[1] A.W. Nienow, Stirring and stirred-tank reactors, Chem. Ing. Tech. 86(12) (20152063-2074.[2] R.V. Calabrese, S.M. Kresta, M. Liu, Recognizing the 21 most influential contributions to mixing research, Chem. Eng. Prog. 110(1) (201420-29.[3] E.L. Paul, V.A. Atiemo-Obeng, S.M. Kresta, Handbook of Industrial Mixing:Science and Practice, John Wiley & Sons, Inc., Hoboken, New Jersey, 2004.[4] G. Montante, K.C. Lee, A. Brucato, M. Yianneskis, An experimental study of doubleto-single-loop flow pattern transition in stirred vessels, Can. J. Chem. Eng. 77(4) (1999) 649-659.[5] G. Montante, K.C. Lee, A. Brucato, M. Yianneskis, Experiments and predictions of the transition of the flow pattern with impeller clearance in stirred tanks, Comput. Chem. Eng. 25(4) (2001) 729-735.[6] G. Montante, K.C. Lee, A. Brucato, M. Yianneskis, Numerical simulations of the dependency of flow pattern on impeller clearance in stirred vessels, Chem. Eng. Sci. 56(12) (2001) 3751-3770.[7] C. Gallettia, E. Brunazzi, M. Yianneskis, A. Paglianti, Spectral and wavelet analysis of the flow pattern transition with impeller clearance variations in a stirred vessel, Chem. Eng. Sci. 58(17) (2003) 3859-3875.[8] K. Rutherford, K.C. Lee, S.M.S. Mahmoudi, M. Yianneskis, Hydrodynamic characteristics of dual Rushton impeller stirred vessels, AIChE J. 42(2) (1996) 332-346.[9] Smith, M., Reversible mixing impeller, USP., 5316443(1999).[10] Bakker, A., Ohio, D., Impeller assembly with asymmetric concave blades, USP., 5791780(1998).[11] K.J. Myers, A.J. Thomas, A. Bakker, M.F. Reeder, Performance of a gas dispersion impeller with vertically asymmetric blades, Chem. Eng. Res. Des. 77(8) (1999) 728-730.[12] D. Pinelli, A. Bakker, K.J. Myers, M.F. Reeder, J. Fasano, F. Magelli, Some features of a novel gas dispersion impeller in a dual-impeller configuration, Chem. Eng. Res. Des. 81(4) (2003) 448-454.[13] Z. Liu, X. Zheng, D. Liu, Y. Wang, C. Tao, Enhancement of liquid-liquid mixing in a mixer-settler by a double rigid-flexible combination impeller, Chem. Eng. Process. 86(2014) 69-77.[14] J. Kumaresan, N.K. Nere, J.B. Joshi, Effect of internals on the flow pattern and mixing in stirred tanks, Ind. Eng. Chem. Res. 44(26) (2005) 9951-9961.[15] Z. Wang, Z.S. Mao, C. Yang, X.Q. Shen, Computational fluid dynamics approach to the effect of mixing and draft tube on the precipitation of barium sulfate in a continuous stirred tank, Chin. J. Chem. Eng. 14(6) (2006) 713-722.[16] J. Min, X.Q. Li, Z.M. Gao, S.X. Xiao, J.M. Smith, R.B. Thorpe, Experimental and CFD studies of a fluid flow in a draft-tube stirred tank, J. Chem. Eng. Jpn 40(8) (2007) 630-635.[17] A. Ochieng, M.S. Onyang, A. Kumar, K. Kiriamoti, P. Musonge, Mixing in a tank stirred by a Rushton turbine at a low clearance, Chem. Eng. Process. 47(5) (2008) 842-851.[18] R. Misumi, T. Toyoda, R. Katayama, K. Nishi, M. Kaminoyama, Optimal seeding conditions for semi-batch type evaporative crystallization of a high suspension density sodium chloride slurry in a draft-tube stirred vessel, J. Chem. Eng. Jpn 44(4) (2011232-239.[19] F. Scargiali, A. Busciglio, F. Grisafi, A. Brucato, Free surface oxygen transfer in large aspect ratio unbaffled bio-reactors, with or without draft-tube, Biochem. Eng. J. 100(2015) 16-22.[20] J. Lueske, K. Kar, L. Piras, J. Pressler, Power draw and gas-liquid mass transfer characteristics of a stirred tank reactor with draft tube configuration, Chem. Eng. Technol. 