石油炼制与化工 ›› 2024, Vol. 55 ›› Issue (4): 74-78.

• 控制与优化 • 上一篇    下一篇

甲醇制烯烃装置立管内下行催化剂的压力特性分析

王云池1,苟荣恒2,彭威3,王飞3,贺娇3   

  1. 1. 国能榆林化工有限公司

    2.  国能新疆化工有限公司

    3. 中国石油大学(北京)克拉玛依校区
  • 收稿日期:2023-06-25 修回日期:2023-12-27 出版日期:2024-04-12 发布日期:2024-03-26
  • 通讯作者: 彭威 E-mail:pengwei@cupk.edu.cn
  • 基金资助:
    基于催化剂物性分析的FCC装置状态监测和故障诊断技术;催化裂化装置松动风优化控制技术的研究

ANALYSIS ON PRESSURE CHARACTERISTIC OF CATALYST DESCENDING IN STANDPIPE OF METHANOL TO OLEFINS UNIT


  • Received:2023-06-25 Revised:2023-12-27 Online:2024-04-12 Published:2024-03-26
  • Supported by:
    Condition monitoring and fault diagnosis technology of FCC unit based on physical property analysis of catalyst;Study on optimal control technology of aeration gas in catalytic cracking unit

摘要: 针对某工业甲醇制烯烃装置再生立管存在催化剂输送不畅,导致催化剂循环量不稳定、双烯收率和产品分布变差的问题,通过测量再生立管不同位置的动态压力和静态压力,分析立管内气固两相流的流态和压力特性,探讨催化剂输送不畅的原因。结果表明:再生立管内催化剂循环量较低是催化剂脱气较快的主要原因;再生立管内的催化剂流态包括斜管部分的分层流、垂直管顶部的稀相流和下部的密相流;不同流态具有不同的压力特性,可以作为流态识别的依据。另外,对立管内的气固线速进行了计算,气泡运行方向与流态分析结果相一致,可以作为装置进行操作调整的依据。

关键词: 甲醇制烯烃, 立管, 再生催化剂, 压力特性, 流态识别

Abstract: The regeneration standpipe of an industrial methanol to olefins unit had the problem of poor catalyst transport, which led to unstable catalyst circulation, poor propylene and ethylene yield and product distribution.The flow state and pressure characteristics of gas-solid two-phase flow in the standpipe were analyzed by measuring the dynamic pressure and static pressure at different positions of the standpipe, and the reasons for the poor catalyst transport were discussed.The results showed that the main reason for the rapid degassing was the low amount of catalyst circulation in the regeneration standpipe.The catalyst flow patterns in the regeneration standpipe included stratified flow in the inclined pipe, thin phase flow in the top of the vertical pipe and dense phase flow in the lower part of the vertical pipe. Different flow patterns had different pressure characteristics, which could be used to identifythe flow patterns.In addition, the gas-solid linearvelocity in the standpipewas calculated, and the bubble direction was consistent with the analysis result of the flow patterns, which could be used as the basis for operation adjustment of the device.

Key words: methanol to olefins, standpipe, regenerated catalyst, pressure characteristic, flow pattern identification