[1]Miquel J.Castells FEasy characterization of petroleum fractions[J].Hydrocarbon Processing, 1993, 72(12):101-105
[2]Miquel J.Castells FEasy characterization of petroleum fractions: Part 2. [PBREAK program][J].Hydrocarbon Processing, 1994, 73(1):99-102
[3]侯凯锋, 李有润, 沈静珠等.原油蒸馏装置的在线模拟、修正与优化[J].石油炼制与化工, 1999, 30(10):29-34
[4]李旦杰, 王健红, 方刚.常减压蒸馏过程实时动态模拟[J].北京化工大学学报, 2001, 28(1):81-83
[5]Fu G, Sanchez Y, Mahalec V.Hybrid model for optimization of crude oil distillation units[J].AIChE Journal, 2016, 62(4):1065-1078
[6]Gupta R K, Kumar V, Srivastava V K.A new generic approach for the modeling of fluid catalytic cracking (FCC) riser reactor[J].Chemical Engineering Science, 2007, 62(17):4510-4528
[7]Hernandez-Barajas J R, Vazquez-Roman R, Felix-Flores M G.A comprehensive estimation of kinetic parameters in lumped catalytic cracking reaction models[J].Fuel, 2009, 88(1):169-178
[8]姜浩, 楚纪正, 周璟.基于基准假组分模型的催化裂化反应-再生系统动态模拟[J].石油学报石油加工, 2012, 28(5):806-813
[9]杨冠三, 楚纪正, 吴萍.基于基准假组分催化裂化反应-再生系统的多稳态特性模拟[J].石油化工, 2016, 45(9):1112-1117
[10]曹睿, 王俊, 刘艳升, 蒋荣兴.法计算假组分体系气-液相平衡的数学模型[J].石油炼制与化工, 2009, 40(08):36-40
[11]Bennett D Marshall.A PC-SAFT model for hydrocarbons IV: Water-hydrocarbon phase behavior including petroleum pseudo-components[J].Fluid Phase Equilibria, 2019, 497(10):79-86
[12]Sanchez S, Ancheyta J, McCaffrey WC.Comparison of Probability Distribution Functions for Fitting Distillation Curves of Petroleum[J].Energy & Fuels, 2007, 21(5):2955-2963
[13]邓四清.保单调有理二次插值样条函数[J].郴州师范高等专科学校学报, 2001, 22(5):14-16
[14]Y.A. Liu, Ai-Fu Chang, and Kiran Pashikanti. Petroleum Refinery Process Modeling-Integrated Optimization Tools and Applications[M]. Germany: WileyCH, 2018. |