用户名: 密码: 验证码:
Prediction of onset of Taylor-Couette instability for shear-thinning fluids
详细信息    查看全文
文摘
The definition of Reynolds number (Re) in a Taylor-Couette flow for a shear-thinning fluid is discussed in this paper. Since the shear-thinning property causes spatial distribution of fluid viscosity in a Taylor-Couette flow reactor (TCFR), a method to determine Re by using a numerical simulation is suggested. The effective viscosity (ηeff) in Re was the average viscosity using a weight of dissipation function$$ {\eta}_{\mathrm{eff}}={\displaystyle \sum_{i=1}^N{\overset{\cdot }{\gamma}}_i^2{\eta}_i\Delta {V}_i}/{\displaystyle \sum_{i=1}^N{\overset{\cdot }{\gamma}}_i^2\Delta {V}_i}, $$where N is the total mesh number, ηi (Pa·s) is the local viscosity, \( {\overset{\cdot }{\gamma}}_i \) (1/s) is the local shear-rate, and ΔVi (m3) is the local volume for each cell. The critical Reynolds number, Recr, at which Taylor vortices start to appear, was almost the same value with the Recr obtained by a linear stability analysis for Newtonian fluids. Consequently, Re based on ηeff could be applicable to predict the occurrence of Taylor vortices for a shear-thinning fluid. In order to understand the relation between the rotational speed of the inner cylinder and the effective shear rate that resulted in ηeff, a correlation equation was constructed. Furthermore, the critical condition at which Taylor vortices appear was successfully predicted without further numerical simulation.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700