Chen Junwu(陈俊武), Lu Hanwei(卢捍卫). Prospects of status and role of FCC in refinery—FCC will continue to play a leading role in petroleum refining industry [J]. Acta Petrolei Sinica: Petroleum Processing Section(石油学报:石油加工), 2003, 19(1): 1-11.
[2]
Cui Shouye(崔守业), Xu Youhao(许友好), Cheng Congli(程从礼), Gong Jianhong(龚剑洪). Commercialization and new developments of MIP technology [J]. Acta Petrolei Sinica: Petroleum Processing Section(石油学报:石油加工), 2010, (suppl.): 23-28.
[3]
Shan Honghong(山红红), Li Chunyi(李春义), Niu Genlin(钮根林), Yang Chaohe(杨朝合), Zhang Jianfang(张建芳). Research progress in fluid catalytic cracking technology [J]. Journal of the University of Petroleum(石油大学学报), 2005, 29(6): 135-150.
[4]
Xu Youhao. Advance in China fluid catalytic cracking (FCC) process [J]. Scientia Sinica Chimica, 2014, 44(1): 13-24.
[5]
Jin Yong(金涌), Yu Zhiqing(俞芷青), Sun Zhufan(孙竹范), Peng Bingpu(彭秉璞). Investigationon branched pipe distributors for fluidized beds (Ⅱ): Deternination of desigh parameters for branched pipe distributors [J]. Journal of Chemical Industry and Engineering (China)(化工学报), 1984, (3): 203-213.
[6]
Wang Zhangmao(王樟茂), Zhang Nianying(张年英), Lü Dewei(吕德伟), Chen Gantang(陈甘棠), Liu Qing(刘青), Jiang Yinrui(江银瑞), Lai Chenlie(赖成烈). Study on characteristics of perforated gas-sidtributors in a commercial fluidized bed [J]. PetroChemical Technoloty(石油化工), 1986, 7: 399-405.
[7]
Wu Chunlian(巫春连), Wei Yaodong(魏耀东), Cai Lianbo(蔡连波), Chen Qiang(陈强). CFD simulation of bubble-type gas distributor's flow field for gas-liquid bubble column [J]. Chemical Engineering &Machinery(化工机械), 2013, 40(30): 340-346.
[8]
Wang Weiwen(王伟文), Xu Kai(许凯), Li Jianlong(李建隆), Li Xingang(李鑫钢). Numerical simulation of the flow field in double cone-diversion gas distributo [J]. Journal of Chemical Engineering of Chinese Universities(高校化学工程学报), 2009, 23(6): 945-950.
[9]
Li Guang, Yang Xiaogang, Dai Gance. CFD simulation of effects of the configuration of gas distributors on gas-liquid flow and mixing in a bubble column [J]. Chemical Engineering Science, 2009, 64: 5104-5116.
[10]
Akbari V, Borhani T N G, Godini H R, Hamid M K A. Model-based analysis of the impact of the distributor on the hydrodynamic performance of industrial polydisperse gas phase fluidized bed polymerization reactors [J]. Powder Technology, 2014, 267: 398-411.
[11]
Bahadori F, Rahimi R. Simulations of gas distributors in the design of shallow bubble column reactors [J]. Chem. Eng. Tech., 2007, 30: 443-447.
[12]
Chen Junwu(陈俊武). Fluid Catalytic Cracking Technology and Engineering (催化裂化工艺与工程)[M]. 2nd ed. Beijing: China PetroChemical Press, 2005
[13]
Li Jinghai(李静海), Ge Wei(葛蔚), Ouyang Jie(欧阳洁), Yang Ning(杨宁), Gao Shiqiu(高士秋), Song Wenli(宋文立). Multi-scale Simulation of Particle-Fluid Complex Systems (颗粒流体复杂系统的多尺度模拟)[M]. Beijing: Science Press, 2005.
[14]
Yang Ning, Wang Wei, Ge Wei, Li Jinghai. Simulation of heterogeneous structure in a circulating fluidized bed riser by combining the two-fluid model with the EMMS approach [J]. Industrial & Engineering Chemistry Research, 2004, 43(18): 5548-5561.
[15]
Yang Ning, Wang Wei, Ge Wei, Li Jinghai. CFD simulation of concurrent-up gas-solid flow in circulating fluidized beds with structure-dependent drag coefficient [J]. Chemical Engineering Journal, 2003, 96: 71-80.
[16]
Xiao Haitao(肖海涛), Qi Haiying(祁海鹰), You Changfu(由长福), Xu Xuchang(徐旭常). The oretical model of drag between gas and solid phase [J]. Journal of Chemical Industry and Engineering (China)(化工学报), 2003, 54(3): 311-315.
[17]
Wang Wei, Li Jinghai. Simulation of gas-solid two-phase flow by a multi-scale CFD approach-of the EMMS model to the sub-grid level [J]. Chemical Engineering Science, 2007, 62: 208-231.
[18]
Wang Junwu, Ge Wei, Li Jinghai. Eulerian simulation of heterogeneous gas-solid flows in CFB risers: EMMS-based sub-grid scale model with a revised cluster description [J]. Chemical Engineering Science, 2008, 63: 1553-1571.
[19]
Lu Bona(鲁波娜), Cheng Congli(程从礼), Lu Weimin(鲁维民), Wang Wei(王维), Xu Youhao(许友好). Numerical simulation of reaction process in MIP riser based on multi-scale model [J]. CIESC Journal(化工学报), 2013, 64(6): 1983-1992.
[20]
Lu Bona, Wang Wei, Li Jinghai, Wang Xianghui, Gao Shiqiu, Lu Weimin, Xu Youhao, Long Jun. Multi-scale CFD simulation of gas-solid flow in MIP reactors with a structure-dependent drag model [J]. Chemical Engineering Science, 2007, 62: 5487-5494.
[21]
Hong Kun, Shi Zhansheng, Ullah Atta, Wang Wei. Extending the bubble-based EMMS model to CFB riser simulations [J]. Powder Technology, 2014, 266: 424-432.
[22]
Shi Zhansheng, Wang Wei, Li Jinghai. A bubble-based EMMS model for gas-solid bubbling fluidization [J]. Chemical Engineering Science, 2011, 66: 5541-5555.
[23]
Liu Yaning, Chen Jianhua, Ge Wei, Wang Junwu, Wang Wei. Acceleration of CFD simulation of gas-solid flow by coupling macro-/meso-scale EMMS model [J]. Powder Technology, 2011, 212: 289-295.
[24]
Liu Xinhua, Hu Shanwei, Jiang Yuefang, Li Jinghai. Extension and application of energy-minimization multi-scale (EMMS) theory for full-loop hydrodynamic modeling of complex gas-solid reactors [J]. Chemical Engineering Journal, 2015, 278: 492-503
[25]
Lu Liqiang, Xu Ji, Ge Wei, Yue Yunpeng, Liu Xinhua, Li Jinghai. EMMS-based discrete particle method (EMMS-DPM) for simulation of gas-solid flows [J]. Chemical Engineering Science, 2014, 120: 67-87.
