McDougall S,Saberian M,Briens C. Using dynamic pressure signals to assess the effects of injected liquid on fluidized bed properties[J]. Chemical Engineering and Processing,2005,44(7):701-708.
[6]
Jennifer M,Cedric B,Franco B. Flow stability in a downer mixing chamber[J]. Chemical Engineering and Processing,2006,45:798-805.
[7]
Maryam M,Majid H,Cedric B. The effects of liquid properties and bed hydrodynamics on the distribution of liquid on solid fiuidized particles in a cold-model fluidized bed[J]. Powder Technology,2014,256:5-12.
[8]
Stefan H,Jan Bn,Markus H. Study of dynamic multi-dimensional temperature and concentration distribution in liquid-sprayed fluidized beds[J]. Chemical Engineering Science,2003,58(23-24):5135-5160.
[9]
Flora P,Cedric B,Franco B. Effect of particle size,liquid content and location on the stability of agglomerates in a fluidized bed[J]. Powder Technology,2013,237:376-385.
[10]
Mills P J T,Seville J P K,Knight P C K. The effect of binder viscosity on particle agglomeration in a low shear mixer/agglomerator[J]. Powder Technology,2000,113(1-2):140-147.
[11]
Saad M M,Barkouti A,Rondet E. Study of agglomeration mechanisms of food powders:Application to durum wheat semolina[J]. Powder Technology,2011,208(2):399-408.
[12]
Ishmael Q,Ataollah N,William S,et al. Addai-Mensah. Single and mixed oxide and clay particle agglomeration:Influence of feed mineralogy and percent drum volume loading[J]. Powder Technology,2014,253(2):568-579.
[13]
Thomas A,Anette S,Torben S. The effect of droplet size and powder particle size on the mechanisms of nucleation and growth in the fluid bed melt agglomeration[J]. International Journal of Pharmaceutics,2002,249(1-2):185-197.
[14]
Sara W,Cedric B,Franco B,Edward C,et al. Effect of agglomerate properties on agglomerate stability in fluidized bed[J]. Chemical Engineering Science,2008,63(17):4245-4256.
[15]
Simon M I,James D L,Karen H,Bryan J E.Nucleation,growth and breakage phenomena in agitated wet granulation processes:A review[J]. Powder Technology,2001,117(1-2):3-39.
[16]
Base T E,Chan E W,Kennett R D. Nozzle for atomizing liquid in two phase flow:US,6003789[P]. 1999-12-21.
[17]
McDougall S,Saberian M,Briens C. Characterization of fluidization quality in fludized beds of wet particles[J]. Int. J. Chem. React. Eng.,2004(2):1542-6580.
[18]
Rondet E,Ruiz T,Delalonede M,et al. Fractal law:A new tool for modelling agglomeration process[J]. International Journal of Chemical Reactor Engineering,2010,8(1):1-12.
[19]
Vicsek T. Fractal models for diffusion controlled aggregation[J]. Journal of Physics A:Mathematical and General,1983,16(17):647-652.
[20]
Rondet E,Delalonde M,Ruiz T,et al. Fractal formation description of agglomeration in low shear mixer[J]. Chemical Engineering Journal,2010,164(2-3):376-382.