期刊文献+

缠绕管式换热器在连续重整装置中的应用 被引量:2

Application of Spiral Wound Heat Exchanger in CCR Unit
下载PDF
导出
摘要 连续重整装置是以石脑油为原料,在催化剂作用下生产芳烃和高辛烷值汽油组分的重要装置,同时还为加氢装置提供大量的廉价氢源。在连续重整装置中,重整进料换热器的选型对产品结构和经济效益都有重要影响。洛阳石化70×10~4t/a连续重整装置选用板壳式换热器,内漏严重,用缠绕管式换热器替代板壳式换热器,既能满足装置的传热要求,拥有优良的传热工艺性能,又具有耐高温高压、抗操作波动的特点,是连续重整装置中较为理想的高效、高可靠性设备。缠绕管式换热器替代板壳式换热器,节省成本553万元;装置3.5MPa蒸汽和燃料气消耗量明显减少,同时产品结构得到优化,提高了主产品氢气和重整汽油的产率以及重整汽油的辛烷值;重整生成油液体收率可以达到84%左右,芳烃含量可以达到77%左右,每年为企业综合节能创效8681.7万元。 Continuous catalytic reforming (CCR) unit is an important unit which converts naphtha into aro- matics and high octane gasoline components in the presence of catalysts.Also it supplies a large amount of cheap hydrogen for hydrogenation unit.The selection of feed heat exchanger for CCR unit greatly influences the product mix and economic benefit.Hate and shell heat exchanger Company for its 700kt/a CCR unit,but serious inner leakage was found.S isfy the heat transfer requirements of the unit,has excellent of high temperature resistance ,high pressure resistance and was selected by SINOPEC Luoyang piral wound heat exchanger can sat- heat transfer performance ,and has characteristics operation fluctuation resistance,so it is an ideal device with high efficiency and high reliability for CCR unit.Replacing the plate and shell heat exchanger with spiral wound heat exchanger can reduce the cost by 5.53 million Yuan,remarkably reduce the consump- tions of 3.5MPa steam and fuel gas,optimize the product mix ,and improve the yields of main product hydro- gen and reformed gasoline and the octane number of reformed gasoline.The liquid yield of reformate may reach 84%,the aromatic content may reach 77%,and a comprehensive energy saving benefit of 86.871 mil- lion Yuan can be created annually for the enterprise.
作者 阮付军
出处 《中外能源》 CAS 2017年第11期84-89,共6页 Sino-Global Energy
关键词 连续重整 缠绕管式换热器 节能 效益分析 continuous catalytic reforming spiral wound heat exchanger energy saving benefit analysis
  • 相关文献

参考文献5

二级参考文献44

  • 1催化重整及芳烃装置工程设计40年文集.中石化北京设计院,1999.
  • 2李成栋.催化重整装置技术问答.中国石化出版社,2005.
  • 3张周卫.双股流螺旋缠绕管式换热器设计计算方法[P].中国:201210303321.X,2013-01.
  • 4张周卫.单股流螺旋缠绕管式换热器设计计算方法[P].中国:201210297815.1,2012-09.
  • 5尹接喜.缠绕管式热交换器设计计算研究[D].北京,清华大学热能工程系,1997.
  • 6徐宏.新型高效换热器在石油化工生产中的应用[C]//中国机械工程学会:中国机械工程学会压力容器分会论文集,北京:[出版者不详],2011:101-110.
  • 7Pacio J C,Dorao C A.A Review on Heat Exchanger Thermal Hydraulic Models for Cryogenic Applications[J].Cryogenics,2011,51(7):366-379.
  • 8Deshpande G N,Sali N V.Experimental Investigation of Performance of Spiral Coil in Spiral Tube Heat Exchanger[J].Applied Mechanics&Materials,2014,592/594:1564-1569.
  • 9Lu X,Du X P,Zeng M,et al.Shell-side Thermal-hydraulic Performances of Multilayer Spiral-wound Heat Exchangers under Different Wall Thermal Boundary Conditions[J].Applied Thermal Engineering,2014,70(2):1216-1227.
  • 10Shirgire N D,Thakur A K,Singh S.Comparative Study and Analysis between Helical Coil and Straight Tube Heat Exchanger[J].International Journal of Engineering Research&Applications,2014,4(8):130-133.

共引文献46

同被引文献10

引证文献2

二级引证文献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