重油催化裂化反应工艺技术创新
CSTR:
作者:
作者单位:

(中国石油大学重质油加工国家重点实验室,北京 102249)

作者简介:

高金森(1964-),男,教授,博士,博士生导师,研究方向为重油催化裂化。E-mail:jsgao@cup.edu.cn。

通讯作者:

中图分类号:

TE 624 〖HTH〗

基金项目:

国家自然科学基金项目(21176252);国家科技支撑计划项目(2012BAE05B02)


Technical innovation of fluid catalytic cracking for heavy oil processing
Author:
Affiliation:

(State Key Laboratory of Heavy Oil Processing in China University of Petroleum, Beijing 102249, China)

Fund Project:

  • 摘要
  • |
  • 图/表
  • |
  • 访问统计
  • |
  • 参考文献
  • |
  • 相似文献
  • |
  • 引证文献
  • |
  • 资源附件
  • |
  • 文章评论
    摘要:

    重油催化裂化(FCC)工艺中,反应器内多相流动规律和精细数学描述是关键。基于湍流气固两相流理论和裂化反应集总动力学基础研究,详细描述和刻画FCC提升管反应器内流动传热过程及裂化反应历程,并创新性地提出以最大限度提高轻质油收率和生产清洁汽油为目标的催化裂化工艺的发展方向,应按照平行—顺序反应历程要求实现反应和转化过程的“分区调控”,并根据烃分子“竞争吸附”和反应特性的差异匹配催化环境。

    Abstract:

    Facing the challenge of heavy oil processing, the chemical engineering details of flow characteristics, heat transfer in fluid catalytic cracking (FCC) riser reactor and the mechanism of cracking reaction, were particularly described, which were based on the fundamental research of turbulent gas-solid two-phase flow and lumped kinetics theories. In order to maximize the light oil yield and obtain clean gasoline, a new idea of "zoning-regulation" was proposed according to the parallel-sequential reaction mechanism and competing-adsorption between different hydrocarbons. Then the reaction performances of feedstocks with different properties were met by their optimal catalytic conditions. In view of the above works, a series of processing or new technologies matched by the novel structures or special equipments were successfully developed.

    参考文献
    相似文献
    引证文献
引用本文

高金森,王刚,卢春喜,徐春明.重油催化裂化反应工艺技术创新[J].,2013,(5):181-185

复制
分享
相关视频

文章指标
  • 点击次数:
  • 下载次数:
  • HTML阅读次数:
  • 引用次数:
历史
  • 收稿日期:2013-06-08
  • 最后修改日期:
  • 录用日期:
  • 在线发布日期: 2014-07-18
  • 出版日期:
文章二维码