[1] 戴厚良主编.芳烃技术[M].北京:中国石化出版社,2014.DAI Houliang.Aromatic technologies[M].Beijing:China Petrochemical Press,2014.
[2] 骆红静,赵睿.中国对二甲苯市场2015年回顾与展望[J].当代石油化工,2016,24(5):17-25.LUO Hongjing,ZHAO Rui.A review of China's PX market in 2015 and a prospect for future[J].Petroleum & Prteochemical Today,2016,24(5):17-25.
[3] MA Shuqi,GUO Xiaoguang,ZHAO Lingxiao,et al.Recent progress in methane dehydroaromatization:from laboratory curiosities to promising technology[J].Journal of Energy Chemistry,2013,22(1):1-20.
[4] GUO Xiaoguang,FANG Guangzong,LI Gang,et al.Direct nonoxidative conversion of methane to ethylene,aromatics,and hydrogen[J].Science,2014,344(6184):616-619.
[5] LIN Zhaojia,NIKOLAKIS Vladimiros,IERAPETRITOU Marianthi.Life cycle assessment of biobased p-xylene production[J].Industrial & Engineering Chemistry Research,2015,54(8):2366-2378.
[6] 葛泮珠.催化裂化柴油综合利用技术及其发展[J].化工进展,2016,35(s1):79-86.GE Panzhu.Comprehensive utilization technologies of LCO and developments[J].Chemical Industry and Engineering Process,2016,35(s1):79-86.
[7] 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.HUANG Xinlu.Technology for producing light aromatics from heavy aromatics[J].Chemical Industry and Engineering Process,2013,32(9):2263-2266.
[8] 龚剑洪,毛安国,刘晓欣,等.催化裂化轻循环油加氢-催化裂化组合生产高辛烷值汽油或轻质芳烃(LTAG)技术[J].石油炼制与化工,2016,47(9):1-5.GONG Jianhong,MAO Anguo,LIU Xiaoxin,et al.LTAG technology for producing high octane number gasoline and light aromatics[J].Petroleum Processing and Petrochemicals,2016,47(9):1-5.
[9] 张洪涛,黄明凯.重整C10重芳烃的综合利用[J].当代化工,2001,20(3):145-148.ZHANG Hongtao,HUANG Mingkai.Coprehensive utilization of heavy aromatics C10 in reformer unit[J].Contemporary Chemical Industry,2001,20(3):145-148.
[10] 韩崇仁主编.加氢裂化工艺与工程[M].北京:中国石化出版社,2006.HAN Chongren.Hydrocracking technology and engineering[M].Beijing:China Petrochemical Press,2006.
[11] 唐卫东.连续重整重芳烃综合利用工艺的探讨[J].石油炼制与化工,2006,37(11):35-39.TANG Weidong.Perspectives on comprehensive utilization of heavy aromatics from CCR unit[J].Petroleum Processing and Petrochemicals,2006,37(11):35-39.
[12] 孔德金,祁晓岚,朱志荣,等.重芳烃轻质化技术进展[J].化工进展,2006,25(9):983-987.KONG Dejin,QI Xiaolan,ZHU Zhirong,et al.Technological advances in conversion of heavy aromatics to light aromatics[J].Chemical Industry and Engineering Progress,2006,25(9):983-987.
[13] LEVIN Doron,ROSS April D,BEECH Jr James H.Transalkylation of heavy aromatic hydrocarbon feed stocks:US8481443B2[P].2013-07-09.
[14] 范景新,臧甲忠,于海斌,等.重芳烃轻质化研究进展[J].工业催化,2015,23(9):666-673.FAN Jingxin,ZANG Jiazhong,YU Haibin,et al.Research progress in conversion of heavy aromatics to light ones[J].Industrial Catalysis,2015,23(9):666-673.
[15] AL-KHATTAF Sulaiman,ALI Syed,AITANI Abdullah M,et al.Catalysis of metal supported zeolites for dealkylation-transalkylation of alkyl-aromatics[J].Applied Catalysis A:General,2016,514:154-163.
[16] 刘建锟,蒋立敬,杨涛,等.乙烯焦油加工利用进展[J].化工进展,2012,31(1):402-405.LIU Jiankun,JIANG Lijing,YANG Tao,et al.Ethylene tar processing and utilization progress[J].Chemical Industry and Engineering Progress,2012,31(1):402-405.
[17] 杨靖华,许修强,曹祖宾.乙烯装置副产C9馏分制备芳烃溶剂油及石油树脂[J].石油炼制与化工,2008,39(2):26-30.YANG Jinghua,XU Xiuqiang,CAO Zubin.Preparation of aromatic solvent naphtha and petroleum and petroleum resin by C9 fraction from ethylene unit[J].Petroleum Processing and Petrochemicals,2008,39(2):26-30.
