化工学报 ›› 2022, Vol. 73 ›› Issue (5): 1974-1985.DOI: 10.11949/0438-1157.20211783

• 流体力学与传递现象 • 上一篇    下一篇

黏弹性表面活性剂溶液中颗粒沉降特性研究

苏晓辉1(),张弛1,徐志锋1,金辉2,王治国1()   

  1. 1.西安石油大学机械工程学院,陕西 西安 710065
    2.西安交通大学动力工程及多相流国家重点实验室,陕西 西安 710049
  • 收稿日期:2021-12-20 修回日期:2022-03-19 出版日期:2022-05-05 发布日期:2022-05-24
  • 通讯作者: 王治国
  • 作者简介:苏晓辉(1987—),男,博士,讲师,xhsu@xsyu.edu.cn
  • 基金资助:
    国家自然科学基金项目(51906202);陕西省自然科学基金项目(2019JQ-814)

Study on particle settling behavior in viscoelastic surfactant solutions

Xiaohui SU1(),Chi ZHANG1,Zhifeng XU1,Hui JIN2,Zhiguo WANG1()   

  1. 1.School of Mechanical Engineering, Xi’an Shiyou University, Xi’an 710065, Shaanxi, China
    2.State Key Laboratory of Multiphase Flow in Power Engineering, Xi’an Jiaotong University, Xi’an 710049, Shaanxi, China
  • Received:2021-12-20 Revised:2022-03-19 Online:2022-05-05 Published:2022-05-24
  • Contact: Zhiguo WANG

摘要:

黏弹性表面活性剂溶液悬浮颗粒流广泛存在于自然界和工业生产中,黏弹性表面活性剂溶液的非线性流变性质及应力松弛效应对其中颗粒沉降有着显著影响。采用FENE-P和Giesekus黏弹性本构模型对表面活性剂溶液中颗粒沉降特性进行研究,发现两种本构模型不仅表现出剪切稀化,而且出现拉伸硬化。颗粒在沉降初期的不稳定性主要是由溶液自身的弹性效应引起,弹性效应越强,颗粒沉降速度不稳定性越强,而剪切稀化效应会减弱颗粒沉降速度的不稳定。颗粒沉降过程中在其尾部形成一个“负尾迹”,随着剪切稀化和拉伸硬化效应增强,负尾迹区增大,弹性效应增加,负尾迹增强,负尾迹区流体内部反向速度分布导致的表面活性剂溶液中微观胶束的拉伸断裂和重构可能是引起颗粒沉降速度持续波动的原因。

关键词: 表面活性剂, 流体动力学, 悬浮系, 非牛顿流体, 剪切稀化, 颗粒沉降, 模拟

Abstract:

The suspended particle flow of viscoelastic surfactant solution widely exists in nature and industrial production. The nonlinear rheological properties and stress relaxation effect of viscoelastic surfactant solution have a significant impact on the particle settlement. The FENE-P and Giesekus constitutive models were used to study the sedimentation characteristics of particles in surfactant solutions. The hydrodynamics of the viscoelastic fluid is solved regarding the settling spherical particle as the reference system. Firstly, the rheological properties of the FENE-P and Giesekus fluids are obtained from the numerical solution of constitutive equations under the planar shear flow and the uniaxial tension conditions. It shows that both constitutive models exhibit not only the shear thinning but also the tension hardening, and the shear band appears when the mobility factor is larger than 0.8 for Giesekus fluids. The numerical results show that the elasticity of the fluid causes the instability of the settling velocity of the particle at the beginning. The stronger the elasticity of the fluid is, the stronger the instability of the settling velocity of the particle is. While the shear thinning weakens the instability of the settling velocity of the particle. The shear thinning and tension hardening affect the flow simultaneously and a negative wake is formed behind the particle. The negative wake region enlarges when the shear thinning and tension hardening are enhanced, and the negative wake is also enhanced with the increase in the fluid elasticity. However, the simulated settling velocity of the sphere using the FENE-P and Giesekus models becomes steady after a while, and the sphere reaches a constant terminal velocity eventually. It shows some difference from the unusual experimental phenomenon, e.g. the continuous velocity fluctuation of the settling sphere in actual surfactant wormlike micellar fluids. Thus, the FENE-P and Giesekus models are incapable when they are used to describe the particle behaviors in these surfactant wormlike micellar fluids. The breakage and reformation of the micro-scale wormlike micelles in surfactant solutions caused by the reversed velocity in the negative wake region may be the reason for the fluctuation of the settling velocity of a particle in this kind of viscoelastic fluids. Therefore, an advanced constitutive model is needed to clarify the phenomenon in the future study.

Key words: surfactants, hydrodynamics, suspensions, non-Newtonian fluids, shear thinning, particle settling, simulation

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