[1]陈永利, 陈浩, 郭振宇.丙烯产业发展现状及趋势分析[J].炼油技术与工程, 2019, 49(12):1-5
[2]杨学萍.国内外丙烯生产技术进展及市场分析[J].石油化工技术与经济, 2017, 33(06):11-15
[3]初春雨, 阎松, 孟秀红, 等.碱处理多级孔-的酸性及吸附扩散性能研究[J].石油炼制与化工, 2016, 47(10):66-71
[4]Xinglong Dong,Sohel Shaikh,Jullian R.Vittenet,etalFine Tuning the Diffusion Length in Hierarchical ZSM-5 to Maximize the Yield of Propylene in Catalytic Cracking of Hydrocarbons)[J].ACS Sustainable Chemistry and Engineering, 2018, 11(6):15832-15840
[5]B R Jermy, M A B. Siddiqui, A M Aitani.Utilization of ZSM-5/MCM-41 composite as FCC catalyst additive for enhancing propylene yield from VGO cracking[J].Journal of Porous Materials, 2012, 19(4):499-509
[6]陈俊武,曹汉昌.催化裂化工艺与工程(第二版)[J].中国石化出版社, 2005, :913-
[7]Ogura M, Shinomiya S Y, Tateno J, etal.Alkali-treatment technique — new method for modification of structural and acid-catalytic properties of ZSM-5 zeolites.[J]. Applied Catalysis A: General, 2001, , 219(1–2):33-43
[8]Kortunov P, Vasenkov S, K?rger J, etal.The role of mesopores in intracrystalline transport in USY zeolite: PFG NMR diffusion study on various length scales[J].Journal of the American Chemical Society, 2005, 127(37):13055-13059
[9]Yanfeng Zhang, Adolfo M.Avila,Begum Tokay,etalBlocking defects in SAPO-34 membranes with cyclodextrin[J].Journal of Membrane Science, 2010, 358(1):7-12
[10]Bazyari, A.A. Khodadadi,NHosseinpour,etal. Effects of steaming-made changes in physicochemical properties of Y-zeolite on cracking of bulky 1,3,5-triisopropylbenzene and coke formation[J].Fuel Processing Technology, 2009, 90(10):1226-1233
[11]袁起民, 龙军, 谢朝钢.重油催化裂解过程中丙烯和干气的生成历程[J].石油学报石油加工, 2014, 30(01):1-6
[12]den HOLLANDER M A, WISSINK M, MAKKEE M, etal.Gasoline conversion: Reactivity towards cracking with equilibrated FCC and ZSM-5 catalysts[ J][J].Appl Catal A, 2002, 223(1-2):85-102
[13]J.S. Buchanan,D[J].H. Olson, S.E. Schramm . Gasoline selective ZSM-5 FCC additives: Effects of crystal size, SiO2 Al2O3, steaming, and other treatments on ZSM-5 diffusivity and selectivity in cracking of hexane octane feed[ J] . Appl Catal A, 2001, 220(1-2):223-234
[14]Knight J, Mehlberg R.Maximize propylene from your FCC unit[J].Hydrocarbon Processing, 2011, :91-95
[15]J.S. Buchanan.The chemistry of olefins production by ZSM-5 addition to catalytic cracking units [J].Catalysis Today, 2000, 55(3):207-212
[16]A I Hussain, A M Aitani, Martin Kub?,et al.Catalytic cracking of Arabian light VGO over novel zeolites as FCC catalyst additives for maximizing propylene yield. [J].Fuel, 2016, 167:226-239
[17]A A Lappas, C S Triantafillidis, Z A Tsagrasouli, et al.Development of new ZSM-5 catalyst-additives in the fluid catalytic cracking process for the maximization of gaseous alkenes yield[J].Studies in Surface science & Catalysis,:, 2002, 142:807-814
[18]李晓红, 钟思青, 周兴贵, 等.催化裂化制乙烯、丙烯催化剂的研究进展[J].化工进展, 2008, 27(09):1316-1327
[19]王为然, 张文斌, 王刚, 等.汽油二次裂化增产丙烯过程中主要影响因素的研究[J].燃料化学学报, 2009, 37(01):65-70 |