Riser hydrodynamic study with different Group B powders
暂无分享,去创建一个
[1] John R. Grace,et al. Circulating fluidized beds , 1996 .
[2] John D. Paccione,et al. Modeling and measurement of the effective drag coefficient in decelerating and non-accelerating turbulent gas—solids dilute phase flow of large parti , 1993 .
[3] H. Weinstein,et al. An evaluation of the actual density in the acceleration section of vertical risers , 1989 .
[4] Shozaburo Saito,et al. PNEUMATIC CONVEYING OF SOLIDS THROUGH STRAIGHT PIPES , 1969 .
[5] Mingchuan Zhang,et al. Hydrodynamics of gas-solid flow in the circulating fluidized bed reactor for dry flue gas desulfurization , 2011 .
[6] Jamal Chaouki,et al. Effective drag coefficient investigation in the acceleration zone of an upward gas–solid flow , 2007 .
[7] Jesse Zhu,et al. Effects of particle properties on flow structure in a 2-D circulating fluidized bed: Solids concentration distribution and flow development , 2011 .
[8] Jesse Zhu,et al. Scale-up effect of riser reactors (3) axial and radial solids flux distribution and flow development , 2005 .
[9] Poupak Mehrani,et al. Investigation of electrostatic charge distribution in gas–solid fluidized beds , 2010 .
[10] Franco Berruti,et al. Evaluation of the gas–solid suspension density in CFB risers with exit effects , 2000 .
[11] Jamal Chaouki,et al. Scaling considerations for circulating fluidized bed risers , 1992 .
[12] J. You,et al. Modeling of core flow in a gas–solids riser , 2010 .
[13] Mohammad. M. Hossain,et al. Chemical-looping combustion (CLC) for inherent CO2 separations—a review , 2008 .
[14] Atsushi Tsutsumi,et al. Effects of solids feeder and riser exit configuration on establishing high density circulating fluidized beds , 2008 .
[15] Efstathios E. Michaelides,et al. Drag coefficients of irregularly shaped particles , 2004 .
[16] M. Yazdanpanah,et al. An experimental investigation of loop-seal operation in an interconnected circulating fluidized bed system , 2012 .
[17] Sofiane Benyahia,et al. A time-averaged model for gas–solids flow in a one-dimensional vertical channel , 2008 .
[18] Chi‐Hwa Wang,et al. Electrostatic characteristics in a large-scale triple-bed circulating fluidized bed system for coal gasification , 2012 .
[19] D. Geldart. Types of gas fluidization , 1973 .
[20] Electrostatics in gas–solid fluidized beds for different particle properties , 2012 .
[21] Yong Jin,et al. Investigation on slip velocity distributions in the riser of dilute circulating fluidized bed , 1992 .
[22] C. Hrenya,et al. Cluster characteristics of Geldart group B particles in a pilot-scale CFB riser. II. Polydisperse systems , 2012 .
[23] O. Levenspiel,et al. Drag coefficient and terminal velocity of spherical and nonspherical particles , 1989 .
[24] M. Yazdanpanah. Investigation of a Chemical Looping Combustion (CLC) Configuration with Gas Feed , 2011 .
[25] Jia Wei Chew,et al. Reverse core-annular flow of Geldart Group B particles in risers , 2012 .