首页 | 本学科首页   官方微博 | 高级检索  
     

镧氧化物对体相MoP加氢脱氮反应性能的影响
引用本文:徐艳春,李翔,王安杰,遇治权,陈永英.镧氧化物对体相MoP加氢脱氮反应性能的影响[J].石油学报(石油加工),2018,34(1):115-122.
作者姓名:徐艳春  李翔  王安杰  遇治权  陈永英
作者单位:1. 大连理工大学 精细化工国家重点实验室,辽宁 大连116024; 2. 辽宁省高校石油化工技术与装备重点实验室,辽宁 大连 116024
基金项目:国家自然科学基金(21473017和21673029)、国家自然科学基金辽宁省联合基金(U1508205)及辽宁省自然科学基金(201602158)项目资助
摘    要:采用共沉淀法制备了体相MoP催化剂和La2O3改性的MoP催化剂,用XRD、N2物理吸附及TEM等手段对催化剂进行表征。以喹啉及其加氢中间体十氢喹啉(DHQ)为模型含氮化合物,研究了这些催化剂的加氢脱氮反应性能。结果表明,La2O3是MoP催化剂的有效助剂,同时促进了MoP的加氢活性和C-N键断裂活性,但抑制了DHQ的脱氢。当La/Mo摩尔比大于02时,增加La2O3含量能够显著提高催化剂的比表面积。La2O3含量过高主要生成LaPO4。La2O3改性的MoP催化剂的活性随La/Mo摩尔比增加而增加。当La/Mo摩尔比大于03(催化剂记为La MoP(03))时,继续增加La2O3含量对催化剂活性影响不大。La MoP(03)中活性相分散度高于MoP催化剂,并且活性相主要呈棒状,不同于MoP催化剂的卵石状。催化剂的性能与其比表面积或分散度之间没有直接联系。喹啉在这些催化剂上主要通过DHQ路径脱氮,引入La2O3对喹啉HDN反应的促进作用比对DHQ的HDN反应更为显著。

关 键 词:加氢脱氮  MoP  镧氧化物  喹啉  助剂  
收稿时间:2017-05-08

Influence of Lanthanum Oxide on the Hydrodenitrogenation Performance of Bulk MoP
XU Yanchun,LI Xiang,WANG Anjie,YU Zhiquan,CHEN Yongying.Influence of Lanthanum Oxide on the Hydrodenitrogenation Performance of Bulk MoP[J].Acta Petrolei Sinica (Petroleum Processing Section),2018,34(1):115-122.
Authors:XU Yanchun  LI Xiang  WANG Anjie  YU Zhiquan  CHEN Yongying
Affiliation:1. State Key Laboratory of Fine Chemicals, Dalian University of Technology, Dalian 116024, China; 2. Liaoning Key Laboratory of Petrochemical Technology and Experiment, Dalian 116024, China
Abstract:Bulk MoP and La2O3 modified MoP catalysts were prepared by a co precipitation method, and characterized by XRD and N2 physisorption methods. The hydrodenitrogenation (HDN) performances of the catalysts were studied using quinoline and decahydroquinoline (DHQ) as the model nitrogen containing compounds. The results indicate that La2O3 is an effective promoter for the MoP HDN catalyst. It enhances both the hydrogenation activity and the C-N bond cleavage activity of MoP but inhibits the dehydrogenation of DHQ. At La/Mo molar ratio above 02, the specific surface area and the dispersion of the catalyst become higher with the increasing of La2O3 content. At high La/Mo molar ratio, LaPO4 is the major phase in the catalyst. Thus, the activity of the catalysts is increasing along with the La/Mo molar ratio. At the La/Mo ratio above 03 (the catalyst is denoted as La MoP(03)), the activity of the catalysts is almost not affected by further increasing the La2O3 content. The dispersion of active phase in La MoP(03) is higher than that of MoP. Rod like and pebble shaped active phases are observed in La MoP(03) and MoP, respectively. There is no relation between the HDN performances and specific surface areas and the dispersions of the La2O3 containing catalysts. The HDN of quinoline over the MoP catalysts occurs mainly through the DHQ pathway, and the HDN of quinoline is significantly enhanced by the addition of La2O3 than the HDN of DHQ.
Keywords:hydrodenitrogenation  MoP  lanthanum oxide  quinoline  promoter  
本文献已被 CNKI 等数据库收录!
点击此处可从《石油学报(石油加工)》浏览原始摘要信息
点击此处可从《石油学报(石油加工)》下载全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号