石油炼制与化工 ›› 2016, Vol. 47 ›› Issue (5): 67-73.

• 催化剂 • 上一篇    下一篇

溶胶凝胶法制备体相型Mo-Ni复合氧化物催化剂及其加氢脱硫性能研究

张大龙,徐永卫,李孟华,侯凯湖   

  1. 河北工业大学化工学院
  • 收稿日期:2015-10-12 修回日期:2015-11-23 出版日期:2016-05-12 发布日期:2016-04-25
  • 通讯作者: 侯凯湖 E-mail:khou@hebut.edu.cn

SYNTHESIS OF Mo-Ni BULK CATALYST BY SOL-GEL METHOD AND HYDRODESULFURIZATION PERFORMANCE

  • Received:2015-10-12 Revised:2015-11-23 Online:2016-05-12 Published:2016-04-25
  • Contact: Kaihu Hou E-mail:khou@hebut.edu.cn

摘要:

采用溶胶-凝胶法制备了体相型Mo-Ni复合氧化物加氢脱硫催化剂,并对其进行XRD,BET,NH3-TPD等表征,以二苯并噻吩质量分数2%的正辛烷溶液为原料,在连续固定床反应装置上对催化剂的加氢脱硫性能进行评价,考察催化剂焙烧温度、溶胶凝胶过程中溶液pH以及淀粉的加入量等对催化剂性质和性能的影响。结果表明:在500 ℃以上高温焙烧后的氧化态催化剂中主要存在α-NiMoO4和β-NiMoO4晶相,硫化态催化剂中则存在MoS2和Ni2S3晶相;焙烧温度的升高有利于氧化态催化剂形成α-NiMoO4晶相,溶液碱性的增加则有利于形成β-NiMoO4晶相,二者均导致催化剂的总酸量显著降低;淀粉的加入对氧化态催化剂的晶相影响很小,但有利于提高活性组分的分散性,适量淀粉的加入可提高催化剂的比表面积和孔体积;在焙烧温度为600 ℃、溶液pH为 2和淀粉加入量为 15 g/mol的条件下所制备的催化剂具有较高的加氢脱硫活性,在反应温度为 260 ℃、反应压力为 2.5 MPa、体积空速为 2 h-1和氢油体积比为 300的条件下,对于硫质量分数为3480μg/g的原料,加氢脱硫率高达98.3%,二苯并噻吩的反应以加氢脱硫路径占优势,加氢脱硫路径与氢解脱硫路径反应的比值约为1.23。

关键词: 溶胶凝胶法, Mo-Ni复合氧化物, 加氢脱硫, 二苯并噻吩

Abstract:

The bulk Mo-Ni composite oxide catalysts were prepared by sol-gel method and were characterized by XRD、BET、NH3-TPD. Using 2 wt% DBT- n-octane solution as the feed, the HDS performance of the catalysts were tested in a continuous flow fixed-bed reactor. According to the results of characterization and evaluation, the effects of calcination temperature, the solution pH of sol-gel process and the addition of starch on the properties and catalytic performance of the catalysts were investigated. The characterization results showed that oxided catalysts under more than 500℃ calcination were mainly composed of crystalline phase α-NiMoO4 and β-NiMoO4, while the sulfided catalysts were mainly composed of MoS2 and Ni2S3. The increasing of calcination temperature is beneficial for the formation of α-NiMoO4, while the enhancement of the alkaline solution is favorable to the formation of β-NiMoO4, the both significantly reduce the total acidity of catalysts. The addition of starch has little fact on the crystalline phase of oxided catalyst, but it can improve the dispersion of active component. The introduction of appropriate amount of starch can increase the specific surface area and pore volume of the catalysts. The results of hydrodesulfurization reaction indicated that the catalyst prepared under the conditions of calcination temperature 600 ℃, the pH solution 2, the starch amount 15g/(Mo+Ni)mol, exhibited a higher hydrodesulfurization activity. Under the conditions of 260 ℃, 2 h-1, 2.5 MPa and H2/oil volume ratio 300, the desulfurization rate of the feed containing 3 480 μg/g S over the catalyst reached to 98.3%, hydrogenation desulfurization (HYD) pathway was the prior way during the HDS reaction of DBT, and the HYD/DDS( direct desulfurization) ratio was 1.23.

Key words: sol-gel method, Mo-Ni bulk catalyst, HDS, DBT