4Foucault S, Ascanio G, Tanguy P A. Power characteristics in coaxial mixing: Newtonian and non-Newtonian fluids [J]. Ind. Eng. Chem. Res. , 2005, 44: 5036-5043. 被引量:1
5Schneider T, Todtenhaupt E. Mixing times and heat transfer in coaxial stirrers. EKATO Ruehr-Mischtech [J]. Chem. Ing. Tech. , 1990, 62 (3): 208-209. 被引量:1
6Foueault S, Ascanio G, Tanguy P A. Coaxial mixer hydrodynamics with Newtonian and non-Newtonian fluids [J]. Chem. Eng. Technol. , 2004, 27 (3): 324-329. 被引量:1
7Rivera C, Foucault S, Heniche M, Espinosa-Solares T, Tanguy P A. Mixing analysis in a coaxial mixer [J]. Chem. Eng. Sci. , 2006, 61 (9) : 2895-2907. 被引量:1
8Farhat M, Rivera C, Fradette L, Heniche M, Tanguy P A. Numerical and experimental study of a dual-shaft coaxial mixer with viscous fluids [ J ]. Ind. Eng. Chem. Res. , 2007, 46 (14): 5021-5031. 被引量:1
9Foucault S, Ascanio G, Tanguy P A. Mixing times in coaxial mixers with Newtonian and non-Newtonian fluids [J]. Ind. Eng. Chem. Res. , 2006, 45 (1) : 352-359. 被引量:1
10Bao Yuyun, Yang Bo, Xie Yong, Gao Zhengming, Zhang Zhongdong, Liu Tao, Gao Xionghou. Power demand and mixing performance of coaxial mixers in non-Newtonian fluids [J].Journal of Chemical Engineering of Japan, 2011, 44 (2): 57-66. 被引量:1