Hydrocarbon composition of liquid products of catalytic oxy-cracking of vacuum gasoil

Elvira Guseinova, Alakbar Hasanov, Rashad Shikhiyev
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Abstract

The hydrocarbon composition of liquid products of oxycracking of vacuum gas oil obtained in the presence of a zeolite-containing catalyst has been studied. It has been established that the group hydrocarbon composition of the liquid oxycracking catalyzate is significantly affected by the process parameters. When considering the influence of the process temperature, it was found that the concentration of C 5 -C 9 and C 10+ alkanes has an opposite temperature dependence: the C 5 -C 9 yield passes through a maximum at a temperature of 500°C, while for C 10+ it is a minimum temperature; there is a linear relationship between the temperature and the yield of unsaturated; the yield of naphthenes gradually decreases with increasing temperature; elevated temperatures contribute to an increase in the total yield of aromatic hydrocarbons. When varying the duration of the process, it was revealed: within 900 seconds from the beginning of the process, the most significant decrease in concentration was noted for aromatic hydrocarbons. The low oxidation state of 0.5% contributes to the intensive conversion of high molecular weight alkanes and aromatic hydrocarbons with long side chains; the concentration of oxygen-containing compounds raises with an increase in the degree of oxidation to 1%, passing through a maximum. The contact time with the catalyst had a complex effect on the hydrocarbon composition of the liquid products of vacuum gas oil oxycracking: a short contact time contributes to a decrease in the concentration of high molecular weight paraffinic and naphthenic hydrocarbons and an increase in aromatic hydrocarbons; with a subsequent increase to 2 s, it drops sharply. The obtained data made it possible to establish the fundamental distinguishing features of the catalytic oxycracking of vacuum gas oil from the traditional catalytic and noncatalytic oxidative ones, and also to propose a list of reactions occurring during the catalytic oxycracking of vacuum gas oil.
真空汽油催化氧化裂化液体产物烃类组成
研究了在含沸石催化剂存在下,真空瓦斯油氧化裂化液体产物的碳氢化合物组成。结果表明,工艺参数对液体氧化裂化催化剂的烃基组成有显著影响。当考虑工艺温度的影响时,发现c5 - c9和c10 +的浓度具有相反的温度依赖性:c5 - c9的产率在500℃时达到最大值,而c10 +的产率是最低温度;温度与不饱和产物的产率呈线性关系;环烷的产率随着温度的升高而逐渐降低;升高的温度使芳烃的总产率增加。当改变过程的持续时间时,发现:在过程开始后900秒内,芳香烃的浓度下降幅度最大。0.5%的低氧化态有利于高分子量烷烃和长侧链芳烃的密集转化;含氧化合物的浓度随着氧化程度的增加而增加到1%,并通过最大值。与催化剂的接触时间对真空气油氧化裂化液体产物的烃组成有复杂的影响:短的接触时间使高分子量烷烃和环烷烃的浓度降低,芳烃的浓度增加;随着随后增加到2秒,它急剧下降。所获得的数据可以建立真空气油催化氧化裂化与传统的催化氧化裂化和非催化氧化裂化的基本区别,并提出真空气油催化氧化裂化过程中发生的一系列反应。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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