化工进展 ›› 2025, Vol. 44 ›› Issue (5): 3009-3016.DOI: 10.16085/j.issn.1000-6613.2024-1913

• 化工过程减排 • 上一篇    

劣质渣油加氢催化剂构筑及其催化性能提升机制

朱慧红1,2(), 刘璐2, 刘鹏1, 李贺2, 杨涛2, 王继锋2, 侯栓弟2(), 彭冲3(), 赵毅毅1, 潘云翔1()   

  1. 1.上海交通大学化学化工学院,上海 200240
    2.中石化(大连)石油化工研究院有限公司,辽宁 大连 116045
    3.大连理工大学化工学院,辽宁 大连 116024
  • 收稿日期:2024-11-20 修回日期:2024-12-27 出版日期:2025-05-25 发布日期:2025-05-20
  • 通讯作者: 侯栓弟,彭冲,潘云翔
  • 作者简介:朱慧红(1978—),女,博士研究生,研究方向为渣油加氢。E-mail:zhuhuihong.fshy@sinopec.com
  • 基金资助:
    国家重点研发计划(2023YFA1507600)

Construction of hydrogenation catalysts for inferior residue and mechanism of catalytic performance enhancement

ZHU Huihong1,2(), LIU Lu2, LIU Peng1, LI He2, YANG Tao2, WANG Jifeng2, HOU Shuandi2(), PENG Chong3(), ZHAO Yiyi1, PAN Yunxiang1()   

  1. 1.School of Chemistry and Chemical Engineering,Shanghai Jiao Tong University, Shanghai 200240, China
    2.SINOPEC (Dalian) Research Institute of Petroleum and Petrochemicals Co. , Ltd. , Dalian 116045, Liaoning, China
    3.School of Chemical Engineering, Dalian University of Technology, Dalian 116024, Liaoning, China
  • Received:2024-11-20 Revised:2024-12-27 Online:2025-05-25 Published:2025-05-20
  • Contact: HOU Shuandi, PENG Chong, PAN Yunxiang

摘要:

原油需求持续增长,如何高效利用劣质渣油已成为亟待解决的重要问题。本文利用不同工艺构筑了两种NiMo/Al2O3催化剂(CAT-1与CAT-2),并系统研究了其在劣质渣油加氢反应中的催化性能。CAT-1在脱硫、脱残炭和脱金属等反应中表现出优于CAT-2的催化性能,催化性能分别较CAT-2提高了10.33%、8.94%和1.05%,且CAT-1的渣油转化率比CAT-2高出3.46%。CAT-1优异的催化性能与其更高的羟基含量密切相关。更多的羟基减弱了载体与金属物种之间的相互作用,使得Mo6+更容易还原为Mo4+,从而形成硫化程度更高、加氢活性更强的Type Ⅱ型活性相;羟基含量的增加也为加氢反应提供了更多的活性位点,并有效提升了金属物种的分散度,进而优化了催化剂的酸性和金属物种的氧化还原性。这些是促进催化剂加氢活性提升的主要原因。本研究为渣油高效转化提供了理论依据与技术支持。

关键词: 催化剂, 加氢, 渣油, 氧化铝, 羟基

Abstract:

As the demand for crude oil continues growing, the efficient utilization of inferior residue has become an important issue to be addressed. In the present study, two NiMo/Al2O3 catalysts (CAT-1 and CAT-2) are prepared using different methods, and their performance in hydrotreating reaction of inferior residue is systematically investigated. CAT-1 exhibits better catalytic performance than CAT-2 in hydrodesulfurization, conradson carbon residue reduction and hydrodemetalization reactions, with improvements of 10.33%, 8.94% and 1.05% respectively. In addition, CAT-1 also has a residue conversion rate 3.46% higher than CAT-2. The superior catalytic performance of CAT-1 is closely related to its high hydroxyl content. More hydroxyl groups weaken the interaction between support and metal species, which makes it easier to reduce Mo6+ to Mo4+, resulting in the formation of Type Ⅱ active phases with a higher degree of sulfurization and higher hydrogenation activity. The increase in hydroxyl content also provides more active sites for hydrogenation reaction and effectively improves dispersion of metal species, the acidity of catalyst and the redox properties of metal species. The present study provides theoretical basis and technical support for the efficient conversion of residue.

Key words: catalyst, hydrogenation, residua, alumina, hydroxyl

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