[1] M. Basavarajappa, T. Draper, P. Toth, T.A. Ring, S. Miskovic, Numerical and experimental investigation of single phase flow characteristics in stirred tanks using Rushton turbine and flotation impeller, Min. Eng. 83(2015) 156-167. [2] A. Busciglio, G. Montante, A. Paglianti, Flow field and homogenization time assessment in continuously-fed stirred tanks, Chem. Eng. Res. Des. 102(2015) 42-56. [3] J.P. Torré, D.F. Fletcher, T. Lasuye, C. Xuereb, Single and multiphase CFD approaches for modelling partially baffled stirred vessels:comparison of experimental data with numerical predictions, Chem. Eng. Sci. 62(2007) 6246-6262. [4] J. Sossa-Echeverria, F. Taghipour, Computational simulation of mixing flow of shear thinning non-Newtonian fluids with various impellers in a stirred tank, Chem. Eng. Process. 93(2015) 66-78. [5] M. Assirelli, W. Bujalski, A. Eaglesham, A.W. Nienow, Macro and micromixing studies in an unbaffled vessel agitated by a Rushton turbine, Chem. Eng. Sci. 63(2008) 35-46. [6] B. Wang, J. Zhang, H.E. Youduo, A.N. Shengli, Investigation on eccentric agitation in the stirred vessel using 3D-laser Doppler velocimeter, Chin. J. Chem. Eng. 14(2006) 618-625. [7] 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(1998) 3031-3040. [8] J.F. Hall, M. Barigou, M.J.H. Simmons, E.H. Stitt, Mixing in unbaffled high-throughput experimentation reactors, Ind. Eng. Chem. Res. 43(2004) 4149-4158. [9] J. Karcz, J. Szoplik, An effect of the eccentric position of the propeller agitator, Chem. Pap. 58(2004) 9-14. [10] M. Yoshida, Y. Wakura, K. Yamagiwa, A. Ohkawa, S. Tezura, Liquid flow circulating within an unbaffled vessel agitated with an unsteady forward-reverse rotating impeller, J. Chem. Technol. Biotechnol. 85(2010) 1017-1022. [11] S. Woziwodzki, Unsteady mixing characteristics in a vessel with forward-reverse rotating impeller, Chem. Eng. Technol. 34(2011) 767-774. [12] M. Alvarez, Using Spatio-temporal Asymmetry to Enhance Mixing in Chaotic Flows:From Maps to Stirred Tanks(Ph.D. Thesis) Rutgers University, Piscataway, NJ, 2000. [13] K.C. Ng, E.Y.K. Ng, Laminar mixing performances of baffling, shaft eccentricity and unsteady mixing in a cylindrical vessel, Chem. Eng. Sci. 104(2013) 960-974. [14] M. Alvarez, J. Zalc, T. Shinbort, P. Arratia, F. Muzzio, Mechanisms of mixing and creation of structure in laminar stirred tanks, AICHE J. 48(2002) 2135-2148. [15] C. Galletti, E. Brunazzi, On the main flow features and instabilities in an unbaffled vessel agitated with an eccentrically located impeller, Chem. Eng. Sci. 63(2008) 4494-4505. [16] C. Galletti, S. Pintus, E. Brunazzi, Effect of shaft eccentricity and impeller blade thickness on the vortices features in an unbaffled vessel, Chem. Eng. Res. Des. 87(2009) 391-400. [17] G. Montante, A. Bakker, A. Paglianti, F. Magelli, Effect of shaft eccentricity on the hydrodynamics of unbaffled stirred tanks, Chem. Eng. Sci. 61(2006) 2807-2814. [18] J. Karcz, M. Cudak, J. Szoplik, Stirring of a liquid in a stirred tank with an eccentrically located impeller, Chem. Eng. Sci. 60(2005) 2369-2380. [19] P.R. Gogate, A.B. Pandit, Mixing of miscible liquid with density differences. Effect of volume and density of the tracer fluid, Can. J. Chem. Eng. 77(1999) 988-996. [20] S. Woziwodzki, L. Jedrzejczak, Effect of eccentricity on laminar mixing in vessel stirred by double turbine impellers, Chem. Eng. Res. Des. 89(2011) 2268-2278. [21] F.L. Yang, S.J. Zhou, C.X. Zhang, G.C. Wang, Mixing of initially stratified miscible fluids in an eccentric stirred tank:detached eddy simulation and volume of fluid study, Korean J. Chem. Eng. 30(2013) 1843-1854. [22] J.J. Derksen, Blending of miscible liquids with different