[1] V.B. Rewatkar, A.J. Deshpande, A.B. Pandit, J.B. Joshi, Gas hold-up behavior of mechanically agitated gas-liquid reactors using pitched blade downflow turbines, Can. J. Chem. Eng. 71(1993)226-237.[2] G.J. Xu, Y.M. Li, Z.Z. Hou, L.F. Feng, K. Wang, Gas-liquid dispersion and mixing characteristics and heat transfer in a stirred vessel, Can. J. Chem. Eng. 75(1997)299-306.[3] J.M. Smith, Z. Gao, H. Muller-Steinhagen, The effect of temperature on the void fraction in gas-liquid reactors, Exp. Thermal Fluid Sci. 28(2004) 473-478.[4] J.C. Gabelle, E. Jourdier, R.B. Licht, F.B. Chaabane, I. Henaut, J. Morchain, F. Augier, Impact of rheology on the mass transfer coefficient during the growth phase of Trichoderma reesei in stirred bioreactors, Chem. Eng. Sci. 75(2012) 408-417.[5] J.J. Wang, L.C. Li, X.P. Gu, L.F. Feng, Progress on CFD simulation of gas-liquid two-phase flow in stirred tank reactor, Process Equip. Piping 49(2012) 1-4(in Chinese).[6] F. Yang, S. Zhou, X. An, Gas-liquid hydrodynamics in a vessel stirred by dual dislocated-blade Rushton impellers, Chin. J. Chem. Eng. 23(2015) 1746-1754.[7] J.J. Zhang, Z.M. Gao, L.Q. Yin, Y.Y. Bao, Gas dispersion and mass transfer in a hotsparged multi-impeller stirred tank, J. Beijing Univ. Chem. Technol. Nat. Sci. 42(2015) 15-20(in Chinese).[8] J.M.T. Vasconcelos, S.C.P. Orvalho, A.M.A.F. Rodrigues, S.S. Alves, Effect of blade shape on the performance of six-blade disk turbine impellers, Ind. Eng. Chem. Res. 39(2000)203-213.[9] Q.H. Zhang, Y.M. Yong, Z.S. Mao, Y. Chao, C.J. Zhao, Experimental determination and numerical simulation of mixing time in a gas-liquid stirred tank, Chem. Eng. Sci. 64(2009)2926-2933.[10] N. Gao, Local void fraction and bubble size distribution in a gas liquid multi-impeller stirred tank, Master Thesis, Beijing University of Chemical Technology, China, 2010.[11] M. Taghavi, R. Zadghaffari, J. Moghaddas, Y. Moghaddas, Experimental and CFD investigation of power consumption in a dual Rushton turbine stirred tank, Chem. Eng. Res. Des. 89(2011)280-290.[12] K.E. Morud, B.H. Hjertager, LDA measurements and CFD modelling of gas-liquid flow in a stirred vessel, Chem. Eng. Sci. 51(1996)233-249.[13] W. Wang, Z.S. Mao, C. Yang, Experimental and numerical investigation on gas holdup and flooding in an areared stirred tank with Rushton impeller, Ind. Eng. Chem. Res. 45(2006) 1141-1151.[14] X.N. Zhang, Y.Y. Bao, Z.M. Gao, Effect of temperature on gas-liquid dispersion in multi-impeller three-phase reactor, Sciencepaper Online 3(2008) 184-188(in Chinese).[15] Y.Y. Bao, J. Yang, B.J. Wang, Z.M. Gao, Influence of impeller diameter on local gas dispersion properties in a sparged multi-impeller stirred tank, Chin. J. Chem. Eng. 23(2015) 615-622.[16] M. Ramezani, B. Kong, X. Gao, M.G. Olsen, R.D. Vigil, Experimental measurement of oxygen mass transfer and bubble size distribution in an air-water multiphase Taylor-Couette vortex bioreactor, Chem. Eng. J. 279(2015)286-296.[17] J.C. Gabelle, J. Morchain, D. Anne-Archard, F. Augier, A. Line, Experimental determination of the shear rate in a stirred tank with a non-Newtonian fluid:Carbopol, AICHE J. 59(2013)2251-2266.[18] M. Gavrilescu, R.V. Roman, Oxygen mass transfer and gas holdup in a bubble column bioreactor with biosynthesis liquid, Acta Biotechnol. 14(1994)27-36.