阿塔苏-阿拉山口油泥催化加氢最佳工艺条件的确定

S. Tyanakh, M. Baikenov, Fengyun Ma, V. Fomin, G. Baikenova, Anuar S. Ashimhanov, Raikhan S. Seitzhan
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引用次数: 0

摘要

利用概率确定性规划的方法,实验确定了油泥(阿塔苏-阿拉山口)催化加氢的最佳工艺条件和馏分运动粘度在350℃时的变化。在油泥加氢过程中,轻馏分的最大总收率达到62.1%,运动粘度从2.2 mm2/s降至1.2 mm2/s。在实验条件下,初始氢压力和含钴纳米催化剂微硅酸盐(催化剂1)的添加量对油泥中馏分收率的影响最大。结果表明,催化剂1能提高油泥加氢过程中柴油馏分组分的收率。首次建立了处理前后350℃馏分的单体和群化学组成。纳米催化剂1的用量为1.2 ~ 1.5%,可提高350℃以下馏分和柴油馏分组分的收率。这是由于石蜡烃产率由57.6%(初始分数)提高到80.7%,芳烃产率由14.1%降低到12.9%,多环芳烃产率由9.56%降低到4.3%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Determination of Optimal Conditions for Catalytic Hydrogenation of Oil Sludge (Atasu-Alashankou)
The optimal conditions of catalytic hydrogenation of oil sludge (Atasu-Alashankou) and the change in the kinematic viscosity of the fraction to 350℃ from the studied factors using the method of probabilisticdeterministic planning were experimentally determined. During the hydrogenation process of oil sludge, the maximum total yield of light fractions reached 62.1 %, and the kinematic viscosity decreased from 2.2 to 1.2 mm2/s. It was established the initial hydrogen pressure and the amount of added nanocatalyst microsilicate with cobalt (catalyst 1) have the greatest influence on the yield of the middle fraction from oil sludge under experimental conditions. It was shown that catalyst 1 increases the yield of diesel fraction components during the hydrogenation process of oil sludge. For the first time, we established the individual and group chemical composition of the fraction up to 350℃ before and after processing. The use of nanocatalyst 1 in amounts of 1.2–1.5 % led to an increase in the yield of the fraction up to 350℃ and diesel fraction components. This is due to the yield of paraffinic hydrocarbons increasing from 57.6 (initial fraction) to 80.7 %, as well as a decrease in aromatic hydrocarbons from 14.1 to 12.9 % and polycyclic aromatic hydrocarbons from 9.56 to 4.3 %.
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