炼油技术与工程 ›› 2023, Vol. 53 ›› Issue (8): 57-60.

• 催化剂和助剂 • 上一篇    下一篇

重整催化剂铂分散度的工业优化措施及效果

严巍宁, 杨兴, 唐显全, 姜华, 于明欣   

  1. 大连西太平洋石油化工有限公司
  • 收稿日期:2023-05-04 出版日期:2023-08-15 发布日期:2023-09-25

Industrial optimization measures and effects of platinum dispersion of reforming catalyst

Yan Weining, Yang Xing, Tang Xianquan, Jiang Hua, Yu Mingxin   

  1. PetroChina Dalian West Pacific Petrochemical Co., Ltd.
  • Received:2023-05-04 Online:2023-08-15 Published:2023-09-25

摘要:

铂分散度是影响催化重整催化剂活性的重要因素,重整催化剂铂分散度一般通过氢氧吸附法测得。由于高温和水汽的作用,催化剂会发生铂晶粒聚集、氯组分流失等问题,从而导致催化剂的活性下降。待生催化剂烧炭后经过氧化和氯化更新补充氯元素、铂晶粒重新分散,恢复催化剂活性。氧氯化段条件是恢复铂分散度的关键因素。该装置通过调整反应苛刻度,将催化剂积炭由3.0%~3.5%提高至大于4.0%。将第二烧焦段入口的温度由480℃提高至大于490℃,氧氯化段床层温度由480~490℃提高至大于510℃。第二烧焦段出口氧体积分数由0.35%降低至0.30%以提高氧氯化段配风量,氧氯化段氧体积分数维持大于5.8%。根据催化剂循环速率,氯元素注入量由2 000μg/g提高至2 600μg/g。水氯摩尔比控制在5~6。催化剂铂分散度由70%有效提高至大于85%。

关键词: 重整催化剂, 铂分散度, 氢氧吸附法, 氧氯化段, 温度, 氧含量, 注氯量, 水氯摩尔比

Abstract:

Platinum dispersion is an important factor affecting the activity of catalytic reforming catalyst. The platinum dispersion of reforming catalyst is generally measured by hydrogen-oxygen adsorption method. Due to high temperature and moisture atmosphere, the platinum on the catalyst will accumulate and the chlorine components will be lost, which leads to the deactivation of catalyst. After carbon burning of the deactivation catalyst, it is oxidized and chlorinated to supplement the chlorine, and disperse platinum crystal particles, and restore the catalyst activity. The oxychlorination stage conditions are key factors in restoring platinum dispersion. By adjusting the reaction severity, the carbon deposition is increased from 3.0%~3.5% to over 4.0%. Increase the temperature at the inlet of the second charring stage from 480 ℃ to more than 490 ℃, and the bed temperature of the oxychlorination stage is increased from 480~490 ℃ to more than 510 ℃. The oxygen volume fraction at the outlet of the second charring stage is reduced from 0.35% to 0.30% to improve the air distribution in the oxychlorination stage, and the oxygen volume fraction in the oxychlorination stage is remained above 5.8%. According to the catalyst circulation rate, the chlorine injection increases from 2,000 μg/g to 2,600 μg/g. The molar ratio of water to chlorine is controlled to 5~6. The platinum dispersion of the reforming catalyst is increased from 70% to more than 85%.

Key words: reforming catalyst, platinum dispersion, hydrogen oxygen adsorption method, oxychlorination stage, temperature, oxygen content, the amount of chlorine injection, molar ratio of water to chlorine