densities starting from a stratified state, Comput. Fluids 50(2011) 35-45. [23] J.J. Derksen, Direct simulations of mixing of liquids with density and viscosity differences, Ind. Eng. Chem. Res. 51(2012) 6948-6957. [24] M. Cudak, J. Karcz, Momentum transfer in an agitated vessel equipped with an eccentrically located HE 3 impeller, Chem. Process. Eng. 29(2008) 1071-1082. [25] J. Szoplik, J. Karcz, Mixing time of a non-Newtonian liquid in an unbaffled agitated vessel with an eccentric propeller, Chem. Pap. 62(2008) 70-77. [26] J. Szoplik, J. Karcz, The efficiency of the homogenization of non-Newtonian liquid in an agitated vessel with an eccentric propeller, Chem. Process. Eng. 30(2009) 125-138. [27] J. Karcz, M. Cudak, Local momentum and heat transfer in a liquid and gas-solid-liquid systems mechanically stirred in a jacketed vessel, Eleventh Eur Conf Mixing. Bamberg, Germany, proceeding, paper P242003, pp. 447-454. [28] H. Ameur, M. Bouzit, A. Ghenaim, Numerical study of the performance of multistage Scaba 6SRGT impellers for the agitation of yield stress fluids in cylindrical tanks, J. Hydrodyn. 27(2015) 436-442. [29] G. Ascanio, F.A. Tanguy, Mixing of shear-thinning fluids with dual off-centered impellers, Can. J. Chem. Eng. 83(2005) 393-400. [30] F. Cabaret, L. Fradette, P.A. Tanguy, Gas-liquid mass transfer in unbaffled dual-impeller mixers, Chem. Eng. Sci. 63(2008) 1636-1647. [31] S. Woziwodzki, L. Broniarz-Press, M. Ochowiak, Effect of eccentricity on transitional mixing in vessel equipped with turbine impellers, Chem. Eng. Res. Des. 88(2010) 1607-1614. [32] R.K. Thakur, C. Vial, G. Djelveh, M. Labbafi, Mixing of complex fluids with flat-bladed impellers:effect of impeller geometry and highly shear-thinning behavior, Chem. Eng. Process. 43(2004) 1211-1222. [33] M. Alliet-Gaubert, R. Sardeing, C. Xuereb, P. Hobbes, B. Letellier, P. Swaels, CFD analysis of industrial multi-staged stirred vessels, Chem. Eng. Process. 45(2006) 415-427. [34] M. Alvarez, P.E. Arratia, F.J. Muzzio, Laminar mixing in eccentric stirred tank systems, Can. J. Chem. Eng. 80(2002) 546-557. [35] C. Ford, F. Ein-Mozaffari, C.P.J. Bennington, F. Taghipour, Simulation of mixing dynamics in agitated pulp stock chests using CFD, AIChE J. 52(2006) 3562-3569. [36] W. Kelly, B. Gigas, Using CFD to predict the behaviour of power law fluids near axialflow impellers operating in the transitional flow regime, Chem. Eng. Sci. 58(2003) 2141-2152. [37] C. Rivera, S. Foucault, M. Heniche, T. Espinsoa-Slares, P.A. Tanguy, Finite element modelling of the laminar and transition flow of the Superblend dual shaft coaxial mixer on parallel computers, Chem. Eng. Sci. 64(2009) 4442-4456. [38] L. Pakzad, F. Ein-Mozaffari, S.R. Upreti, A. Lohi, Characterisation of the mixing of nonNewtonian fluids with a scaba 6SRGT impeller through ERT and CFD, Can. J. Chem. Eng. 91(2013) 90-100. [39] J. Aubin, I. Naude, C. Xuereb, J. Bertrand, Blending of Newtonian and shear-thinning fluids in a tank stirred with a helical screw agitator, Chem. Eng. Res. Des. 78(2000) 1105-1114. [40] I. Naude, Direct Simulations of Impellers in a Stirred Tank. Contribution to the Optimization of the Choice of an Agitator(Ph.D. thesis) INPT, France, 1998. [41] H. Ameur, M. Bouzit, M. Helmaoui, Hydrodynamic study involving a maxblend impeller with yield stress fluids, J. Mech. Sci. Technol. 26(2012) 1523-1530. [42] B.C.H. Venneker, J.J. Derksen, H.E.A. Van den Akker, Turbulent flow of shear-thinning liquids in stirred tanks-the effects of Reynolds number and flow index, Chem. Eng. Res. Des. 88(2010) 827-843. [43] G.B. Tatterson, Fluid Mixing and Gas Dispersion in Agitated Tanks, McGraw-Hill, New York, 1991221. |