丙烷脱沥青油的催化裂化性质研究
详细信息    查看全文 | 推荐本文 |
  • 英文篇名:Catalytic Cracking Property of Propane Deasphalted Oil
  • 作者:邓益强 ; 程丽华 ; 杨月 ; 沈健 ; 廖定满
  • 英文作者:Deng Yiqiang;Cheng Lihua;Yang Yue;Shen Jian;Liao Dingman;Guangdong University of Petrochemical Technology;Liaoning Shihua University;Institute of Maoming Petrochemical Company;
  • 关键词:减压渣油 ; 催化裂化油浆 ; 脱沥青油 ; 催化裂化
  • 英文关键词:Vacuum residuum;;FCC slurry oil;;Deasphalted oil;;Catalytic cracking
  • 中文刊名:SYHX
  • 英文刊名:Journal of Petrochemical Universities
  • 机构:广东石油化工学院;辽宁石油化工大学;茂名石化公司研究院;
  • 出版日期:2018-01-09 15:15
  • 出版单位:石油化工高等学校学报
  • 年:2018
  • 期:v.31;No.129
  • 基金:广东省公益研究与能力建设项目(2014A010105051,2014A020216047);; 茂名市科技计划项目(201525);; 广东石油化工学院科研基金项目(2015rc04)
  • 语种:中文;
  • 页:SYHX201801003
  • 页数:4
  • CN:01
  • ISSN:21-1345/TE
  • 分类号:15-18
摘要
在前期丙烷脱沥青工艺得到不同脱沥青油的基础上,通过固定流化床反应装置,在反应温度490℃,剂油质量比为5(催化剂为80g),空速15h-1的实验条件下,研究了脱沥青油的催化裂化性能。结果表明,饱和分质量分数最高的减压渣油的丙烷脱沥青油是很好的催化裂化原料;减压渣油和减压渣油掺兑催化油浆所得的丙烷脱沥青油也具有较好的轻油选择性和产物分布;但催化油浆的丙烷脱沥青油作催化裂化原料时,其转化率、轻油收率最低,裂化性能较差。
        The catalytic cracking performances of several propane deasphalted oil obtained in our earlier work were investigated in a fixed fluidized bed reactor at the reaction temperature of 490 ℃,catalyst to oil mass ratio of 5(catalysts 80 g)and space velocity of 15 h-1.It was found that the propane deasphalting oil with the highest saturated fraction mass fraction of vacuum residuum was a good FCC feedstock.the product distribution and selectivity of the deasphalted oil from vacuum residuum blending FCC slurry oil were better than that from FCC slurry oil.But for the deasphalted oil from FCC,slurry oil had lower conversion and light oil yield,and the cracking performance was also poor.
引文
[1]刘永红,王万真,杨军朝.催化裂化-溶剂脱沥青组合工艺的应用[J].石油炼制与化工,2003,34(11):63-65.Liu Y H,Wang W Z,Yang J Z.Application of the combination process of catalytic cracking and solvent deasphlating[J].Petroleum Processing and Petrochemicals,2003,34(11):63-65.
    [2]袁晓云,赵飞,魏广春,等.溶剂脱沥青-催化裂化工艺的优化组合及其应用[J].炼油技术与工程,2011,41(5):6-9.Yuan X Y,Zhao F,Wei G C,et al.Optimized integration of solvent deasphalting-FCC process and aplication[J].Petroleum Refinery Engineering,2011,41(5):6-9.
    [3]范雨润,孙鉴.丙烷脱沥青工业装置掺炼催化裂化油浆[J].石油炼制与化工,1998,29(8):6-9.Fan Y R,Sun J.Commercial application of blending FCC slurry into propane deasphalting feedstock[J].Petroleum Processing and Petrochemicals,1998,29(8):6-9.
    [4]杨月,沈健,程丽华,等.掺入催化裂化油浆对减压渣油性质的影响[J].石油炼制与化工,2016,47(6):48-52.Yang Y,Shen J,Cheng L H,et al.Effect of blending FCC slurry on properties of vacuum residue[J].Petroleum Processing and Petrochemicals,2016,47(6):48-52.
    [5]Stratiev D,Shishkova I,Tsaneva T,et al.Investigation of relations between properties of vacuum residual oils from different origin,and of their deasphalted and asphaltene fractions[J].Fuel,2016,170:115-129.
    [6]Cabrales-Navarro F A,Pereira-Almao P.Catalytic steam cracking of a deasphalted vacuum residue using a Ni/K ultradispersed catalyst[J].Energy&Fuels,2017,31(3):3121-3131.
    [7]赵光辉,马克存,孟锐.炼厂催化裂化外甩油浆的分离技术及综合利用[J].现代化工,2006,26(1):20-23.Zhao G H,Ma K C,Meng R.Separating technique and integrated utilization of FCC slurry in refining petroleum[J].Modern Chemical Industry,2006,26(1):20-23.
    [8]Hamidi Z M,Khorasheh F,Ivakpour J,et al.Improvement of the thermal cracking product quality of heavy vacuum residue using solvent deasphalting pretreatment[J].Energy&Fuels,2016,30(12):10322-10329.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700