石油炼制与化工 ›› 2023, Vol. 54 ›› Issue (5): 42-47.

• 催化剂 • 上一篇    下一篇

工业C8+芳烃馏分脱烯烃催化剂失活原因分析

张孔远1,马亮1,张唯稚2,黄仁强1,崔孟达1   

  1. 1. 中国石油大学(华东)重质油国家重点实验室 CNPC催化重点实验室
    2. 青岛惠城环保科技集团股份有限公司
  • 收稿日期:2022-11-10 修回日期:2023-02-06 出版日期:2023-05-12 发布日期:2023-05-12
  • 通讯作者: 张孔远 E-mail:zkyuana@126.com

CAUSE ANALYSIS OF DEACTIVATION OF INDUSTRIAL DEOLEFINIZATION CATALYST FOR C8+ AROMATICS FRACTION

  • Received:2022-11-10 Revised:2023-02-06 Online:2023-05-12 Published:2023-05-12
  • Contact: Zhang Kongyuan E-mail:zkyuana@126.com

摘要: 采用N2吸附-脱附、X射线衍射、NH3程序升温脱附、吡啶吸附红外光谱方法对工业新鲜、失活及再生C8+芳烃脱烯烃催化剂的孔结构、晶相结构及表面酸性质进行了对比分析,采用热重分析、13C 核磁共振方法对工业失活催化剂进行了分析表征,采用红外光谱分析了失活催化剂甲苯-乙醇洗涤液中的有机物组成;以催化重整C8+芳烃为原料对工业新鲜、失活及再生催化剂进行了脱烯烃活性评价。结果表明:与新鲜催化剂相比,失活催化剂的比表面积与孔体积大幅度下降,平均孔径增大,总酸量下降,B酸和L酸酸量明显下降;造成脱烯烃催化剂失活的主要原因是催化剂表面及孔道中的积炭(结焦),积炭(结焦)以芳烃缩合结焦为主,烯烃缩合结焦为辅;催化剂再生后,比表面积、孔体积、总酸量以及B酸、L酸酸量基本恢复至新鲜催化剂水平,脱烯烃初活性恢复至96%。

关键词: C8+ 芳烃, 脱烯烃, Y分子筛催化剂, 失活, 再生

Abstract: The pore structure, crystal structure and surface acid properties of commercial fresh, deactivated and regenerated catalysts for olefin removal were studied by means of N2 adsorption-desorption, XRD, NH3-TPD and Py-IR, the commercial deactivated catalyst were characterized by TG and 13C NMR, and the organic composition in toluene-ethanol washing solution of deactivated catalyst was analyzed by FT-IR. The deolefinization activity of commercial fresh, deactivated and regenerated catalysts was evaluated by using catalytic reforming C8+ aromatics as raw materials. The results showed that the specific surface area and pore volume of the deactivated catalyst decreased significantly, the average pore size increased, the total acid content decreased, and the acid strength of B acid and L acid decreased significantly. The main cause of deactivation of the deolefinization catalyst was the carbon (coke) deposited on the surface and in the pores of the catalyst. The carbon (coke) was mainly formed by the condensation of aromatics and assisted by the condensation of olefin. After regeneration, the specific surface area, pore volume, total acid amount, B acid and L acid amount recovered basically to the level of fresh catalyst, and the initial deolefinization activity restored to 96 %.

Key words: C8+ aromatics, deolefin, Y zeolite catalyst, deactivation, regeneration