石油炼制与化工 ›› 2014, Vol. 45 ›› Issue (7): 29-35.

• 催化剂 • 上一篇    下一篇

FCC催化剂后处理工艺的探索

周岩1,张杰潇2,许明德2,田辉平2   

  1. 1. 中国石化催化剂齐鲁分公司
      2. 中国石化石油化工科学研究院
  • 收稿日期:2013-12-23 修回日期:2014-03-10 出版日期:2014-07-12 发布日期:2014-06-16
  • 通讯作者: 张杰潇 E-mail:zjx.ripp@sinopec.com
  • 基金资助:

    中国石油化工股份有限公司合同项目

RESEARCH ON POST-TREATMENT OF FCC CATALYST

  • Received:2013-12-23 Revised:2014-03-10 Online:2014-07-12 Published:2014-06-16

摘要: 针对目前FCC催化剂制备方法工艺流程复杂的现状,进行催化剂后处理工艺制备流程的探索。将NaY分子筛、拟薄水铝石、铝溶胶、高岭土打浆混合,喷雾干燥得到催化剂粉体,对该催化剂粉体进行基本性质的表征。利用已经制备好未经改性的催化剂NaY35作为起始原料,采用三次焙烧和三次常温(<90 ℃)铵盐交换、两次焙烧和两次高温(>90 ℃)铵盐交换两种不同催化剂洗涤方法进行后处理工艺的研究,得到的两种催化剂的Na2O质量分数均达到0.3%以下,且其基本性质能够满足工业要求。

Abstract: Due to the complexity of present FCC catalyst preparation process, catalyst post-treatment technology was explored. NaY zeolite, pseudo-boehmite, aluminum sol and kaolin were mixed and spray-dried into catalyst microsphere NaY35. The basic properties of the unmodified NaY35 were characterized by XRF、XRD、BET. The NaY35 catalyst was treated by once calcination and then once rare earth ion exchange. The treated NaY35 was used as a starting precursor. The precursor was then treated by three times calcinations and three times ammonium ion exchanges at normal temperature(<90 ℃), and two times calcinations and two times ammonium ion exchanges at high temperature(>90 ℃), respectively to explore the optimized post-treatment conditions for FCC catalyst.The test results indicate that the Na2O contents in both prepared catalysts are less than 0.3% (wt).