[1] 赵野,张文成,郭金涛,等.清洁柴油的加氢技术进展[J]. 工业催化,2008, 16(1):10-17. [2] LI D D.Pertroleum refining technologies and catalysis in the 21st century[J].Acta Petrolei Sinica,2005, 21(3):17-25. [3] 朱丹.国内清洁柴油的加氢技术进展[J].华工科技市场,2010, 33(3):4-8. [4] 边思颖,边钢月,张福琴.炼油行业发展清洁燃料面临的形势分析[J].中外能源,2010, 15(7):73-80. [5] LI D D.Crucial technologies supporting future development of petroleum refining industry[J].Chinese Journal of Catalysis,2013, 34(1):48-60. [6] FANG X C, GUO R, YANG C M.The development and application of catalysts for ultra-deep hydrodesulfurization of diesel[J].Chinese Journal of Catalysis,2013, 34(1):130-139. [7] 黄新露,曾榕辉.催化裂化柴油加工方案的探讨[J].中外能源,2012(7):75-80. [8] TIMOTHY H, VASANT T, EMMANUEL B, et al. Developments in distillate fuel specifications and strategies for meeting them[M].National Petroleum Refiners Association, San Francisco,California,1998. [9] 周宇红,黄庆梅.二十一世纪柴油质量及其相关技术的发展趋势[J].化学工程师,2006(2):19-22. [10] 王福江,张毓莹,龙湘云,等.催化裂化柴油馏分加氢精制提高十六烷值研究[J].石油炼制与化工,2013, 44(10):27-31. [11] 兰玲,贝耀明,方向晨.新一代催化裂化柴油加氢改质催化剂的工艺条件及工业应用[J].石油炼制与化工,2003, 34(8):36-39. [12] 杜艳泽,黄新露,石友良,等.中国石化加氢装置生产技术交流会论文集[C].北京:中国石化出版社,2012:27-37. [13] 黄新露.重芳烃高效转化生产轻芳烃技术[J].化工进展,2013,32(9):2263-2266. [14] 张毓莹,胡志海,辛靖,等.MHUG技术生产满足欧V排放标准柴油的研究[J].石油炼制与化工,2009, 40(6):1-7. [15] 刘继华,关明华,郇维方,等.柴油深度加氢脱硫脱芳烃工艺技术的研究与开发[J].炼油技术与工程,2003(10):1-4. [16] GAO X D, NIE H, SHI Y L, et al.SSHT process-a low cost solution for low sulfur and low aromatics diesel[J].China Petroleum Processing and Petrochemical Technology,2003(2):43-46. [17] 白宏德,薛稳曹,蒋东红,等.提高柴油十六烷值RICH工艺技术的工业应用[J].石油炼制与化工,2001, 32(9):28-30. [18] 王欣.RICH技术在柴油加氢装置上的应用[J].石化技术与应用,2006(4):282-284. [19] 韩崇仁,方向晨,赵玉琢,等.催化裂化柴油一段加氢改质的新技术-MCI[J].石油炼制与化工,1999, 30(9):1-4. [20] 张全信,刘希尧.多环芳烃的加氢裂化[J].工业催化,2001, 9(2):10-17. [21] ARRIBAS M A, COMA A, DIAZ-CABANAS M J, et al. Hydrogenation and ring opening of Tetralin over bifunctional catalysts based on the new ITQ-21 zeolite[J]. Applied Catalysis A:General,2004, 273(1):277-286. [22] 鞠雪艳,张毓莹,胡志海,等.NiMo加氢催化剂上1-甲基萘的饱和反应规律[J].石油学报(石油加工),2012, 28(4):538-544. [23] ITO K, KOGASAKA Y, KUROKAWA H, et al. Preliminary study on mechanism of naphthalene hydrogenation to form decalins via tetralin over Pt/TiO2[J]. Fuel Processing Technology,2002, 79:77-80. [24] 包洪洲,方向晨,刘继华,等.柴油加氢脱芳烃动力学模型研究进展[J].化工进展,2011, 30(5):948-954. [25] 沈凯,翟富民,宗志敏,等.催化剂和芳烃及硫对1-甲基萘以及二(1-萘)甲烷反应的影响[J].煤炭转化,1998, 21(3):88-91. [26] MONTEIRO-GEZORK A C A, NATIVIDAD R, WINTERBOTTOM J M.Hydrogenation of naphthalene on NiMo catalysts:Langmuir-Hinshelwood kinetic modelling[J].Catalysis Today,2008, 130:471-485. [27] DEMIREL B, WISER W H.High conversion (98%) for the hydrogenation of 1-methylnaphthalene to methyldecalins[J]. Fuel Processing Technology,1997, 53:157-169. [28] 黄新露,石培华,于淼.适应用户需求的催化柴油加氢改质技术[J].当代化工,2011(7):702-705. [29] 张毓莹,胡志海,辛靖,等.MHUG技术生产满足欧Ⅴ排放标准柴油的研究[J].石油炼制与化工,2009(6):1-7. [30] 张毓莹,蒋东红,辛靖,等.中国石化炼油加氢技术交流会论文集[C].北京:中国石化出版社,2014:204-212 [31] THAKKAR V P, ABDO S F, GEMBICKI V A, et al.LCO upgrading:a novel approach for greater added value and improved returns[C]//Des Plaines, Illinois, USA:NPRA Annual Meeting, 2005. [32] PAPPAL D A, LEE C, GOEBEL K W, et al.MAK-LCO:MAK Light Cycle Oil Upgrading to Premium Products[C]//National Petroleum Resincrs Association,San Francisco,California,1995. [33] 李永存.MAK-LCO工艺[J].石油炼制与化工,1995, 26:68. [34] JOHNSON J A, FREY S J, THAKKAR V P.Unlocking high value xylenes from light cycle[C].National Petroleum Resincrs Association,San Antonio, TX, 2007. |