摘要介绍扬子石化有限公司裂解汽油加氢装置的工艺流程 ,设计特点 。Introduce pyrolysis gasoline hydrotreating unit for YPC technological process, characteristics, reconstructing concept, etc.
3HATANAKA S,YAMADA M,SADAKANE O. Hydrodesulfurization of catalytic cracked gasoline: 1 Inhibiting effects of olefins on HDS of Alkyl(Benzo)thiophenes contained in catalytic cracked gasoline[J]. Ind Eng Chem Res,1997,36(5): 1519-1523.
4ANDERSSON P-O F,PIRJAMALI M,JRS S G,BOUTONNET-KIZLING M. Cracking catalyst additives for sulfur removal from FCC gasoline[J]. Catal Today,1999,53(4): 565-573.
5GIRGIS M J,GATES B C. Reactivities,reaction networks,and kinetics in high-pressure catalytic hydroprocessing[J]. Ind Eng Chem Res,1991,30(9): 2021-2058.
6SHAFI R,HUTCHINGS G J. Hydrodesulfurization of hindered dibenzothiophenes: An overviews[J]. Catal Today,2000,59(3-4): 423-442.
7OROZCO E O,VRINAT M. Kinetics of dibenzothiophene hydrodesulfurization over MoS2 supported catalysts: modelization of the H2S partial pressure effect[J]. Appl Catal A,1998,170(2): 195-206.
8屈锦华.[D].北京: 北京化工大学,2001.
9BIANCHINI C,MELI A,VIZZA F. Role of single-site catalysts in the hydrogenation of thiphenes: from models systems to effective HDS catalysts[J]. J Organomet Chem,2004,689(24): 4277-4290.
10BORGNA A,HENSEN E J M,VAN VEEN J A R,NIEMANTSVERDRIET J W. Intrinsic kinetics of thiophene hydrodesulfurization on a sulfided NiMo/SiO2 planar model catalyst[J]. J Catal,2004,221(2): 541-548.