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催化裂化提升管进料段的优化 被引量:6

OPTIMIZATION DESIGN OF FEEDSTOCK INJECTION-MIXING ZONE OF FCC RISER
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摘要 通过分析冷模实验的结果,并结合催化裂化提升管的实际操作情况,揭示了催化裂化提升管进料混合段内存在的问题:由于射流二次流的产生,在进料段内局部区域催化剂颗粒相返混严重并且油剂两相浓度分布并不匹配——在油相浓度高(低)的位置,剂相浓度却较低(高)。并介绍了一种能够有效地利用和控制二次流的CS型雾化喷嘴,工业应用的结果表明CS喷嘴对提升管内油、剂两相流动、混合状况有明显地改善,可有效地提高液收、降低结焦。 In the FCC units,two disadvantages of the traditional structure of FCC riser feedstock injection- mixing zone,namely the intense particle backmixing and the unanticipated distributions of oil-catalyst- concentration,are revealed.The principle of impro- ving the flow and mixing pattern in the feedstock in- jection-mixing zone is put forward,i.e.utilizing the favorite aspect of the jet secondary flow while dimin- ishing its disadvantageous influence.A new type of FCC CS-atomizing-nozzle is proponed.The advan- tages brought about by CS-Nozzle are seen clearly in several industrial FCC units.
出处 《石油化工设计》 CAS 2007年第1期18-20,共3页 Petrochemical Design
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参考文献8

  • 1Lomas, D. A. FCC Riser with Transverse Feed Injection [P],US, 5139748. 1992.
  • 2Mauleon,J. L., M. Demar, and J. B. Sigaud. The Method for the Injection of Catalyst in a Fluid Catalytic Cracking Process,Especially for Heavy Feedstock[P], US, 4832825. 1989.
  • 3Maroy, J. D.. Process and Apparatus for Contacting a Hydrocarbon Feedstock with the Hot Solid Particles in Tubular Reactor with a Rising Fluidizecl Bed[P] ,US,5348644. 1994.
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  • 6范怡平,叶盛,卢春喜,时铭显.提升管反应器进料混合段内气固两相流动特性(Ⅰ)实验研究[J].化工学报,2002,53(10):1003-1008. 被引量:30
  • 7范怡平.新型催化裂化提升管进料混合段结构的开发[D],北京:博士后出站报告,石油大学(北京),2003.
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二级参考文献14

  • 1Fan Y P, Ye Sh, Lu Ch X, et al. Gas-solid two phase flow in FCC riser[J]. AIChE J, 2002, 48 (9): 1869-1887.
  • 2Albrecht A, Simonin O, Barthod D, et al. Multidimensional numerical simulation of the liquid feed injection in a industrial FCC riser[J]. CFB-10 preprints, 2001, 349-353.
  • 3Lomas D A. FCC riser with transverse feed injection[P]. USP: 5139748, 1992.
  • 4Mauleon J L, Demar M, Sigaud J B. The method for the injection of catalyst in a fluid catalytic cracking process, especially for heavy feedstock[P]. USP: 4832825, 1989.
  • 5Maroy J D. Process and apparatus for contacting a hydrocarbon feedstock with the hot solid particles in tubular reactor with a rising fluidized bed[P].USP: 5348644, 1994.
  • 6Miller A, Gidaspow D G. Dense, vertical gas-solid flow in a pipe[J]. AIChE J, 1992, 38(11): 1801-1805.
  • 7Thelogs K N, Nikou I D, Lygeros A I, et al. On the simulation of fluid catalytic cracking riser-type reactors[J]. CFB-5 preprints, MSS5 1996 : 1-6.
  • 8范怡平. 新型催化裂化提升管进料混合段结构的开发[R]. 博士后出站报告, 北京:石油大学, 2003.
  • 9Xu Guangwen(许光文). In: Yang Guanghua(杨光华), eds.The Symposium of 7th Conference of National Chemical Engineering(第七届全国化学工程论文报告会).Beijing:NCCE(中国化工学会化学工程专业委员会),1994.991-994
  • 10GaoJinsen(高金森). Numerical Simulatiion on the Flow, Heat-Transfer and Reaction in the Catalytic Cracking Riser Reactors:[dissertation] (学位论文). Beijing: Petroleum of University,1997

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