石油炼制与化工 ›› 2023, Vol. 54 ›› Issue (12): 6-13.

• 加工工艺 • 上一篇    下一篇

国内首套加工低硫高氮渣油的固定床加氢装置运行分析

方强,邵志才,戴立顺   

  1. 中石化石油化工科学研究院有限公司
  • 收稿日期:2023-03-28 修回日期:2023-09-12 出版日期:2023-12-12 发布日期:2023-12-05
  • 通讯作者: 邵志才 E-mail:shaozc.ripp@sinopec.com

OPERATION ANALYSIS OF THE FIRST FIXED-BED HYDROTREATING UNIT FOR LOW SULFUR AND HIGH NITROGEN RESIDUE IN CHINA

  • Received:2023-03-28 Revised:2023-09-12 Online:2023-12-12 Published:2023-12-05
  • Contact: Shao Zhicai E-mail:shaozc.ripp@sinopec.com

摘要: A装置为国内首套加工低硫高氮渣油的固定床加氢装置,其原料S质量分数较低(为1.38%)、N质量分数较高(为0.68%),与以往高硫渣油固定床加氢装置的原料性质显著不同。为了分析这种原料的加氢反应特性,在实验室进行了与高硫渣油加氢处理对比试验,也比较了两者工业装置运行数据。在实验室中型装置上,采用相同催化剂级配,在反应温度375.5 ℃、氢分压15.0 MPa、体积空速0.23 h-1、氢油体积比700的条件下,进行了这两种典型原料的固定床加氢试验,结果表明,处理低硫高氮渣油时降残炭率为49.83%,处理高硫渣油时降残炭率高达69.10%。A装置加工残炭为11.32%的低硫高氮渣油时,降残炭率为48.14%;B装置加工残炭为11.50%的高硫渣油时,降残炭率为55.39%。实验室和工业装置的试验结果均说明低硫高氮类渣油中残炭前身物的加氢转化较为困难。A装置自建成以来已完成6个周期的运行,每周期原料的S质量分数(平均值)均不大于1.51%,N质量分数(平均值)均不小于0.62%。对运行情况分析发现:高压换热器结垢导致其在运行中后期时提高反应温度较困难;原料中减压渣油的比例对该装置运行周期的长短影响较大,减压渣油比例高时运行周期较短,反之亦然;消除装置运行瓶颈的措施为进行高压换热器及反应器系统的改造。

关键词: 低硫高氮, 渣油, 固定床加氢, 运行分析, 消除瓶颈

Abstract: Unit A was the first fixed bed residue hydrogenation unit for processing low sulfur and high nitrogen residue in China. Its mass fraction of sulfur(1.38%) was lower and mass fraction of nitrogen(0.68%) was higher. The feedstock properties of the fixed-bed hydrogenation unit for high sulfur residue were significantly different from those in the past. In order to analyze the hydrogenation reaction characteristics of low sulfur and high nitrogen residue, a comparative experiment was carried out in the laboratory with the hydrotreating of high sulfur residue, and the operating data of industrial units of processing low sulfur and high nitrogen residue and high sulfur residue were also be compared. In the pilot test, the same catalyst gradation was used under the conditions of reaction temperature 375.5 ℃, H2 partial pressure 15.0 MPa, liquid volumetric space velocity 0.23 h-1, and volume ratio of H2/oil 700. The results showed that the reduction rate of carbon residue was 49.83% for low sulfur and high nitrogen residue, and 69.10% for high sulfur residue. In commercial application, the carbon residue reduction rate was 48.14% for low sulfur and high nitrogen residue with 11.32% of carbon residue in unit A, and 55.39% for high sulfur residue with 11.50% of carbon residue in unit B. The results of both laboratory and commercial application showed that it was difficult to hydrogenation the carbon residue precursors in low sulfur and high nitrogen residual oils. Unit A has completed 6 cycles of operation since it was built. The average sulfur content in the feedstock in each cycle was no more than 1.51%, and the average nitrogen content in the feedstock was no less than 0.62%. By analyzing the operation of Unit A, it was found that the scaling of the high-pressure heat exchanger made it difficult to increase the reaction temperature in the middle and end of run. The proportion of vacuum residue in the feedstock had a significant impact on the length of the operating cycle. The operating cycle was short when the proportion of vacuum residue was high, and vice versa. The measure to eliminate the operation bottleneck of the unit is to retrofit the high-pressure heat exchanger and reactor system.

Key words: low sulfur and high nitrogen, residue, fixed-bed hydrotreating, operation analysis, eliminating bottlenecks