石油炼制与化工 ›› 2014, Vol. 45 ›› Issue (5): 83-86.

• 加工工艺 • 上一篇    下一篇

绥中36-1原油减三线馏分油催化加氢脱酸研究

费亚南,孙国方,李孝国,于海斌   

  1. 中国海油天津化工研究设计院
  • 收稿日期:2013-11-12 修回日期:2013-12-18 出版日期:2014-05-12 发布日期:2014-04-22
  • 通讯作者: 孙国方 E-mail:sgf7996119@163.com

STUDY ON HYDRO-DEACIDIFICATION OF SZ36-1 THIRD LINE VACUUM DISTILLATE

  • Received:2013-11-12 Revised:2013-12-18 Online:2014-05-12 Published:2014-04-22

摘要: 采用等体积浸渍法制备了一系列不同NiO含量的Ni-W体系催化剂,用于绥中36-1原油减三线馏分油的加氢脱酸反应,对催化剂的加氢反应工艺条件进行了考察。结果表明,NiO含量(w)为4.9%时催化剂活性最佳,较佳的反应工艺条件为反应温度315 ℃、反应压力3.2 MPa、氢油体积比300、质量空速1.5 h-1,在该条件下可将原料油的酸值由3.48 mgKOH/g降到0.05 mgKOH/g以下。并对催化剂进行2 000 h的稳定性试验,结果表明催化剂活性稳定,相比参比催化剂,反应条件更为缓和、裂解反应程度低。

Abstract: A series of Ni-W based catalysts with different NiO content were prepared by incipient wetness method for hydro-deacidification of Suizhong36-1 crude third line vacuum distillate. The effect of operating conditions was investigated. The test results show that the optimum NiO content is around 4.9%. At the conditions of 315℃, 3.2 MPa, hydrogen to oil ratio 300, and volume space velocity 1.5 h-1, the acid value of Suizhong36-1 third line vacuum distillate is reduced to 0.05 mgKOH/g from 3.48 mgKOH/g of feed. A long term stability test for more than 2 000 h is conducted. The results indicate that compared with reference catalyst, the catalyst prepared has a lower cracking degree and is more stable under the moderate conditions.