[18] 许友好,张久顺,马建国,等.MIP工艺反应过程中裂化反应的可控性[J].石油学报(石油加工),2004,20(3):1-6.XU Youhao,ZHANG Jiushun,MA Jianguo,et al.Controllability of cracking reaction in MIP process[J].Acta Petrolei Sinica (Petroleum Processing Section),2004,20(3):1-6.
[19] 周佩玲.深度催化裂解(DCC)技术[J].石油化工,1997,26(8):540-544.ZHOU Peiling.Deep catalytic cracking (DCC) technology[J].Petrochemical Technology,1997,26(8):540-544.
[20] 赵焘,曾榕辉,孙洪江,等.劣质柴油加氢改质工艺研究[J].当代化工,2013,42(4):382-385.ZHAO Tao,ZENG Ronghui,SUN Hongjiang,et al.Study on the hydro-upgrading process for poor diesel oil[J].Contemporary Chemical Industry,2013,42(4):382-385.
[21] 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.HAN Chongren,FANG Xiangchen,ZHAO Yuzhuo,et al.MCI——a new hydrotreating technology for upgrading LCO[J].Petroleum Processing and Petrochemicals,1999,30(9):1-4.
[22] 尹恩杰,方向晨,廖士纲.劣质柴油生产清洁柴油技术的比较[J].炼油设计,2000,30(4):16-20.YIN Enjie,FANG Xiangchen,LIAO Shigang.Comparison of technologies for clean diesel production from inferior gas oil[J].Petroleum Refinery Engineering,2000,30(4):16-20.
[23] 佟瑞利.煤基液体产物的组成分析与芳烃组分催化加氢研究[D].北京:中国矿业大学(北京),2016.TONG Ruili.Composition analysis of coal based liquid and its aromatics catalytic hydrogenation[D].Beijing:China University of Mining and Technology(Beijing),2016.
[24] 陈俊武.催化裂化工艺与工程[M].北京:中国石化出版社,2005.CHEN Junwu.Catalytic cracking engineering and technology[M].Beijing:China Petrochemical Press,2005.
[25] 马怀军,田志坚,杨晓梅,等.四氢萘的加氢与选择性开环[J].分子催化,2006,20(5):449-451.MA Huaijun,TIAN Zhijian,YANG Xiaomei,et al.Hydrogenation and selective ring-opening of tetralin[J].Journal of Molecular Catalysis,2006,20(5):449-451.
[26] 鞠雪艳,蒋东红,胡志海,等.四氢萘类化合物与萘类化合物混合加氢裂化反应规律的考察[J].石油炼制与化工,2012,43(11):1-5.JU Xueyan,JIANG Donghong,HU Zhihai,et al.Study on the hydrocracking reaction rule of feed containing tetralins and naphthalenes mixture[J].Petroleum Processing and Petrochemicals,2012,43(11):1-5.
[27] 任杰,唐之勤,郭友娣,等.重整重芳烃选择加氢Ni-M/Al2O3催化剂性能[J].化学反应工程与工艺,2016,32(3):211-216.REN Jie,TANG Zhiqin,GUO Youdi,et al.Ni-M/Al2O3 catalyst performance for selective hydrogenation of heavy reforming aromatics[J].Chemical Reaction Engineering and Technology,2016,32(3):211-216.
[28] 张小菲,邵正锋,毛国强,等.萘在贵金属Pd、Pt及Pd-Pt催化剂上的加氢活性及耐硫性能[J].物理化学学报,2010,26(10):2691-2698.ZHANG Xiaofei,SHAO Zhengfeng,MAO Guoqiang,et al.Naphthalene hydrogenation activity over Pd,Pt and Pd-Pt catalysts and their sulfur tolerance[J].Acta Physico-Chimica Sinica,2010,26(10):2691-2698.
[29] 李大东.加氢处理工艺与工程[M].北京:中国石化出版社,2004.LI Dadong.Hydrotreating technology and process[M].Beijing:China Petrochemical Press,2004.
[30] 郑仁垟,辛靖,张润强,等.加氢精制深度对催化裂化柴油性质的影响[J].石油炼制与化工,2014,45(10):1-7.ZHENG Renyang,XIN Jing,ZHANG Runqiang,et al.Influence of hydrotreating depth on properties of LCO[J].Petroleum Processing and Petrochemicals,2014,45(10):1-7.
[31] 王洪星,李学,曹志涛,等.乙烯焦油生产汽油调和组分油的工艺研究[J].中外能源,2015,20(8):76-79.WANG Hongxing,LI Xue,CAO Zhitao,et al.A study into using ethylene tar to make gasoline blending component[J].Sino-Global Energy,2015,20(8):76-79.
