期刊文献+

W改性SiO_2催化剂催化氧化脱除苯并噻吩的性能 被引量:1

Catalytic performance of W-modified SiO_2 catalyst in oxidative desulfurization of dibenzothiophene
下载PDF
导出
摘要 采用溶胶-凝胶法制备了W改性SiO2催化剂,并通过X射线衍射(XRD)、红外光谱(FTIR)、N2吸附(BET)、扫描电镜(SEM)等方法对催化剂进行表征。以苯并噻吩(BT)/石油醚模拟油为原料、H2O2为氧化剂,研究了催化剂催化氧化脱硫性能,考察了溶剂及用量、反应温度、氧化剂用量、催化剂用量、反应时间对苯并噻吩脱硫率的影响。结果表明,催化剂中W以WO3晶相存在,引入W后催化剂的比表面积有所降低。在模拟油原料20 mL、催化剂用量0.04 g、H2O2/S摩尔比8、乙腈/模拟油体积比0.3∶1、65℃下反应60 min时,模拟油脱硫率可达99.6%。 The W-modified SiO2 catalyst was prepared by sol-gel method and characterized by X-ray diffraction(XRD),Fourier transform infrared spectroscopy(FT-IR),N2-adsorption specific surface area measurement(BET)and scanning electron microscopy(SEM).The catalytic oxidative desulfurization performance was studied with the simulated oil of benzothiophene(BT)sulfur as feedstock,H2O2 as oxidant.The effects of solvent,solvent dosage,reaction temperature,H2O2 dosage,catalyst dosage and reaction time on desulfurization performance of BT were investigated.The results show that the predominant phase of W in catalyst was WO3,the introduction of W led to the reduction of the specific surface area of catalyst.Under the condition of simulated oil sample 20mL,catalyst 0.04 g,H2O2 /S molar ratio of 8,acetonitrile/simulated oil volume ratio of 0.3∶1,at 65 ℃,reaction time of 60 min,the desulfurization ratio of simulated oil reach to 99.6%.
出处 《化工进展》 EI CAS CSCD 北大核心 2012年第4期833-838,共6页 Chemical Industry and Engineering Progress
关键词 SiO2-0.1WO3 催化氧化 苯并噻吩 脱硫 SiO2-0.1WO3 catalytic oxidation benzothiophene desulfurization
  • 相关文献

参考文献16

  • 1Stanislaus A,Marafi A,Rana M S.Recent advances in the scienceand technology of ultra low sulfur diesel(ULSD)production[J].Catalysis Today,2010,153:1-68. 被引量:1
  • 2Jia Y H,Li G,Ning G L.Effcient oxidative desulfurization(ODS)of model fuel with H2O2 catalyzed by MoO3/γ-Al2O3 under mild andsolvent free conditions[J].Fuel Processing Technology,2011,92:106-111. 被引量:1
  • 3黄绍祥,黎先财,黄晓文,徐庆荣,杨沂凤,刘厚凡.WO_3/SBA-15催化剂的制备及其氧化脱硫性能[J].石油化工,2009,38(12):1281-1285. 被引量:13
  • 4张存,王洪娟,刘涛,刘晓勤.WO_3/ZrO_2固体超强酸催化氧化柴油深度脱硫研究[J].四川大学学报(工程科学版),2011,43(3):176-181. 被引量:7
  • 5Zhu W S,Li H M,Jiang X,et al.Commercially available molybdiccompound-catalyzed ultra-deep desulfurization of fuels in ionicliquids[J].Green Chemistry,2008,10:641-646. 被引量:1
  • 6Yan X M,Mei P,Lei J H,et al.Synthesis and characterization ofmesoporous phosphotungstic acid/TiO2 nanocomposite as a noveloxidative desulfurization catalyst[J].Journal of Molecular CatalysisA:Chemical,2009,304:52-57. 被引量:1
  • 7Sachdeva T O,Pant K K.Deep desulfurization of diesel via peroxideoxidation using phosphotungstic acid as phase transfer catalyst[J].Fuel Processing Technology,2010,91:1133-1138. 被引量:1
  • 8Bordoloi A,Halligudi S B.Studies in structural characterization andcorrelation with the catalytic activity of an efficient and stableWOx/SBA-15 nanocomposite catalyst[J].Journal of Catalysis,2008,257:283-290. 被引量:1
  • 9Rodriguez-Gattorno G,Galano A,Torres-Garc a E.Surfaceacid-basic properties of WOx-ZrO2 and catalytic efficiency inoxidative desulfurization[J].Applied Catalysis B:Environmental,2009,92:1-8. 被引量:1
  • 10陈长松..W-AIPO的合成及其氧化脱硫性能[D].大连理工大学,2008:

二级参考文献103

共引文献59

同被引文献20

引证文献1

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