[1] |
KUNⅡ D,LEVENSPIEL O.Fluidization Engineering[M].Amsterdam:Elsevier,2013.
|
[2] |
GRACE J R,KNOWLTON T M,AVIDANA A A.Circulating Fluidized Beds[M].Berlin:Springer Science&Business Media,2012.
|
[3] |
郭慕孙,李洪钟.流态化手册[M].北京:化学工业出版社,2008.KWAUK M,LI H Z.Handbook of Fluidization[M].Beijing:Chemical Industry Press,2008.
|
[4] |
陈俊武.催化裂化工艺与工程[M].北京:中国石化出版社,2005.CHEN J W.Fluidized Catalytic Cracking Process and Engineering[M].Beijing:China Petrochemical Press,2005.
|
[5] |
BENYAHIA S,ARASTOOPOUR H,KNOWLTON T M,et al.Simulation of particles and gas flow behavior in the riser section of a circulating fluidized bed using the kinetic theory approach for the particulate phase[J].Powder Technol.,2000,112(1):24-33.
|
[6] |
ZHANG N,LU B,WANG W,et al.3D CFD simulation of hydrodynamics of a 150 MWe circulating fluidized bed boiler[J].Chem.Eng.J.,2010,162:821-828.
|
[7] |
JIRADIALOK V,GIDASPOW D,DAMRONGLERD S,et al.Kinetic theory based CFD simulation of turbulent fluidization of FCC particles in a riser[J].Chem.Eng.Sci.,2006,61(17):5544-5559.
|
[8] |
杨朝合,杜玉朋,赵辉.催化裂化提升管反应器流动反应耦合模型研究进展[J].化工进展,2015,34(3):608-616.YANG C H,DU Y P,ZHAO H.Evolvement of flow-reaction models for fluid catalytic cracking riser reactors[J].Chemical Industry and Engineering Progress,2015,34(3):608-616.
|
[9] |
DU Y,ZHAO H,MA A,et al.Equivalent reactor network model for the modeling of fluid catalytic cracking riser reactor[J].Ind.Eng.Chem.Res.,2015,54(35):8732-8742.
|
[10] |
ANDREUX R,PETIT G,HEMATI M,et al.Hydrodynamic and solid residence time distribution in a circulating fluidized bed:experimental and 3D computational study[J].Chem.Eng.Process.,2008,47(3):463-473.
|
[11] |
HUA L,WANG J,LI J.CFD simulation of solids residence time distribution in a CFB riser[J].Chem.Eng.Sci.,2014,117:264-282.
|
[12] |
YANG N,WANG W,GE W,et al.CFD simulation of concurrent-up gas-solid flow in circulating fluidized beds with structure-dependent drag coefficient[J].Chem.Eng.Sci.,2003,96(1):71-80.
|
[13] |
WANG W,LI J.Simulation of gas-solid two-phase flow by a multi-scale CFD approach-of the EMMS model to the sub-grid level[J].Chem.Eng.Sci.,2007,62(1):208-231.
|
[14] |
KIM S W,KIRBAS G,BI H,et al.Flow structure and thickness of annular downflow layer in a circulating fluidized bed riser[J].Powder Technol.,2012,380(1):48-58.
|
[15] |
ZHANG W,JOHNSSON F,LECKNER B,et al.Fluid dynamic boundary layers in CFB boilers[J].Chem.Eng.Sci.,1995,50:201-210.
|
[16] |
BEZZO F,MACCHIETTO S,PANTELIDES C C.Computational issues in hybrid multizonal/computational fluid dynamics models[J].AIChE J.,2005,51(4):1169-1177.
|
[17] |
LI C,DAI Z,SUN Z,et al.Modeling of an opposed multiburner gasifier with a reduced-order model[J].Ind.Eng.Chem.Res.,2013,52:5825-5834.
|
[18] |
LE MOULLEC Y,GENTRIC C,POTIER O,et al.Comparison of systemic,compartmental and CFD modelling approaches:application to the simulation of a biological reactor of wastewater treatment[J].Chem.Eng.Sci.,2010,65(1):343-350.
|
[19] |
DU Y,YANG Q,BERROUK A S,et al.Equivalent reactor network model for simulating the air gasification of polyethylene in a conical spouted bed gasifier[J].Energy&Fuels,2014,28(11):6830-6840.
|
[20] |
BI H T,GRACE J R.Flow regime diagrams for gas-solid fluidization and upward transport[J].Int.J.Multiphas.Flow,1995,21(6):1229-1236.
|
[21] |
RHODES M J,SOLLAART M,WANG X S.Flow structure in a fast fluid bed[J].Powder Technol.,1998,99(2):194-200.
|
[22] |
戎顺熙,范良政.连续流动系统停留时间分布的随机模型和模拟[J].化工学报,1986,37(3):259-268.RONG S X,FAN L Z.Stochastic modeling and simulation of the residence time distribution for continuous flow systems[J].Journal of Chemical Industry and Engineering (China),1986,37(3):259-268.
|