Zhang Nan(张楠), Sun Zhongning(孙中宁), Yan Changqi(阎昌琪). Numerical analysis of flow field in three-dimensional randomly packed pebble-bed channel [J]. Atomic Energy Science and Technology(原子能科学技术), 2012, 46(Suppl.): 792-795.
[2]
Tan Lei(谭雷). Mathematical simulation on reactor for methanation of syngas[D].Shanghai: East China University of Science and Technology, 2012.
[3]
Guo Xueyan(郭雪岩). CFD modeling of heat transfer in fixed bed reactors [J]. Journal of Chemical Industry and Engineering (China) (化工学报), 2008, 59(8): 1914-1922.
[4]
Luo Xionglin(罗雄麟), Liu Jianxin(刘建新), Xu Feng(许锋), Zuo Xin(左信). Heterogeneous two-dimensional dynamic modeling and analysis of acetylene hydrogenation reactor [J]. Journal of Chemical Industry and Engineering (China) (化工学报), 2008, 59(6): 1454-1461.
[5]
Ding Shi, Wu Changning, Cheng Yinhong, Jin Yong, Cheng Yi. Analysis of catalytic partial oxidation of methane on rhodium-coated foam monolith using CFD with detailed chemistry [J]. Chemical Engineering Science, 2009, 65(6): 1989-1999.
[6]
Zhai Xuli, Ding Shi, Cheng Yinhong, Jin Yong, Cheng Yi. CFD simulation with detailed chemistry of steam reforming of methane for hydrogen production in an integrated micro-reactor [J]. International Journal of Hydrogen Energy, 2010, 35(11): 5383-5392.
[7]
Hulme I, Clavelle E, vander Lee L, et al. CFD modeling and validation of bubble properties for a bubbling fluidized bed [J]. Ind. Eng. Chem. Res., 2005, 44(12): 4254-4266..
[8]
Beerens M. Chemical Reaction Engineering (化学反应工程)[M]. Zhang Jiyan(张继炎), trans. Beijing: China Petrochemical Press, 1991: 83-120, 429-445.
[9]
Orhan M Tarhan. Catalytic Reactor Design (催化反应器设计)[M].Que Daoyou(阙道悠), trans. Beijing: Hydrocarbon Processing Press, 1989: 81-99.
[10]
Wang Qicheng (王其成), Pei Pei (裴培), Zhang Kai (张锴), et al. Numerical simulation of jetting characteristics in a gas-solid fluidized bed. Journal of Fuel Chemistry and Technology (燃料化学学报), 2007, 35 (3): 354-358.
[11]
Lei Yingjie(雷英杰). Genetic algorithm toolbox and its application by MATLAB(MATLAB 遗传算法工具箱及应用)[M]. Xi'an: Xi'an Electronic and Science University Press, 2005: 95-103.
[12]
Tian Liang(田亮), Jiang Da(蒋达), Qian Feng(钱锋). Simulation and optimization of acetylene converter with decreasing catalyst activity [J]. CIESC Journal (化工学报), 2012, 63(1): 185-192.
[13]
Chen Minheng(陈敏恒). Principles of Chemical Engineering(化工原理)[M]. Beijing: Chemical Industry Press, 1999: 161.
[14]
Zhang Kai(张锴), Brandani S.A model based on two-fluid theory for predicting hydrodynamics behavior in 3D fluidized beds(Ⅰ): Homogeneous or bubbling fluidization of gas-solid system[J].Journal of Chemical Industry and Engineering (China) (化工学报), 2008, 59(5): 1091-1099.
[15]
Hu Baolong(胡宝龙), Hu Guihua(胡贵华), Jiang Da(蒋达), Qian Feng(钱锋). Simulation and optimization of operating parameters of isothermal reaction process for acetylene hydrogenation [J]. CIESC Journal (化工学报), 2015, 66(1): 366-372.
[16]
Long Huilong(龙回龙), Xu Mingjie(许明杰), Yu Donghua(于东华), et al. Two-temperature model of water gas shift reaction in porous media based on FLUENT [J]. Computers and Applied Chemistry(计算机与应用化学), 2012, 29(8): 981-985.
[17]
Liu Wendong (刘文东), Zhang Kai (张锴), Bi Jicheng(毕继诚).CFD simulation on homogeneous or aggregative fluidization of FCC particles [J]. Journal of Petrochemical Universities (石油化工高等学校学报), 2007, 20 (2): 43-46.
[18]
Pamela Berkeley, Van P Carey.Thermodynamic analysis of wall effects on phase stability and homogeneous nucleation in nanochannels containing super heated liquid [J]. Nanoscale and Microscale Thermophysical Engineering, 2013, 17(4): 281-303.
[19]
Franz Román, Vitus Strahl-Sch？fer, Oliver Hensel. Improvement of air distribution in a fixed-bed dryer using computational fluid dynamics [J]. Biosystems Engineering, 2012, 11(24): 359-369.
[20]
Mark F Mathias, Gregory P Muldowney. Effect of solids loading method on bed porosity and gas flux distribution in a fixed-bed reactor [J]. Chemical Engineering Science, 2000, 55(21): 4981-4991.
