石油炼制与化工 ›› 2015, Vol. 46 ›› Issue (8): 18-23.

• 加工工艺 • 上一篇    下一篇

煤焦油常压渣油悬浮床加氢工艺及中试研究

吴乐乐1,2,戴鑫1,李金璐1,邓文安1   

  1. 1. 中国石油大学(华东)重质油国家重点实验室
      2. 中海油能源发展股份有限公司安全环保分公司
  • 收稿日期:2015-01-04 修回日期:2015-02-05 出版日期:2015-08-12 发布日期:2015-07-27
  • 通讯作者: 邓文安 E-mail:dengwenan@upc.edu.cn
  • 基金资助:

    中国石油大学(华东)创新工程资助项目

REASERCH ON COAL TAR ATMOSPHERIC RESIDUE HYDROCRACKING IN SLURRY-BED AND PILOT SCALE TEST

  • Received:2015-01-04 Revised:2015-02-05 Online:2015-08-12 Published:2015-07-27

摘要: 以中温煤焦油常压渣油为原料,在高压釜中进行悬浮床加氢裂化模拟实验,考察了不同反应压力、反应温度、催化剂、助剂、反应时间对加氢效果的影响,并以优化后的工艺条件在3 000 mL环流反应器悬浮床加氢装置进行实验。结果表明,在反应压力为12.5 MPa、反应温度为425 ℃、油溶性钼镍双金属催化剂加入量为150 μg/g、助剂SDBS加入量为200 μg/g、硫粉加入量为400 μg/g、反应空速为1.0 h-1,新鲜氢气量为1 800 L/h的条件下,连续运转24 h石脑油、柴油和蜡油产率高达88.28%,减压渣油仅剩7.98%,单位生焦轻油转化率达48.13。

Abstract: The hydrocracking experiment of medium temperature coal tar atmospheric residue (MCAR,>350 ℃ fraction) was conducted in a magnetic-stirred autoclave to simulate the situation in real slurry-bed and the influence of reaction pressure, temperature, catalyst, additive and time was investigated. Then the pilot scale test was performed in a slurry-bed hydrocracking pilot plant with a 3 000 mL loop reactor under the optimal conditions determined by the above test. The results show that when the reaction conditions are 425 ℃, initial hydrogen pressure of 9 MPa (reaction pressure of 12.5 MPa), reaction time of 60 min, space velocity of 1.0 h-1, fresh H2 rate of 1 800 L/h , and the dosage of oil soluble Mo-Ni bimetallic catalyst, additive (SDBS) and sulfur of 150 μg?g-1, 200 μg?g-1and 400 μg?g-1, respectively, the total yield of naphtha, diesel and wax oil is 88.26% and vacuum residue is only 7.98% for 24 h operation. Furthermore, the light oil yield per unit of coke formed is up to 48.13%.