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催化裂化汽油选择性加氢脱硫前后组成分析 被引量:3

Composition analysis of fluidized-bed catalytic cracking gasoline before and after selective hydrodeslfurization
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摘要 采用色谱、质谱、元素分析、电位计等分析手段研究了中国石化石家庄炼油化工股份有限公司催化裂化汽油选择性加氢脱硫前后组成的变化。结果表明:加氢前后汽油中的氮化物均主要为碱性氮化物,加氢后总氮质量分数减少12.1个百分点,碱性氮化物质量分数减少8.3个百分点;汽油中的酚类主要为C1~2苯酚,苯酚和C3苯酚含量很少,加氢前后汽油中酚类的质量分数分别为0.14%和0.05%;加氢前汽油中的硫化物主要为噻吩和硫醚,硫醇含量较少且为C5~8硫醇;加氢后汽油中的硫化物主要为噻吩和硫醇,硫醚含量较少;加氢前后,硫醇质量分数由48.9×10-6降低到15.6×10-6,总硫质量分数由924.6×10-6降低到43.0×10-6;加氢后汽油的异构烷烃质量分数增加5.55个百分点,烯烃质量分数降低10.12个百分点(饱和率为31%),环烷烃质量分数增加2.95个百分点。 A series of analytical methods such as chromatograghy,mass spectrometry,elementary analysis and potentiometer,were used for analyzing the composition of fluidized-bed catalytic cracking(FCC) gasoline of Shijiazhuang Refinery before and after selective hydrodesulfurization(SHDS).The results showed that the nitrogen compounds were mainly composed of basic nitrogen,and after SHDS the mass fractions of total nitrogen and basic nitrogen decreased by 12.1 and 8.3 percentage points respectively,and the species of basic nitrogen remained unchanged.The phenols compounds were mainly consisted of C1 and C2 phenol,including a little C3 phenol and phenol.And the mass fractions of phenols were 0.14% and 0.05% respectively before and after SHDS.The mass fraction of mercaptan was decreased from 48.9×10-6 to 15.6×10-6,and total sulfur decreased from 924.6μg/g to 43μg/g after SHDS.The mass fractions of the isoparaffins and the cycloparaffins increased by 5.55 and 2.95 percentage points respectively and the mass fraction of olefin decreased by 10.12 percentage points after SHDS.
出处 《石化技术与应用》 CAS 2011年第1期72-77,共6页 Petrochemical Technology & Application
关键词 催化裂化汽油 选择性加氢脱硫 氮化物 酚类 硫化物 族组成 fluidized-bed catalytic cracking gasoline selective hydrodesulfurization basic nitride phenols sulfide group composition
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  • 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
  • 2刘晓欣,王艳涛,赵乐平,刘继华.FCC汽油选择性加氢脱硫降烯烃工艺技术的工业应用[J].石油炼制与化工,2006,37(8):44-48. 被引量:29
  • 3刘继华,赵乐平,方向晨,宋永一.FCC汽油选择性加氢脱硫技术开发及工业应用[J].炼油技术与工程,2007,37(7):1-3. 被引量:20
  • 4Thomas R H, Garland B B. Technology options for meeting low sulfur mogas targets[ C ]//NPRA annual Meeting, San Antonio, Texas,2000, AM-00-11.
  • 5Debuisschert Q, Nocca J. Prime-G + TM commercial performance of FCC naphtha desulfurization technology[ C]//NPRA annual meeting, San Antonio, Texas, 2003, AM-03 -26.
  • 6胜利石油化工总厂炼油厂.胜利焦化汽油不安定组分的气相色谱分析及焦化汽油变质变色原因的考察[J].石油炼制,1975,6(2):33-41.
  • 7NAGPAL J M, JOSHI G C, RASTOGI S N. Stability of cracked naphthas from thermal catalytic processes and their additive response[J]. Fuel, 1995, 74(5): 714-719.
  • 8Malmaison R, Nocca J L. Prime-G+^TM commercial performance of FCC naphtha desulfurization technology. NPRA 2003 annual meeting. San Antonio,Texas. NPRA AM-03-26,2003
  • 9中国石油化工股份有限公司科技开发部.SH/T0162-1992,石油产品中碱性氮测定法,中国石化出版社
  • 10Changlong Yin, Daohong Xia. A study of the distribution of sulfur compounds in gasoline produced in China. Part 1. A method for the determination of distribution sulfur compounds in light petroleum and gasoline [ J ]. Fuel. 80 ( 2001 ) 607 - 610.

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