石油炼制与化工 ›› 2020, Vol. 51 ›› Issue (7): 43-48.

• 催化剂 • 上一篇    下一篇

加氢处理催化剂催化活性降低原因分析

金吉海   

  1. 中海油炼油化工科学研究院(北京)有限公司
  • 收稿日期:2019-12-30 修回日期:2020-03-16 出版日期:2020-07-12 发布日期:2020-07-28
  • 通讯作者: 金吉海 E-mail:jinjihai216@126.com
  • 基金资助:
     

CAUSE ANALYSIS OF REDUCTION OF HYDROGENATION CATALYST ACTIVITY

    

  1.  
  • Received:2019-12-30 Revised:2020-03-16 Online:2020-07-12 Published:2020-07-28
  • Supported by:
     

摘要: 为了研究不同条件下加氢处理催化剂的脱酸、脱硫和脱氮活性及其活性变化的原因,以WO3-NiO/Al2O3为催化剂、绥中减三线油为原料进行加氢试验,采用升温升压的方法改变反应条件,考察催化剂的活性稳定性。结果发现与未经升温升压的催化剂相比,经过高温高压反应600 h的催化剂活性降低,而催化剂的比表面积、孔体积、平均孔径及孔径分布变化不大。催化剂表征结果证明活性下降的原因是其碳含量偏高,活性组分中高活性的W4+及NiWS含量均有所降低,而活性较低的NiS,W5+,W6+含量相对较高。

关键词: 高酸原油, 加氢脱酸, 催化剂活性, 催化剂表征

Abstract: In order to study the deacidification, desulfurization and denitrification activities of hydrotreating catalysts under different conditions and the reasons for the activity reduction, the hydrogenation experiments were carried out with WO3-NiO/Al2O3 as the catalyst and Suizhong vacuum gas oil as feed. The activity stability of the catalysts under severe conditions was investigated byraising temperature and pressure. The results showed that the activity of the catalyst decreased after 600 h ofreaction under high temperature and high pressure, but the specific surface area, pore volume, average pore size and pore size distribution of the catalyst changedslightly compared with the same catalyst without temperature and pressure rise. The results of catalyst characterization show that the reasons for the decrease of activity are the higher carbon content, the reduced content of W4+ and NiWS phase with high activity and the increased content of NiS, W5+ and W6+ with low activity in the active component.

Key words: high acid crude oil, hydrodeacidification, catalyst activity, catalyst characterization

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