Effect of blade shape on the performance of six-bladed disk turbine impellers
暂无分享,去创建一个
S. S. Alves | J. Vasconcelos | S. Alves | Jorge M.T. Vasconcelos | Sandra C. P. Orvalho | and Ana M. A. F. Rodrigues | S. Orvalho | And Rodrıgues
[1] K. Riet,et al. The behaviour of gas—liquid mixtures near Rushton turbine blades , 1973 .
[2] K. Riet,et al. Review of Measuring Methods and Results in Nonviscous Gas-Liquid Mass Transfer in Stirred Vessels , 1979 .
[3] Vivek V. Ranade,et al. Fluid mechanics and blending in agitated tanks , 1991 .
[4] Michael Yianneskis,et al. On the structure of the trailing vortices around rushton turbine blades , 1993 .
[5] Alvin W. Nienow,et al. POWER, GAS DISPERSION AND HOMOGENISATION CHARACTERISTICS OF SCABA SRGT AND RUSHTON TURBINE IMPELLERS , 1992 .
[6] S. Nagata,et al. Power Characteristics of Mixing Impellers , 1956 .
[7] Alvin W. Nienow,et al. Scale‐up of mixing in gassed multi‐turbine agitated vessels , 1998 .
[8] H. Kramers,et al. A comparative study on the rate of mixing in stirred tanks , 1953 .
[9] Alberto Brucato,et al. Prediction of flow fields in a dual-impeller stirred vessel , 1999 .
[10] H. Schlichting. Boundary Layer Theory , 1955 .
[11] M. Nocentini,et al. Gas-liquid mass transfer and holdup in vessels stirred with multiple Rushton turbines: water and water-glycerol solutions , 1993 .
[12] Yasuhiro Murakami,et al. Turbulent mixing in baffled stirred tanks with vertical‐blade impellers , 1988 .
[13] S. Kresta,et al. Impact of tank geometry on the maximum turbulence energy dissipation rate for impellers , 1996 .
[14] James Y. Oldshue,et al. Fluid Mixing Technology , 1983 .
[15] Michel Roustan,et al. Bubble size and mass transfer coefficients in dual‐impeller agitated reactors , 1998 .
[16] André Bakker,et al. Gassed power draw of mixed impeller systems , 1997 .
[17] G. B. Tatterson,et al. Form and skin drag contributions to power consumption for the pitched‐blade turbine , 1985 .
[18] Suzanne M. Kresta,et al. Turbulence in stirred tanks: Anisotropic, approximate, and applied , 1998 .
[19] K. Niranjan,et al. An experimental investigation into the effect of impeller design on gas hold-up in a highly viscous Newtonian liquid , 1999 .
[20] J. Joshi,et al. Flow generated by a disc turbine. III: Effect of impeller diameter, impeller location and comparison with other radial flow turbines , 1993 .
[21] M. Gavrilescu,et al. Performance of industrial scale bioreactors with modified RUSHTON turbine agitators , 1996 .
[22] Aniruddha B. Pandit,et al. Effect of agitator design on hydrodynamics and power consumption in mechanically agitated gas-liquid reactors , 1994 .
[23] Jorge M. M. Barata,et al. Mixing in gas-liquid contactors agitated by multiple turbines , 1995 .
[24] Alvin W. Nienow,et al. Gas-liquid mixing studies : A comparison of Rushton turbines with some modern impellers , 1996 .
[25] J. H. Rushton,et al. Gas-Liquid Contacting by Mixers , 1944 .
[26] Jamshid M. Nouri,et al. Scalar mixing measurements in batch operated stirred tanks , 1997 .
[27] Alvin W. Nienow,et al. On impeller circulation and mixing effectiveness in the turbulent flow regime , 1997 .
[28] P. Beltrame,et al. Side-chain alkylation of toluene by methanol over a basic zeolite: a kinetic study , 1993 .
[29] Chandra P. P. Singh,et al. Simulation of Ammonia Synthesis Reactors , 1979 .
[30] J. Smith. Simple Performance Correlations for Agitated Vessels , 1992 .
[31] Wei-Ming Lu,et al. Effect of blade pitch on the structure of the trailing vortex around rushton turbine impellers , 1998 .
[32] Michael Yianneskis,et al. Hydrodynamic characteristics of dual Rushton impeller stirred vessels , 1996 .
[33] Václav Linek,et al. Gas-liquid mass transfer in vessels stirred with multiple impellers—I. Gas-liquid mass transfer characteristics in individual stages , 1996 .
[34] Piero M. Armenante,et al. Power consumption in agitated vessels provided with multiple-disk turbines , 1998 .
[35] Alvin W. Nienow,et al. Performance of the scaba 6SRGT agitator in mixing of simulated xanthan gum broths , 1993 .
[36] K. Van't Riet,et al. The trailing vortex system produced by Rushton turbine agitators , 1975 .