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用过渡金属改性硅胶吸附剂脱除焦化柴油中的氮化物
引用本文:王云芳,张坤,蒋超,刘伟. 用过渡金属改性硅胶吸附剂脱除焦化柴油中的氮化物[J]. 石化技术与应用, 2011, 29(4): 299-302
作者姓名:王云芳  张坤  蒋超  刘伟
作者单位:1. 中国石油大学(华东)化学工程学院,山东,青岛,266555
2. 中国石油大连润滑油厂,辽宁,大连,116032
3. 中国石化胜利油田胜利勘察设计研究院有限公司,山东,东营,257026
摘    要:将过渡金属离子(Fe3+,Co2+,Ni2+,Cu2+)负载到硅胶上,先制得过渡金属离子改性硅胶吸附剂(Fe(Ⅲ)/SiO2,Co(Ⅱ)/SiO2,Ni(Ⅱ)/SiO2,Cu(Ⅱ)/SiO2),后在氢气环境中和500℃下对过渡金属离子改性硅胶吸附剂进行还原处理,制备出过渡金属改性硅胶吸附剂Fe/SiO2,Co/SiO2,Ni/SiO2。分别在间歇式和连续固定床吸附装置上,以焦化柴油(氮质量分数为2.1×10-3)为原料,在常压下研究了吸附条件对吸附剂脱氮效果的影响。结果表明,最佳吸附温度为120℃,最佳油剂比[m(焦化柴油)/m(吸附剂)]为60;平衡吸附量[m(氮)/m(吸附剂)]由小到大顺序为Fe(Ⅲ)/SiO2,Ni/SiO2,Co(Ⅱ)/SiO2,Cu(Ⅱ)/SiO2,Fe/SiO2,Ni(Ⅱ)/SiO2,Co/SiO2;分别用Fe(Ⅲ)/SiO2,Ni/SiO2,Co(Ⅱ)/SiO2处理焦化柴油,吸附剂的平衡吸附量分别为22.713×10-3,23.305×10-3,18.480×10-3。

关 键 词:吸附脱氮  改性硅胶  焦化柴油  吸附剂  过渡金属改性硅胶吸附剂

Experimental study on nitride removal from coker diesel by transition metal modified silica gel
Wang Yunfang,Zhang Kun,Jiang Chao,Liu Wei. Experimental study on nitride removal from coker diesel by transition metal modified silica gel[J]. Petrochemical Technology & Application, 2011, 29(4): 299-302
Authors:Wang Yunfang  Zhang Kun  Jiang Chao  Liu Wei
Affiliation:Wang Yunfang1,Zhang Kun2,Jiang Chao3,Liu Wei1(1.College of Chemistry and Chemical Engineering,China University of Petroleum,Qingdao 266555,China,2.Dalian Lubricating Oil Factory,PetroChina,Dalian 116032,3.Shengli Engineering & Consulting Co Ltd,SINOPEC,Dongying 257026,China)
Abstract:The transition metal ions modified silica gel adsorbents Fe(Ⅲ)/SiO2,Co(Ⅱ)/SiO2,Ni(Ⅱ)/SiO2,Cu(Ⅱ)/SiO2 were prepared by loading Fe3+,Co2+,Ni2+ and Cu2+ on silica gel,and then the transition metal modified adsorbents of Fe/SiO2,Co/SiO2 and Ni/SiO2 were obtained by reducing the metal ion modified species in pure hydrogen at 500℃.The effect of adsorption condition on the nitride removal was investigated using coker diesel with nitrogen mass fraction 2.1×10-3 as feedstock separately in an intermittent absorber and a fixed bed absorber at atmospheric pressure.The results showed that the optimal adsorption condition was temperature 120℃,mass ratio of coker diesel to adsorbent 60.The order of equilibrium adsorption capacity from small to big was:Fe(Ⅲ)/SiO2,Ni/SiO2,Co(Ⅱ)/SiO2,Cu(Ⅱ)/SiO2,Fe/SiO2,Ni(Ⅱ)/SiO2,Co/SiO2.When the coker diesel was treated by Fe(Ⅲ)/SiO2,Ni/SiO2,Co(Ⅱ)/SiO2,the equiblibrium adsorption capacity(mass ratio of coker diesel to adsorbent)was 22.713×10-3,23.205×10-3 and 18.480×10-3 respectively.
Keywords:adsorptive denitrogenation  modified silica gel  coker diesel  adsorbent  transition metal modified silica gel adsorbent  
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