Critical impeller speed for suspending solids in aerated agitation tanks

Systematic measurements have been carried out in agitated gas-liquid-solids systems to determine the just off-bottom suspension speed. A variety of solids sizes, solids concentrations, impeller sizes and tank sizes are used. The difference between the just off-bottom suspension speeds with and without gas sparging does not show a linear relationship with the gassing rate and the relation is system-dependent. The relative just off-bottom suspension speed RJSS = Njsg/Njs is found to be dependent only on the just suspension aeration number Najs = Qg/NjsD 3 and, for DT6 impellers, the relation is RJSS = 1 + mNa n js with the values of 2.6 and 0.7 for m and n, respectively. The relation is independent of the impeller size, solids size, solids loading and tank size, and can be used to scale up laboratory data to full-scale mixing vessels. Data from different studies support the present findings.

[1]  Yonggang Zhu,et al.  Solids suspension with axial‐flow impellers , 2000 .

[2]  Vishwas G. Pangarkar,et al.  Critical impeller speed for solid suspension in multi‐impeller three phase agitated contactors , 1995 .

[3]  A. Nienow,et al.  Chapter 16 – The suspension of solid particles , 1992 .

[4]  Thanapalan Murugesan,et al.  Critical Impeller Speed for Solid Suspension in Mechanically Agitated Contactors , 2001 .

[5]  C. W. Wong,et al.  Investigations of fluid dynamics in mechanically stirred aerated slurry reactors , 1987 .

[6]  A. W. Nienow,et al.  Particle-gas-liquid mixing in stirred vessels. I: Particle-liquid mixing , 1983 .

[7]  J. Joshi,et al.  Critical impeller speed for solid suspension in mechanically agitated three-phase reactors. 1. Experimental part , 1991 .

[8]  Th.N. Zwietering Suspending of solid particles in liquid by agitators , 1958 .

[9]  Alvin W. Nienow,et al.  Studies on three-phase mixing: a review and recent results , 1986 .

[10]  Kevin J. Myers,et al.  Solids suspension with up‐pumping pitched‐blade and high‐efficiency impellers , 1998 .

[11]  Yonggang Zhu,et al.  The effect of impeller pumping and fluid rheology on solids suspension in a stirred vessel , 2001 .

[12]  Michael T. Hicks,et al.  CLOUD HEIGHT IN SOLIDS SUSPENSION AGITATION , 1997 .

[13]  Alvin W. Nienow,et al.  Particle suspension in the turbulent regime: The effect of impeller type and impeller/vessel configuration , 1996 .

[14]  C. Buurman,et al.  Scaling-up rules for solids suspension in stirred vessels , 1986 .

[15]  A. Bakker,et al.  Suspension of solid particles with gassed impellers , 1990 .

[16]  Kevin J. Myers,et al.  Agitator design for solids suspension under gassed conditions , 1999 .