[1] 李立权.催化裂化汽油加氢技术工程化的问题及对策[J].炼油技术与工程,2010,40(11):5-9.[2] Nocca J I . The Domino interaction of refinery processes for gasoline quality attainment [C]//NPRA Annual Meeting.AM -00-61,2000[3] G.J. Antos, R.B. Solari, R.Monque. Hydroprocessing to produce reformulated gasolines: The ISALTM process[J]. Studies in Surface Science and Catalysis, 1997, 106(1): 27-40.[4] Malmaison R., Nocca J. I. Prime-G+TM commercial performance of FCC naphtha desulfurization technology. NPRA 2003 annual meeting[C]. SanAntonio, Texas. NPRA AM-03-26, 2003.[5] T.G. Kaufmann, A. Kaldor, G.F. Stuntz, at al. Catalysis science and technology for cleaner transportation fuels [J]. Catalysis Today, 2000,62(1): 77-90.[6] I. V. Babich, J. A. Moulijn. Science and technology of novel processes for deep desulfurization of oil refinery streams: a review [J]. Fuel, 2003,82(6): 607-631.[7] 兰玲,鞠雅娜. 催化裂化汽油加氢脱硫(DSO)技术开发及工业试验 [J]. 石油炼制与化工,2010,41(11):53-55.[8] 兰玲,钟海军,鞠雅娜,吴平易.催化裂化汽油选择性加氢脱硫催化剂及工艺技术开发[J]. 石油科技论坛,2013,1:53-56.[9] 张学军,齐铁忠,赵秦峰等.催化裂化汽油预加氢催化剂GHC-32的工业应用试验[J]. 石油炼制与化工,2014,45(5):34-37.[10] 张学军,袁晓亮,侯远东等.催化裂化汽油预加氢催化剂的开发与评价[J]. 当代化工,2014,34(6):105-107