期刊文献+

H_2S含量对加氢汽油中硫醇的影响 被引量:2

Impact of H_2S on mercaptan in hydrotreated gasoline
下载PDF
导出
摘要 考察了Hydro-GAP技术循环氢中H2S含量对加氢汽油中硫醇的影响。结果表明,当循环氢中H2S体积分数低于0.06%时,加氢汽油中的硫醇含量与氢气单程通过时相当;当循环氢中H2S体积分数达到0.25%时,加氢汽油中的硫醇含量显著提高。在循环氢中H2S含量一定时,加氢汽油中的硫醇含量随反应温度的升高而降低。反应温度由260℃提高至380℃,循环氢中H2S体积分数为0.25%时,加氢汽油中的硫醇的质量分数由172μg/g降到42μg/g,降低幅度达到75.6%。由于Hydro-GAP技术采用较高的反应温度,并且催化剂上含有丰富的酸性中心,因而对烯烃与H2S反应生成硫醇具有抑制作用。 The impact of H2S in recycle hydrogen in Hydro-GAP process on mercaptan in hydrotreated gasoline is investigated. The results show that, when H2S in recycle hydrogen is lower than 0.06%, the mer- captan in hydrotreated gasoline is close to that in single pass of hydrogen. When H2S in recycle hydrogen is as high as 0.25%, the mercaptan in hydrotreated gasoline is apparently increased. At a fixed H2S in recycle hy- drogen, the mercaptan in hydrotreated gasoline goes down with rising reaction temperature. When the reaction temperature is raised to 380 ℃ from 260℃ and HiS in recycle hydrogen is 0.25%, the mercaptan in hydro- treated gasoline is reduced to 42 ppm from 172 ppm, which is a 75% reduction. As Hydro-GAP process is op- erated at a higher reaction temperature, and the catalyst have a large amount of active sites, it has an inhabita- tion effect on the reaction of olefins with H2S to produce mercaptan.
出处 《炼油技术与工程》 CAS 2013年第4期24-26,共3页 Petroleum Refinery Engineering
关键词 硫醇 H2S 催化裂化汽油加氢 循环氢 mercaptan, H2S, hydrptreating of FCC gasoline, recycle hydrogen
  • 相关文献

参考文献4

  • 1赵乐平,庞宏,尤百玲,刘继华.硫化氢对催化裂化汽油重馏分加氢脱硫性能的影响[J].石油炼制与化工,2006,37(7):1-5. 被引量:21
  • 2Hatanaka S, Yanmada M. Hydrodesulfurization of catalytic cracked gasoline [ J]. Ind Eng Chem Res, 1997 ( 36 ) : 5110- 5117.
  • 3Rana M S, Navarro R, Leglise J. Competitve effects of nitrogen and sulfur content on activity of hydrotreating CoMo/A1203 cata- lysts : a batch reactor study [ J ]. Catalysis Today, 2004 ( 98 ) : 67- 72.
  • 4Makoto Toba, Yasuo Miki, Takashi Masaru, et al. Reactivity of olefins in the hydrodesulfurization of FCC gasoline over CoMo sul- fide catalyst[ J. Appl. Catal. B :Environ,2007(70) :542-547.

二级参考文献7

  • 1Malmaison R, Nocca J I.. Prime-G^+TM commercial performance of FCC naphtha desulfurization technology. NPRA 2003 annual meeting. San Antonio,Texas. NPRA AM-03 26,2003
  • 2Hatanaka S, Yanmada M. Hydrodesulfurization of cratalytic cracked gasoline. Ind Eng Chem Res,1997,36:1519-1523
  • 3Rana M S,Navarro R,Leglise J. Competitive effects of nitrogen and sulfur content on activity of hydrotreating CoMo/Al2O3 catalysts : a batch reactor study. Catalysis Today, 2004,98 : 67-72
  • 4Cook B R,Ernst R H,Demmin R A. High temperature depressurization for naphtha mercaptan removal. US Pat Appl, US6387249. 2002
  • 5尚琪,汤大钢.控制车用汽油有害物质降低机动车排放[J].环境科学研究,2000,13(1):32-35. 被引量:50
  • 6范志明,柯明,刘溆蕃,谢宗壁,陈晓林.催化裂化汽油无碱脱臭II型工业化试验[J].炼油设计,2000,30(7):17-19. 被引量:4
  • 7赵乐平,周勇,段为宇,梁永超,徐志达,李立权,薛浩.OCT-M催化裂化汽油选择性加氢脱硫技术[J].炼油技术与工程,2004,34(2):6-8. 被引量:73

共引文献20

同被引文献27

引证文献2

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