共 35 条
[1]
A narrow size distribution on a high shear mixer by applying a flux number approach. Boerefijn R,Juvin P Y,Garzon P. Powder Technology . 2009
[2]
Wet granulation in laboratory-scale high shear mixers:Effect of chopper presence,design and impeller speed. T.M.Chitu,D.Oulahna,M.Hemati. Powder Technology . 2011
[3]
Expression for turbulent power draw of an in-line Silverson high shear mixer. Kowalski A J,Cooke M,Hall S. Chemical Engineering Science . 2011
[4]
Flow pattern,periodicity and energy dissipation in a batch rotor-stator mixer. Adi T Utomo,Michael Baker,Andrzej W Pacek. Chemical Engineering . 2008
[5]
Modelling of the turbulent wall jetgenerated by a pitched blade turbine impeller:the effect of turbulencemodel. Jaworski Z,Zakrzewska B. Chemical Engineering Research and Design . 2002
[6]
An expression for the power consumption of in-line rotor-stator devices. Adam J Kowalski. Chemical Engineering and Processing:Process Intensification . 2009
[7]
Modelling and experimental validation of emulsification processes in continuous rotor-stator units. Cristhian Almeida-Rivera,Peter Bongers. Computers and Chemistry . 2010
[8]
Modelling of the Turbulent Wall Jet Generated by a Pitched Blade Turbine Impeller[J] . Z. Jaworski,B. Zakrzewska.  Chemical Engineering Research and Design . 2002 (8)
[9]
Numerical Simulation of Turbulent Flow Characteristics in a Stirred Vessel Using the LES and RANS Approaches with the Sliding/Deforming Mesh Methodology[J] . S.L. Yeoh,G. Papadakis,M. Yianneskis.  Chemical Engineering Research and Design . 2004 (7)
[10]
Numerical analysis of similarities of particle behavior in high shear mixer granulators with different vessel sizes. Hideya Nakamura,Yoshikazu Miyazaki,Yoshinobu Sato,et al. Advanced Powder Technology . 2009