石油炼制与化工 ›› 2025, Vol. 56 ›› Issue (6): 1-9.

• 催化剂 •    下一篇

渣油加氢降残炭催化剂初期积炭结构规律研究

侯冉冉,杨清河,曾双亲,聂红,贾燕子,郭传奎   

  1. 中石化石油化工科学研究院有限公司
  • 收稿日期:2024-04-02 修回日期:2024-04-28 出版日期:2025-06-12 发布日期:2025-05-30
  • 通讯作者: 聂红 E-mail:niehong.ripp@sinopec.com
  • 基金资助:
    国家重点研发计划项目

STUDY ON THE STRUCTURE VARIATION OF INITIAL COKE ON RESIDUE HDCCR CATALYSTS


  • Received:2024-04-02 Revised:2024-04-28 Online:2025-06-12 Published:2025-05-30

摘要: 为研究渣油加氢催化剂上积炭结构随运转时间变化的规律,通过改变高压釜渣油加氢过程的反应时间,获得积炭催化剂,以正庚烷和甲苯为溶剂对积炭催化剂进行连续分步处理,得到溶于甲苯的可溶性软炭和不溶于甲苯的固体积炭,分别对两种积炭的结构进行分析。通过分析加氢后渣油的硫含量和残炭随反应时间的变化,得知随反应进行催化剂的加氢活性呈现出一定的下降趋势。通过对甲苯萃取后的固体积炭催化剂进行热重-质谱分析、固体核磁共振以及拉曼光谱分析,发现反应时间为0~60 min时,催化剂积炭的芳香度及石墨化程度并未发生明显提高,但继续延长反应时间,积炭结构中的芳香碳含量增加,积炭的石墨化程度提高。结合不同反应时间下的甲苯可溶性软炭的傅里叶变换离子回旋共振质谱分析结果,反应时间为60 min的可溶性软炭中稠环芳烃类物质增加,表明积炭前身物在反应初期就已发生脱氢缩合反应,但是在催化剂的加氢作用下,形成的积炭仍溶于甲苯;反应后期由于催化剂加氢能力的限制,脱氢缩合反应程度加剧,积炭的芳香度进一步提高,且积炭难以通过加氢反应被去除,沉积在催化剂上使得加氢能力进一步下降。

关键词: 渣油加氢, 催化剂, 积炭, 芳香度, 可溶性积炭

Abstract: To study the structural variation of coke on residue HDCCR catalysts with time-on-stream, the spent catalysts tested at different times on a bench-scale continuous stirred tank reactor were analyzed. The spent catalysts were successively dissolved in steps with n-heptane and toluene to obtain toluene-soluble soft coke and hard coke deposited on catalysts. Then the structures of the two types of coke were analyzed respectively. The variation of sulfur content and carbon residue of hydrotreatedresidue was investigated, and it was concluded that the catalytic performance tended to decrease as the reaction proceeded. TG-MS, 13CNMR and Raman spectroscopywere used to investigate the structural changes of hard coke, it revealed that the aromaticity and graphitization of the hard coke did not significantly increase at the time-on-stream from 0 to 60 min. However, when the time-on-stream was increased to 240 min, the proportion of aromatic carbon in the hard coke increased, and the graphitization of coke enhanced. Combined with the results of FT-ICR MS of toluene-soluble soft coke at different time-on-stream, the increase in condensed aromatics in the toluene-soluble soft coke performed on 60 min suggests that the coke precursors have already dehydrogenatedandcondensated in the early stage, whereas the formed coke is still soluble in toluene. In the advanced stage of the residue hydrotreating reaction, owing to the limitation of the catalytic capacity, the dehydrogenation-condensation reaction was intensified, which contributed to the further increase in coke aromaticity, hard coke which is difficult to remove even further reducing the catalytic activity.

Key words: heavy oil hydrotreating, catalyst, coke, aromaticity, toluene-soluble soft coke