[32] 李大东.炼油工业:市场的变化与技术对策[J].石油学报(石油加工),2015,31(2):208-217.LI Dadong.Petroleum industry:market changes and technical strategy[J].Acta Petrolei Sinica (Petroleum Processing Section),2015,31(2):208-217.
[33] PENG Chong,HUANG Xinlu,DUAN Xuezhi,et al.Direct production of high octane gasoline and ULSD blend stocks by LCO hydrocracking[J].Catalysis Today,2016,271:149-153.
[34] FREY Stanley J,TOWLER Gavin.Multi-zone process for the production of xylene compounds:US20080161622[P].2008-07-03.
[35] FREY Stanley J,ABDO Suheil F,NEGIZ Antoine,et al.Process for xylene production:WO2009008876[P].2009-01-15.
[36] Honeywell,UOP.UOP LCO-X Process[EB/OL].https://www.Uop.com/lcox/.
[37] 龚剑洪,龙军,毛安国,等.LCO加氢-催化组合生产高辛烷值汽油或轻质芳烃技术(LTAG)的开发[J].石油学报(石油加工),2016,32(5):867-874.GONG Jianhong,LONG Jun,MAO Anguo,et al.Development of the LTAG technology for LCO to produce higher RON naphtha and light aromatics[J].Acta Petrolei Sinica (Petroleum Processing Section),2016,32(5):867-874.
[38] 金洪赞,金圣原,金容升,等.由含有芳族化合物的油馏分制备高附加值芳族产品和烯烃产品的方法:103328416A[P].2013-09-25.KIM Hongchan,KIM Sungwon,KIM Yongseung,et al.Method for producing high-added-value aromatic products and olefinic products from an aromatic-compound-containing oil fraction:103328416A[P].2013-09-25.
[39] 柳川真一朗,伊田领二,小林正英.芳香族烃的制造方法:103097496A[P].2013-05-08.YANAGAWA Shinichiro,IDA Ryoji,KOBAYASHI Masahide.Aromatic hydrocarbon production process:103097496A[P].2013-05-08.
[40] SIMANZHENKOV Vasily,OBALLA Michael C,KIM Grace.Technology for producing petrochemical feedstock from heavy aromatic oil fractions[J].Industrial & Engineering Chemistry Research,2010,49(3):953-963.
[41] OBALLA Michael C,SIMANZHENKOV Vasily,WEITKAMP Jens,et al.Aromatic saturation and ring opening process:US20070062848A1[P].2007-03-22.
[42] KATO Hajime,TANAKA Itoshi,IWAYAMA Kazuyoshi,et al.Catalyst composition for transalkylation of alkylaromatic hydrocarbons and process for production of xylene:US6060417[P].2000-05-09.
[43] 臧甲忠,张国辉,于海斌,等.一种C10+重芳烃加氢轻质化方法:104357083[P].2015-02-18.ZANG Jiazhong,ZHANG Guohui,YU Haibin,et al.A method for
hydrogenation of C10+ heavy aromatics to light aromatics:104357083[P].2015-02-18.
[44] 郑均林,钱斌,祁晓岚,等.从催化柴油直接生产BTX 芳烃技术的研究[J].石油化工,2014,43(s1):124-125.ZHENG Junlin,QIAN Bin,QI Xiaolan,et al.Study on direct
production of BTX aromatics from catalytic diesel oil[J].Petrochemical Technology,2014,43(s1):124-125.
[45] 郑均林,孔德金,李旭光,等.由劣质重芳烃直接生产苯和二甲苯的方法:105085135B[P].2015-11-25.ZHENG Junlin,KONG Dejin,LI Xuguang,et al.Method for producebenzene and xylene directly from low heavy aromatics:105085135B[P].2015-11-25.
[46] 孔德金,郑均林,李旭光,等.由含有稠环烃的混合物制取芳烃的方法:103121897B[P].2013-05-29.KONG Dejin,ZHENG Junlin,LI Xuguang,et al.Method forpreparing aromatics from polycyclic aromatics containing mixture:103121897B[P].2013-05-29.
[47] 孔德金,钱斌,郑均林.轻质循环油选择性加氢脱硫方法:103122258B[P].2013-05-29.KONG Dejin,QIAN Bin,ZHENG Junlin.Selective hydrogenation desulfurization method for LCO:103122258B[P].2013-05-29.
[48] 郑均林,李旭光,孔德金,等.稠环芳烃制取单环芳烃方法:103121895B[P].2013-05-29.ZHENG Junlin,LI Xuguang,KONG Dejin,et al.Method for preparing single ring aromatics from polycyclic aromatics:
103121895B[P].2013-05-29. |