THE EFFECT OF RHEOLOGICAL COMPLEXITIES ON POWER CONSUMPTION IN AN AERATED, AGITATED VESSEL
暂无分享,去创建一个
[1] K. Riet,et al. Review of Measuring Methods and Results in Nonviscous Gas-Liquid Mass Transfer in Stirred Vessels , 1979 .
[2] H. Taguchi,et al. Power requirement in non‐newtonian fermentation broth , 1966 .
[3] R. Mashelkar,et al. Torque suppression in mechanically stirred liquids and multiphase liquid systems , 1976 .
[4] A. B. Metzner. Agitation of non‐Newtonian fluids , 1957 .
[5] A. W. Nienow,et al. CAVERN SIZES IN AGITATED FLUIDS WITH A YIELD STRESS , 1981 .
[6] A. W. Nienow,et al. Impeller Power Numbers in Closed Vessels , 1971 .
[7] A. Nienow,et al. A dynamometer for the accurate measurement of mixing torque , 1969 .
[8] A. W. Nienow,et al. Gas recirculation rate through impeller cavities and surface aeration in sparged agitated vessels , 1979 .
[9] R. Bates,et al. Examination of Some Geometric Parameters of Impeller Power , 1963 .
[10] A. Nienow,et al. POWER AND HOLD-UP IN THE MIXING OF AERATED HIGHLY VISCOUS NON-NEWTONIAN FLUIDS , 1981 .
[11] A. B. Metzner,et al. Agitation of viscous Newtonian and non-Newtonian fluids , 1961 .
[12] A. W. Nienow,et al. Some effects of pseudoplasticity on hold-up in aerated, agitated vessels , 1980 .
[13] D. Kale,et al. Rotational viscoelastic laminar boundary layer flow around a rotating disc , 1975 .
[14] A. W. Nienow,et al. Surface aeration in a small, agitated, and sparged vessel , 1980 .
[15] M. Denn. Boundary layer flows for a class of elastic fluids , 1967 .