期刊文献+

聚乙二醇对HPMo/SiO_2结构及其催化氧化脱除二苯并噻吩性能的影响 被引量:4

INFLUENCE OF POLYETHYLENEGLYCOL ON HPMo/SiO_2 STRUCTURE AND ITS PERFORMACE OF OXIDATIVE REMOVAL OF DIBENZOTHIOPHENE
下载PDF
导出
摘要 采用聚乙二醇(PEG6000)为模板剂,以正硅酸乙酯为前躯体,通过沉淀法制备了SiO2负载型磷钼酸(HPMo)催化剂PEG-HPMo/SiO2,并对催化剂进行了FT-IR,XRD,FE-SEM,31P-NMR表征,采用NLDFT平衡模型分析计算了催化剂的比表面积、孔径分布、总孔体积及介孔分率。考察了催化剂使用量、H2O2使用量、反应温度及反应时间对催化氧化脱硫效果的影响。研究结果表明,制备的催化剂PEG-HPMo/SiO2中含有HPMo的Keggin活性结构。对于10 mL模型油(硫质量分数为400μg/g),在催化剂用量0.05g,H2O2用量0.03mL,反应温度50℃,反应时间15 min的条件下,模型油中二苯并噻吩(DBT)的脱除率可以接近100%。催化剂在重复使用6次后,经过简单干燥处理仍有较高活性。 PEG-HPMo/SiO2 catalysts were prepared by precipitation method using PEG6000 as template and tetraethyl orthosilicate(TEOS)as silica source and characterized by Fourier transform infrared spectroscopy(FT-IR),X-ray diffraction(XRD),field emission scanning electron microscope(FE-SEM)and 31 P superconducting nuclear magnetic resonance spectrometer(31P-NMR).The specific surface area,pore size distribution and mesoporous ratio were calculated via the NLDFT equilibrium model.The influence of various parameters including dosage of catalyst,dosage of H2O2,reaction temperature and reaction time on the conversion of DBT was investigated.The results show that PEGHPMo/SiO2 contains the Keggin active structures.For 10 mL model fuel(mass fraction of sulfur element is 400μg/g),DBT in the model oil can be almost totally removed under the conditions of catalyst0.05 g,H2O20.03 mL,reaction temperature 50 ℃ and reaction time 15 min.The catalytic activity of PEG-HPMo/SiO2 is not significantly reduced after the catalyst is reused for 6times.
出处 《石油炼制与化工》 CAS CSCD 北大核心 2015年第10期50-55,共6页 Petroleum Processing and Petrochemicals
基金 国家自然科学基金资助项目(21473126) 高等学校博士学科点专项科研基金资助课题(20124219110002)
关键词 聚乙二醇 磷钼酸 氧化脱硫 二苯并噻吩 polyethyleneglycol phosphomolybdic acid hydrate oxidative desulfurization dibenzothiop
  • 相关文献

参考文献15

二级参考文献120

共引文献86

同被引文献30

  • 1安高军,周同娜,柴永明,张景成,柳云骐,刘晨光.轻质油品非加氢脱硫技术[J].化学进展,2007,19(9):1331-1344. 被引量:33
  • 2詹拥共,蔡炳新,高建军,刘玉章,黄小妮.氧化钼/二氧化硅纳米复合催化剂表面结构及其催化性能[J].硅酸盐学报,2007,35(11):1473-1477. 被引量:4
  • 3朱伯仲,林钰,尚雪亚,刘双月,李新生.钼酸铵的热分解机理研究[J].兰州大学学报(自然科学版),1997,33(3):72-76. 被引量:13
  • 4Garcia-Gutierrez J L, Fuentes G A, Herndndez-Terdn M E, et al. Ultra-deep oxidative desulfurization of diesel fuel with H2O2 catalyzed under mild conditions by polymolybdates supported on Al2O3 [J]. Applied Catalysis A General, 2006, 305(1) :15-20.
  • 5Yan Xuemin, Mei Zhankui, Mei Ping. Self-assembled HPW/ silica-alumina mesoporousnanocomposite as catalysts for oxi dative desulfurization of fuel oil[J]. Journal of Porous Mate- rials,2014,21(5) :729-737.
  • 6Wang Guangjian,Zhang Jiankang, Liu Ying. Catalytic oxida- tive desulfurization of benzothiophene with hydrogen perox ide over Fe/AC in a biphasic model diesel-acetonitrile system [J]. Korean J Chem Eng,2013,30(8) :1559-1565.
  • 7Qian Eika W. Development of novel nonhydrogenation process-oxldative desulfurization of dlstillate[J]. Journal of the Japan Petroleum Institute, 2008,51 (1) : 14-31.
  • 8Wang Danhong,Qian Eika W,Amano H,et al. Oxidative des- ulfurization of fuel oil. Part 1. Oxidation of dibenzothiophenes using tert-butyl hydroperoxide[J]. Applied Catalysis A Gen- eral,2003,253(1) :91-99.
  • 9Li Xiang, Liu Luda, Wang Anjie. Creation of oxygen vacan- cies in MoOa/SiO2 by thermal decomposition of pre-impreg nated citric acid under N2 and their positive role in oxidative desulfurization of dibenzothiophene[J]. Catal Lett, 2014,144 (3) :531-537.
  • 10Dou Jian, Zeng Huachun. Integrated networks of meso- poroussilica nanowires and their bifunctionalcatalysis-sorp- tion application for oxidative desulfurization[J]. ACS Cataly- sis. 2014,4(2) : 566-576.

引证文献4

二级引证文献7

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部