[1] S. Wang, B. Shao, R. Liu, J. Zhao, Y. Liu, S. Yang, Comparison of numerical simulations and experiments in conical gas-solid spouted bed, Chin. J. Chem. Eng. 23 (10) (2015) 1579-1586.[2] W. Zhang, A review of techniques for the process intensification of fluidized bed reactors, Chin. J. Chem. Eng. 17 (4) (2009) 688-702.[3] J. Zhang, J. Lu, X.Wang, H. Zhang, G. Yue, T. Suda, J. Sato, Characterization of pressure signals in fluidized beds loaded with large particles using wigner distribution analysis: Feasibility of diagnosis of agglomeration, Chin. J. Chem. Eng. 15 (1) (2007) 24-29.[4] C.Wu, Y. Gao, Y. Cheng, L.Wang, X. Li, Solid concentration and velocity distributions in an annulus turbulent fluidized bed, Chin. J. Chem. Eng. 23 (7) (2015) 1077-1084.[5] Z. Veran, J. Lutcha, Optimizing particle residence time in fluidized bed dryer, Chem. Eng. (1975) 678-681.[6] J. Raghuraman, Y.B.G. Varma, An experimental investigation of the residence time distribution of solids in multistage fluidisation, Chem. Eng. Sci. 30 (1) (1975) 145-150.[7] A.N. Chandran, S.S. Rao, Y.B.G. Varma, Fluidized bed drying of solids, AIChE J. 36 (1) (1990) 29-38.[8] J. Raghuraman, Y.B.G. Varma, A model for residence time distribution in multistage systems with cross-flow between active and dead regions, Chem. Eng. Sci. 28 (2) (1973) 585-591.[9] K. Krisrnaiah, Y. Pydisetty, Y.B.G. Varma, Residence time distribution of solids in multistage fluidisation, Chem. Eng. Sci. 37 (9) (1982) 1371-1377.[10] S.S. Chapadgaokar, Y. Pydi Setty, Residence time distribution of solids in a fluidised bed, Indian J. Chem. Technol. 6 (1999) 100-106.[11] M.P. Babu, Y.P. Setty, Residence time distribution of solids in a fluidized bed, Can. J. Chem. Eng. 81 (1) (2003) 118-123.[12] M.A.T. Cocquerel, Some studies of solids mixing in fluidized beds, Ph. D. Thesis, University of London, England, 1960.[13] P. Bachmann, E. Tsotsas, Analysis of residence time distribution data in horizontal fluidized beds, Procedia Eng. 102 (2015) 790-798.[14] D. Wolf, W. Resnick, Residence time distribution in real systems, Ind. Eng. Chem. Fundam. 2 (4) (1963) 287-293.[15] D.Wolf,W. Resnick, Experimental study of residence time distribution inmultistage fluidized bed, Ind. Eng. Chem. Fundam. 4 (1) (1965) 77-81.[16] D.R. Morris, K.E. Gubbins, S.B. Watkins, Residence time studies in fluidized and moving bedswith continuous solids flow, Trans. Inst. Chem. Eng. 42 (1964) 323-331.[17] J.Chen, H. Li,X. Lv, Q. Zhu, A structure-based dragmodel for the simulationofGeldart A and B particles in turbulent fluidized beds, Powder Technol. 274 (2015) 112-122.[18] H. Li, Important relationship between meso-scale structure and transfer coefficients in fluidized beds, Particuology 8 (6) (2010) 631-633.[19] X. Lv, H. Li, Q. Zhu, Simulation of gas-solid flow in 2D/3D bubbling fluidized beds by combining the two-fluid model with structure-based drag model, Chem. Eng. J. 236 (2014) 149-157.[20] Q. Han, N. Yang, J. Zhu, M. Liu, Onset velocity of circulating fluidization and particle residence time distribution: A CFD-DEM study, Particuology 21 (2015) 187-195.[21] R. Andreux, G. Petit, M. Hemati, O. Simonin, Hydrodynamic and solid residence time distribution in a circulating fluidized bed: Experimental and 3D computational study, Chem. Eng. Process. Process Intensif. 47 (3) (2008) 463-473.[22] Y. Zhang, Z. Wang, Y. Jin, Z. Li, W. Yi, CFD simulation and experiment of residence time distribution in short-contact cyclone reactors, Adv. Powder Technol. 26 (4) (2015) 1134-1142.[23] H. Bai, A. Stephenson, J. Jimenez, D. Jewell, P. Gillis, Modeling flow and residence time distribution in an industrial-scale reactor with a plunging jet inlet and optional agitation, Chem. Eng. Res. Des. 86 (12) (2008) 1462-1476.[24] L. Li, J. Remmelgas, B.G.M. vanWachem, C. von Corswant, M. Johansson, S. Folestad, A. Rasmuson, Residence time distributions of different size particles in the spray zone of a Wurster fluid bed studied using DEM-CFD, Powder Technol. 280 (2015) 124-134.[25] P. Pongsivapai, Residence Time Distribution of Solids in a Multi-compartment Fluidized Bed System, Master Thesis, Oregon State Univ, USA, 1994.[26] O. Levenspiel, Tracer Technology: Modeling the Flow of Fluids, Springer-Verlag, New York, 2012.[27] J.T. Adeosun, A. Lawal, Numerical and experimental studies of mixing characteristics in a T-junction microchannel using residence-time distribution, Chem. Eng. Sci. 64 (10) (2009) 2422-2432.[28] I.L. Gamba, S.M. Damian, D.A. Estenoz, N. Nigro, M.A. Storti, D. Knoeppel, Residence time distribution determination of a continuous stirred tank reactor using computational fluid dynamics and its application on the mathematical modeling of styrene polymerization, Int. J. Chem. React. Eng. 10 (1) (2012) 1-30.[29] N.O. Lemcoff, E.N. Ponzi, M.G. Gonzáles, Comparison between the dispersion and tanks in series models, Chem. Eng. Sci. 35 (8) (1980) 1804-1806.[30] Y. Wang, Z. Zou, H. Li, Q. Zhu, A new drag model for TFM simulation of gas-solid bubbling fluidized beds with Geldart-B particles, Particuology 15 (2014) 151-159.[31] J.A.H. De Jong, Vertical air-controlled particle flow from a bunker through circular orifices, Powder Technol. 3 (1) (1969) 279-286.[32] J.F. Davidson, R. Clift, D. Harrison, Fluidization, second ed. Academic Press, London, 1985.[33] Y. Kato, S. Morooka, A. Nishiwaki, Behavior of dispersed- and continuous-phase in multi-stage fluidized beds for gas-liquid-solid and gas-liquid-liquid systems, Fluidization '85, Science and Technology, Beijing, China, 1985.[34] L. Wei, Y. Lu, J. Wei, Hydrogen production by supercritical water gasification of biomass: Particle and residence time distribution in fluidized bed reactor, Int. J. Hydrog. Energy 38 (29) (2013) 13117-13124. |