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THE DEVELOPMENT OF FCC STRIPPING TECHNOLOGY 被引量：2

THE DEVELOPMENT OF FCC STRIPPING TECHNOLOGY
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摘要 This article briefly describes the major patents domestic and the abroad, and the current situation and achievements of FCC stripping technology in China. The developing trend of FCC stripping technology is presented, including further developments of FCC stripper to improve unit performance, combination of the stripper and pre stripper within disengager to form a complete high efficiency FCC stripping system. In addition to high efficiency, simple structure and easiness of installation and maintenance for a new FCC stripper are all of consideration. This article briefly describes the major patents domestic and the abroad, and the current situation and achievements of FCC stripping technology in China. The developing trend of FCC stripping technology is presented, including further developments of FCC stripper to improve unit performance, combination of the stripper and pre stripper within disengager to form a complete high efficiency FCC stripping system. In addition to high efficiency, simple structure and easiness of installation and maintenance for a new FCC stripper are all of consideration.
作者 ZHANG Zhen qian (Equipment Research Institute of Luoyang Petrochemical Engineering Corp., SINOPEC,Luoyang 471003, China)
出处 《石油学报（石油加工）》 EI CAS CSCD 北大核心 2003年第1期62-66,共5页 Acta Petrolei Sinica(Petroleum Processing Section)
关键词 炼油 催化裂化 汽提 技术进展 catalyst stripping stripper steam technology development FCC
分类号 TE624.41 [石油与天然气工程—油气加工工程]
  • 相关文献

参考文献14

  • 1Lin Sh X. Petroleum Refining Engineering[ M], Petroleum Publish House, 1988.
  • 2Haddad, et al. FCC Catalyst stripping method[P]. USP: 4,605,491, 1986.
  • 3Cetinkaya, et al. FCC Stripping apparatus[P]. USP: 4,927,606, 1990.
  • 4Cetinkaya. FCC Stripping method[P]. USP: 5,015,363, 1991.
  • 5Kruse. Catalytic cracking unit with combined catalyst separator and stripper[P]. USP: 5,112,576, 1992.
  • 6Ismail B, et al. Side mounted FCC stripper with two-zone stripping[P]. USP: 5,474,669,1995.
  • 7Zinke. FCC Stripper with spoke arrangement for bi-directional catalyst stripping[ P]. USP: 5,549,814, 1996.
  • 8Lomas. FCC Separation method and apparatus with improved stripping[P]. USP: 5,584,985, 1996.
  • 9Senior. FCC Unit catalyst stripper[ P]. USP: 5,910,240, 1999.
  • 10Senegas, et al. Process and apparatus for stripping fluidized solids and use thereof in a fluid cracking process[P]. USP: 5,716,585.

二级参考文献8

  • 1[1]Haddad, et al. FCC catalyst stripping method. US, US 4 605 491.1986
  • 2[2]Cetinkaya, et al. FCC Stripping apparatus. US, US 4 927 606.1990
  • 3[3]Cetinkaya. FCC stripping method. US, US 5 015 363.1991
  • 4[4]Kruse. Catalytic cracking unit with combined catalyst separator and stripper. US, US 5 112 576.1992
  • 5[5]Johnson, et al. FCC catalyst stripper. US, US 5 531 884.1996
  • 6[6]Zinke. FCC stripper with spoke arrangement for bi-directional catalyststripping. US, US 5 549 814.1996
  • 7[7]Lomas. FCC separation method and apparatus with improved stripping.US, US 5 584 985.1996
  • 8[8]Senior. FCC unit catalyst stripper. US, US 5 910 240.1999

共引文献24

同被引文献33

  • 1于国庆,高金森,徐春明.重油催化裂化装置汽提段及汽提工艺研究进展[J].当代化工,2004,33(2):68-71. 被引量：13
  • 2张永民,卢春喜,时铭显.催化剂汽提器内气固传质特性的研究[J].高校化学工程学报,2004,18(4):409-413. 被引量：24
  • 3周遊,鲁维民,郑冲,秦霁光.多孔挡板导流筒型流化床内构件研究[J].化工冶金,1995,16(2):143-150. 被引量：6
  • 4张振千,田耕.FCC待生催化剂多级组合式汽提器的开发[J].炼油技术与工程,2006,36(9):12-16. 被引量：7
  • 5RICHARD R R,DEMULDER B.New internal for maximizing performance of FCC catalyst strippers[R].San Francisco:Twelfth Refining Seminar,2000.
  • 6SENIOR R C,SMALLEY C G,GBORDZOE E.Hardware modifications to overcome common operating problems in FCC catalyst strippers[C]//L S FAN,T M KNOWLTON Eds.Fluidization IX.New York:Engineering Foundation,1998,725-732.
  • 7RIVAULT P,NGUYEN C,LAGUERIE C,et al.Countercurrent stripping dense circulating beds effect of the baffles[C]//Fluidization Ⅷ.J F LARGE,C LAGUERIE Eds.New York:Engineering Foundation,1995,491-499.
  • 8PADYEN S,KONWLTON T M,ARASTOOPOUR H.Stripping in recirculating bubbling fluidized bed using group A particles[C]//Fluidization X.M KWAUK,J LI,W C YANG Eds.New York:Engineering Foundation,2001,581-588.
  • 9MCKEEN T,PUGSLEY T.Simulation of cold flow FCC stripper hydrodynamics at small scale using computational fluid dynamics[J].Int J Chem React Eng,2003,1,A18.
  • 10MCKEEN T,PUGSLEY T.Simulation and experimental validation of a freely bubbling bed of FCC catalyst[J].Powder Technology,2003,129,139-152.

引证文献2

二级引证文献7

石油学报（石油加工）
2003年 第1期

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