38(11) (2015) 1993-2001.[21] I. Houcine, E. Plasari, R. David, Effects of the stirred tank's design on power consumption and mixing time in liquid phase, Chem. Eng. Technol. 23(7) (2000) 605-613.[22] G.O. Fountain, D.V. Khakhar, J.M. Ottino, Visualization of three-dimensional chaos, Science 281(1998) 683-686.[23] K. Takahashi, Recent advance in chaotic mixing in a mixing equipment, J. Chem. Eng. Jpn 40(8) (2007) 605-610.[24] M.M. Alvarez, P.E. Arratia, F.J. Muzzio, Laminar mixing in eccentric stirred tank systems, Can. J. Chem. Eng. 80(4) (2002) 546-557.[25] S. Wang, J. Wu, N. Ohmura, Inclined-shaft agitation for improved viscous mixing, Ind. Eng. Chem. Res. 52(33) (2013) 11741-11751.[26] J.Y. Oldshue, H.E. Hirschland, A.T. Gretton, Blending of low-viscosity liquids with side-entering mixers, Chem. Eng. Prog. 52(11) (1956) 481-484.[27] Y. Komoda, Y. Inoue, Y. Hirata, Mixing performance by reciprocating disk in cylindrical vessel, J. Chem. Eng. Jpn 33(6) (2000) 879-885.[28] D.J. Lamberto, F.J. Muzzio, P.D. Swanson, A.L. Tonkovich, Using time-dependent RPM to enhance mixing in stirred vessels, Chem. Eng. Sci. 51(5) (1996) 733-741.[29] W.G. Yao, H. Sato, K. Takahashi, K. Koyama, Mixing performance experiments in impeller stirred tanks subjected to unsteady rotational speeds, Chem. Eng. Sci. 53(17) (1998) 3031-3040.[30] S.M. Kresta, A.W. Etchells Ⅲ, D.S. Dickey, V.A. Atiemo-Obeng, Advances in Industrial Mixing-A Companion to the Handbook of Industrial Mixing, John Wiley & Sons, Inc., Hoboken, New Jersey, 2016.[31] F.L. Yang, S.J. Zhou, X.H. An, Gas-liquid hydrodynamics in a vessel stirred by dual dislocated-blade Rushton impellers, Chin. J. Chem. Eng. 23(11) (2015) 1746-1754.[32] R.L. Liu, S. Li, Z.H. Liu, C.Y. Tao, Y.D. Wang, Chaotic mixing enhanced by punchedflexible impeller in stirred vessel, J. Chem. Ind. Eng. 66(12) (2015) 4736-4742.[33] F.L. Yang, S.J. Zhou, C.X. Zhang, Turbulent flow and mixing performance of a novel six-blade grid disc impeller, Korean J. Chem. Eng. 32(5) (2015) 816-825.[34] H. Wu, G.K. Patterson, Laser-Doppler measurements of turbulent-flow parameters in a stirred mixer, Chem. Eng. Sci. 44(10) (19892207-2221.[35] G. Montante, F. Magelli, Liquid homogenization characteristics in vessels stirred with multiple Rushton turbines mounted at different spacings:CFD study and comparison with experimental data, Chem. Eng. Res. Des. 82(9) (2004) 1179-1187.[36] V.V. Rannade, M. Perrard, C. Xureb, N. Le Sauze, J. Bertrand, Influence of gas flow rate on the structure of trailing vortices of a Rushton turbine, Chem. Eng. Res. Des. 79(8) (2001) 957-964.[37] K. Ng, N.J. Fentiman, K.C. Lee, M. Yianneskis, Assessment of sliding mesh CFD predictions and LDA measurements of the flow in a tank stirred by a Rushton impeller, Chem. Eng. Res. Des. 79(6) (1998) 737-747.[38] J.J. Derksen, M.S. Doelman, H.E.A. Van den Akker, Three-dimensional LDA measurements in the impeller region of a turbulently stirred tank, Exp. Fluids 27(6) (1999) 522-532.[39] G. Ascanio, B. Castro, E. Galondo, Measurement of power consumption in a stirred tank vessels-a review, Chem. Eng. Res. Des. 82(A9) (2004) 1282-1290.[40] S. Murthy, S. Jayanti, CFD study of power and mixing time for paddle mixing in unbaffled vessels, Chem. Eng. Res. Des. 80(5) (2002) 482-498. |