals. In this study we examine the dependence of the onset of mesophase in a batch microreactor designed to enable in situ microscopic observation of the reacting liquid. The following process variables were investigated: temperature, partial pressure of hydrogen, catalyst concentration, agitation speed, and their interactions. Athabasca vacuum residue was converted in the presence of an iron sulfide particulate catalyst, and a statistical model was developed to describe the effects of the process variables on the onset time for mesophase formation. The temperature and catalyst concentration, respectively, had the most effect on mesophase onset time. The time for mesophase formation dropped by 12.1 min when the operating temperature increased from 440 degrees C to 450 degrees C. The mesophase onset time increased by 7.4 min when 3 wt.% of catalyst was added at 440 degrees C, compared to no catalyst addition. Partial pressure of hydrogen was not significant as an independent process variable for the range studied, from 2.4 to 5.2 MPa. The combined effects of hydrogen partial pressure and catalyst concentration were significant, as were the combined effects of temperature and catalyst concentration. (C) 2014 Published by Elsevier B.V.
机译:在沥青或石油的真空残余物馏分的催化加氢转化过程中,中间相的形成会导致反应器内部结垢。在这项研究中,我们检查了间歇式微反应器中中间相开始的依赖性,该反应器设计为能够原位观察反应液。研究了以下工艺变量:温度,氢气分压,催化剂浓度,搅拌速度及其相互作用。阿萨巴斯卡减压渣油在硫化铁颗粒催化剂的存在下转化,并建立了统计模型来描述工艺变量对中间相形成开始时间的影响。温度和催化剂浓度分别对中间相开始时间影响最大​​。当操作温度从440摄氏度增加到450摄氏度时,中间相形成的时间减少了12.1分钟。与不添加催化剂相比,当在440摄氏度下添加3 wt。%的催化剂时,中间相的形成时间增加了7.4分钟。 。在2.4至5.2 MPa的研究范围内,氢气的分压作为独立的过程变量并不显着。氢分压和催化剂浓度的组合作用是显着的,温度和催化剂浓度的组合作用也是显着的。 (C)2014由Elsevier B.V.发布

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