[1]汪萍,唐玮,杨帆,等.中国石油储量现状及变化特点[J].特种油气藏, 2011, 18(1):12-17 [2]陈俊武,卢捍卫.催化裂化在炼油厂中的地位和作用展望———催化裂化仍将发挥主要作用[J].石油学报石油加工, 2003, 19(1):1-11 [3]Brunet S, Mey D, Perot G., et al. On the hydrodesulfurization of FCC gasoline: A review[J].Applied Catalysis A, 2005, 278(2):143-172 [4]龚剑洪,陆善祥,崔建,等.国产重油组成的表征[J].石油炼制与化工, 2000, 31(10):48-54 [5]李凤琪,全瀛寰,朱凌辉,等.哈油汽油硫及烯烃含量分布特征研究[J].炼油技术与工程, 2015, 45(7):18-20 [6]杨晓宇,王永长,龙化云,等.流化催化裂化汽油改质前后组分变化分析[J].中外能源, 2013, 18(7):76-82 [7]朱萌萌,郑兰歌,宋丽娟,等.芳烃在催化剂上的吸附扩散行为[J].石油化工高等学校学报, 2015, 28(3):7-11 [8]刘俊.烯烃与环烷烃在催化裂化中反应的异同点[J].工业催化, 2017, 25(4):56-62 [9]李荻,藤秋霞,高雄厚,等.镧和铈在型分子筛方钠石笼中的定位差异以及对催化剂反应性能的影响[J].工业催化, 2013, 21(2):51-54 [10]方玉堂,李大艳,高学农,等.稀土改性分子筛的表征与性能[J].化工学报, 2011, 62(6):1581-1586 [11]Zheng HM, Zhaom L, Yang Q, et al.Insight into the adsorption mechanism of benzene in HY zeolites: The effect of loading[J].RSC Advances, 2016, 6(41):34175-34187 [12]Seyforth J, A literature review of the computational methods used to investigate molecular machines [Z].ResearchGate, J. Seyforth, 2016. [13]Hou TJ, Zhu LL, Xu XJ.Adsorption and diffusion of benzene in ITQ-1 type zeolite: Grand canonical monte carlo and molecular dynamics simulation study[J].Journal of Physics Chemical B, 2000, 104(39):9356-9364 [14]Dann SE, Mead PJ, Mark T, et al.Lowenstein’s rule extended to an Aluminum rich frameworkThe structure of bicchulite,Ca8(Al2SiO6)4(OH)8,by masnmr and neutron diffraction[J].Inorganic Chemical, 1996, 35(6):427-1428 [15]Sun H, Ren P, Fried JR.The COMPASS force field: Parameterization and validation for phosphazenes[J].Computational and Theoretical Polymer Science, 1998, 8(2):229-246 [16]Gautham P, Jeppua T, Prabhakar C.A modified Langmuir-Freundlich isotherm model for simulating pH-dependent adsorption effects[J].Journal of Contaminant Hydrology, 2012, 129(130):46-53 |