[19] J.C. Gabelle, F. Augier, A. Carvalho, R. Rousset, J. Morchain, Effect of tank size on kLa and mixing time in aerated stirred reactors with non-Newtonian fluids, Can. J. Chem. Eng. 89(2011) 1139-1153.[20] Z. Zhou, Characteristics of gas liquid flows in stirred tank bioreactor, Master Thesis, East China University of Science and Technology, China, 2014.[21] B. Liu, B. Huang, Y. Zhang, J. Liu, Z. Jin, Numerical study on gas dispersion characteristics of a coaxial mixer with viscous fluids, J. Taiwan Inst. Chem. Eng. 66(2016) 54-61.[22] B. Liu, F. Fan, X. Chen, J. Liu, Z. Jin, The influence of impeller combination on the gas-liquid dispersion performance of a coaxial mixer in viscous fluids, Int. J. Chem. React. Eng. (2017)https://doi.org/10.1515/ijcre-2016-0191.[23] N. Hashemi, F. Ein-Mozaffari, S.R. Upreti, D.K. Hwang, Analysis of mixing in an aerated reactor equipped with the coaxial mixer through electrical resistance tomography and response surface method, Chem. Eng. Res. Des. 109(2016) 734-752.[24] N. Hashemi, F. Ein-Mozaffari, S.R. Upreti, D.K. Hwang, Analysis of power consumption and gas holdup distribution for an aerated reactor equipped with a coaxial mixer:Novel correlations for the gas flow number and gassed power, Chem. Eng. Sci. 151(2016)25-35.[25] N. Hashemi, F. Ein-Mozaffari, S.R. Upreti, D.K. Hwang, Experimental investigation of the bubble behavior in an aerated coaxial mixing vessel through electrical resistance tomography (ERT), Chem. Eng. J. 289(2016) 402-412.[26] T. Espinosa-Solares, L.F.E. Brito-De, A. Tecante, P.A. Tanguy, Flow patterns in rheologically evolving model fluids produced by hybrid dual mixing systems, Chem. Eng. Technol. 24(2001) 913-918.[27] T. Espinosa-Solares, L.F.E. Brito-De, A. Tecante, P.A. Tanguy, Gas dispersion in rheologically-evolving model fluids by hybrid dual mixing systems, Chem. Eng. Technol. 25(2002) 723-727.[28] B. Liu, Y. Zheng, H. Liang, M. Wang, Z. Jin, CFD simulation on shear-thinning gas-liquid dispersion in coaxial mixer, CIESC J. 68(2017)2280-2289.[29] S.J. Arjunwadkar, K. Sarvanan, P.R. Kulkarni, A.B. Pandit, Gas-liquid mass transfer in dual impeller bioreactor, Biochem. Eng. J. 1(1998) 99-106.[30] F. Garcia-Ochoa, E. Gomez, Bioreactor scale-up and oxygen transfer rate in microbial processes:An overview, Biotechnol. Adv. 27(2009) 153-176.[31] M.L. Jackson, C.-C. Shen, Aeration and mixing in deep tank fermentation systems, AICHE J. 24(1978) 63-71.[32] P. Moilanen, M. Laakkonen, O. Visuri, V. Alopaeus, J. Aittamaa, Modelling mass transfer in an aerated 0.2 m3 vessel agitated by Rushton, Phasejet and Combijet impellers, Chem. Eng. J. 142(2008) 95-108.[33] M.M. Wang, Research on gas dispersion, mass-transfer, mixing characteristics of coaxial mixers in shear-thinning fluids, Master Thesis, Zhejiang University, China, 2016.[34] M.S. Puthli, V.K. Rathod, A.B. Pandit, Gas-liquid mass transfer studies with triple impeller system on a laboratory scale bioreactor, Biochem. Eng. J. 23(2005)25-30.[35] M.O. Albaek, K.V. Gernaey, S.M. Stocks, Gassed and ungassed power draw in a pilot scale 550 litre fermentor retrofitted with up-pumping hydrofoil B2 impellers in media of different viscosity and with very high power draw, Chem. Eng. Sci. 63(2008) 5813-5820.[36] D.Y. Luan, S.J. Zhou, S.Y. Chen, S.P. Chu, CFD simulation of the flow field and cavern formation of pseudoplastic fluid with a 6-bent-blade impeller, Chin. J. Process. Eng. 10(2010) 1054-1059(in Chinese). |