石油炼制与化工 ›› 2024, Vol. 55 ›› Issue (4): 47-52.

• 加工工艺 • 上一篇    下一篇

硫酸法烷基化装置原始开工问题研究

苗鹏杰,陈自娇,李烨,郭勤,田虎楠   

  1. 新疆理工学院能源化工工程学院
  • 收稿日期:2023-07-12 修回日期:2023-12-30 出版日期:2024-04-12 发布日期:2024-03-26
  • 通讯作者: 田虎楠 E-mail:hunan_tian2005@126.com
  • 基金资助:
    新疆维吾尔自治区自然科学基金面上项目

RESEARCH ON INITIAL START-UP OF ALKYLATION PLANT BY SULFURIC ACID CATALYSIS

  • Received:2023-07-12 Revised:2023-12-30 Online:2024-04-12 Published:2024-03-26

摘要: 面对硫酸法烷基化装置原始开工存在异丁烷不足、缺少烷基化油的难题,按照传统的开工标准会发生投料时“飞温”的危险。利用Aspen Plus软件对反应工段进行模拟及灵敏度分析,结果表明开工原料中含质量分数12.7%的碳四烯烃组分时最高反应温度为17 ℃,由此提出应用正丁烷代替部分异丁烷及全部烷基化油的新开工方法,大幅度降低对开工异丁烷及烷基化油的要求,确立装置原始开工的“五步法”新方案,使装置顺利初次开工并获得成功。实践表明,该新方法具有安全可靠、控制稳定的特点,对非标准状况下烷基化装置原始开工具有指导意义。

关键词: 硫酸法, 烷基化, 原始开工, 化工模拟

Abstract: Faced with the problems of insufficient isobutane and lack of alkylation oil in the initial srart-up of alkylation plant by sulphuric acid catalysis, the danger of “runaway temperature” will occur according to the traditional start-up standard. The simulation and sensitivity analysis of the reaction process were carried out by Aspen Plus software. The results showed that the maximum reaction temperature was 17 ℃ when the starting material contained 12.7% C4 olefin component. Therefore, a new start-up method of using n-butane to replace part of isobutane and all alkylated oil was put forward, which greatly reduced the requirements for start-up isobutane and alkylated oil, and a new “five step method” scheme for the initial start-up of the unit was established, making the initial start-up of the plant successful. The application results indicated that the new method was safe, reliable and stable, and had has a guiding significance for the initial start-up of alkylation units under non-standard conditions.

Key words: sulfuric acid method, alkylation, initial start-up, chemical simulation