›› 2019, Vol. 50 ›› Issue (8): 1-5.

• 加工工艺 •    下一篇

催化剂积炭对逆流连续催化重整反应的影响

王杰广1,马爱增1,袁忠勋2,盖金祥3   

  1. 1. 中国石化石油化工科学研究院
    2. 中国石化工程建设有限公司
    3. 中国石化济南分公司
  • 收稿日期:2018-10-30 修回日期:2019-02-17 出版日期:2019-08-12 发布日期:2019-08-27
  • 通讯作者: 王杰广 E-mail:wangjg.ripp@sinopec.com
  • 基金资助:
    逆流移动床连续重整技术工业试验;低积炭高选择性逆流连续重整技术开发

EFFECT OF COKE DEPOSITION OF CATALYST ON COUNTERCURRENT CONTINUOUS CATALYTIC REFORMING REACTION

  • Received:2018-10-30 Revised:2019-02-17 Online:2019-08-12 Published:2019-08-27
  • Contact: Wang Jieguang E-mail:wangjg.ripp@sinopec.com

摘要: 在中国石化济南分公司600 kt/a逆流连续催化重整(简称逆流连续重整)工业试验装置上,考察了第四反应器(四反)入口温度和四反催化剂碳含量的关系以及催化剂积炭对逆流连续重整反应规律的影响。结果表明:四反入口温度对四反催化剂碳含量和总积炭量影响很大,降低四反入口温度有利于降低逆流连续重整的总体积炭水平;随着催化剂碳含量的增加,反应器温降减少,芳烃产率和氢气产率下降明显,环烷烃和烷烃的转化率下降,低碳数环烷烃转化率下降的幅度比高碳数的大,五元环烷烃转化率下降的幅度比六元环烷烃的大,异构烷烃转化率下降的幅度高于正构烷烃,低碳数正构烷烃转化率下降的幅度高于高碳数正构烷烃;逆流连续重整技术优化的方向是控制催化剂的总体积炭水平,尤其要尽可能降低四反的积炭量。

关键词: 逆流连续重整, 积炭, 环烷烃转化, 烷烃转化

Abstract: The relations between the inlet temperature of the 4th reactor and its coke content on the catalyst, and the effects of coke on countercurrent CCR reaction were investigated at a 600kt/a countercurrent CCR unit of SINOPEC Jinan Branch Company. The results showed that the inlet temperature of the 4th reactor had a great influence on its coke content and total coke amount of the whole reactor system. The lower inlet temperature of the 4th reactor could reduce the total coke amount of countercurrent CCR; With the increasing of coke content on catalysts, the temperature drop in each reactor reduced, the yield of aromatics and hydrogen apparently decreased, and the conversion of both naphthene and paraffin decreased; and the conversion rates of low carbon number naphthene and C5 ring naphthene decreased more than that of high carbon number and C6 ring naphthene, respectively; the conversion rate of iso-paraffin and low carbon number normal-paraffin decreased greater than that of normal-paraffin and high carbon number normal-paraffin, respectively. The optimization direction of countercurrent continuous reforming technology is to control the overall carbon accumulation level on catalyst, especially to reduce the carbon accumulation on the 4th reactor as far as possible.

Key words: countercurrent continuous catalytic reforming, coke deposition, naphthene conversion, paraffin conversion