化工进展 ›› 2022, Vol. 41 ›› Issue (S1): 229-238.DOI: 10.16085/j.issn.1000-6613.2022-0734

• 工业催化 • 上一篇    下一篇

ZSM-5/γ-Al2O3质量比对FCC轻汽油异构化/芳构化性能影响

宋绍彤1,2(), 吕忠武1, 姜增琨1, 李阳1, 吴培1, 张雅琳1, 张然1, 陈金洋2, 鞠雅娜1()   

  1. 1.中国石油天然气股份有限公司石油化工研究院,北京 102206
    2.中国石油大学(北京)化学工程学院重质油 国家重点实验室,北京 102249
  • 收稿日期:2022-04-24 修回日期:2022-05-16 出版日期:2022-10-20 发布日期:2022-11-10
  • 通讯作者: 鞠雅娜
  • 作者简介:宋绍彤(1990—),女,博士研究生,研究方向为汽油加氢催化剂。E-mail:songshaotong@petrochina.com.cn
  • 基金资助:
    中国石油天然气股份有限公司科学研究与技术开发项目(2018E-03)

Effect of ZSM-5/γ-Al2O3 mass ratio on isomerization/aromatization performance of FCC light gasoline

SONG Shaotong1,2(), LYU Zhongwu1, JIANG Zengkun1, LI Yang1, WU Pei1, ZHANG Yalin1, ZHANG Ran1, CHEN Jinyang2, JU Yana1()   

  1. 1.Petrochemical Research Institute, PetroChina Company Limited, Beijing 100195, China
    2.State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China
  • Received:2022-04-24 Revised:2022-05-16 Online:2022-10-20 Published:2022-11-10
  • Contact: JU Yana

摘要:

通过调变ZSM-5分子筛与γ-Al2O3质量比,采用等体积浸渍法制备系列FCC轻汽油异构化/芳构化催化剂。本文采用X射线衍射(XRD)、N2吸附脱附、扫描电子显微镜(SEM)、氨气程序升温脱附(NH3-TPD)、红外光谱(IR)和吡啶红外光谱(Py-IR)等手段对其进行表征,并以乌鲁木齐石化醚后C5掺杂液化石油气(LPG)为原料对催化剂异构化/芳构化性能进行评价。实验结果表明,ZSM-5分子筛与γ-Al2O3质量比的调变可以改变催化剂的酸性质及孔结构性质。在反应温度380℃、反应压力1.0MPa、反应空速1.0h-1、氢/油体积比100、LPG进量4.4g/h的条件下,ZnLa/ZSM-5/γ-Al2O3-1异构化/芳构化产物与反应原料相比,烯烃体积分数降低27.49%、异构烷烃体积分数增加15.87%、芳烃体积分数增加3.97%,辛烷值损失3.38个单位,产品收率高达89.90%,实现了异构化/芳构化大幅降烯烃保辛烷值的目标。

关键词: ZSM-5, γ-Al2O3, 质量比, FCC轻汽油, 异构化/芳构化

Abstract:

A series of FCC light gasoline isomerization/aromatization catalysts with different ZSM-5/γ-Al2O3 mass ratio were prepared by the incipient wetness method. The physico-chemical properties of the catalysts were characterized by XRD, N2 adsorption desorption, SEM, NH3-TPD, IR and pyridine FTIR. The isomerization/aromatization properties of the catalysts were evaluated using etherified C5 light gasoline in Urumqi Petrochemical Company with LPG as feedstocks. The results showed that the acidity and pore structure of the catalysts can be changed by adjusting the ZSM-5/γ-Al2O3 mass ratio. Under the ZnLa/ZSM-5/γ-Al2O3-1 catalyst at the reaction temperature 380℃, reaction pressure 1.0MPa, the space velocity 1.0h-1, hydrogen/oil volume ratio 100 and LPG feed rate 4.4g/h by comparing the isomerization/aromatization products with feedstocks, the volume fraction of olefins decreased by 27.49%, the volume fraction of isoalkanes increased by 15.87%, the volume fraction of aromatics increased by 3.97%, the octane number reduced by 3.38 and the yield of the product was up to 89.90%. The goal of greatly reducing olefins with maintaining octane number by isomerization/aromatization was achieved.

Key words: ZSM-5, γ-Al2O3, mass ratio, light FCC gasoline, isomerization/aromatization

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