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Studies on the Catalytic Cracking Performance of Coker Gas Oil

机译:焦化瓦斯油催化裂化性能的研究

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摘要

Catalytic cracking experiments in which various blend levels of coker gas oil (CGO) in fluidized catalytic cracking (FCC) feedstock were reacted over two kinds of commercial equilibrium catalysts (RGD-1 and LBO-16) demonstrate that the blending ratio affects the potential ability of a FCC unit treating CGO obviously. The limits of the blending ratio for Daqing CGO and Dagang CGO are 30 and 20 wt %, respectively, to obtain a desirable product distribution at a relatively high feed conversion. The operating condition of a high catalyst/ oil ratio in combination with a short residence time (or high weight hourly space velocity) and moderate reaction temperature is the optimal operating condition for catalytic cracking of CGO and its mixture. A FCC catalyst, such as RGD-1, which has proper acidities and high accessibility, is suitable for dealing with CGO effectively, which leads to an obvious improvement over conversion and product distribution. The analysis and contrast catalytic cracking experiments of narrow cuts of Daqing CGO show that the fraction of Daqing CGO is accumulated largely in the range of 300-450℃ and there exists high content of basic nitrogen and polycyclic aromatics. The lowest crackability of the cut from 400 to 450℃ constrains total CGO cracking performance, which is caused by a preferential chemisorption of the polycyclic aromatic molecules, and basic nitrogen compounds take place prior to the desirable adsorption of the other hydrocarbons, which is necessary for the cracking reaction to occur.
机译:催化裂化实验中,流化催化裂化(FCC)原料中各种焦化瓦斯油(CGO)的混合水平在两种商业平衡催化剂(RGD-1和LBO-16)上反应表明,混合比例会影响潜在的能力FCC部门处理CGO的情况明显。大庆CGO和大港CGO的混合比例的极限分别为30和20wt%,以在相对高的进料转化率下获得期望的产品分布。高催化剂/油比和短停留时间(或高时空重量)和适中反应温度的操作条件是CGO及其混合物催化裂化的最佳操作条件。具有适当酸度和高可及性的FCC催化剂,例如RGD-1,适合有效地处理CGO,从而在转化率和产物分布方面带来了明显的改善。通过对大庆CGO窄馏分的分析和对比催化裂化实验表明,大庆CGO的馏分在300-450℃范围内大量积累,碱性氮和多环芳烃含量较高。从400到450℃的切口的最低可裂性会限制CGO的整体裂解性能,这是由于多环芳族分子的优先化学吸附而引起的,而碱性氮化合物会先于其他烃的理想吸附而发生,这对于发生裂解反应。

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  • 来源
    《Energy & fuels》 |2009年第2期|1942-1949|共8页
  • 作者单位

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
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