An experimental study of the mixing characteristics of viscoplastic fluids in dual-impeller agitation systems

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL Chemical Engineering Research & Design Pub Date : 2025-02-26 DOI:10.1016/j.cherd.2025.02.032
Andrew W. Russell , Patrick M. Piccione , Paul F. Luckham , Konstantin S. Pervunin , Christos N. Markides
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Abstract

We study experimentally the agitation of viscoplastic Carbopol™ 980 (C980) fluids in a 2.5-L vertical unbaffled cylindrical vessel using central dual-impeller stirring systems, examining the mixing characteristics of different combinations of standard six-blade Rushton turbines (RTs) and downward-pumping 45°-pitched four-blade turbines (PBTs) of identical diameter D = 41 mm. We consider the effects of rotational speed (as expressed by the modified power-law Reynolds number, Rem), impeller separation (G/D = 0.73 and 1.22) and a variety of arrangements of the rotors on the mixing characteristics of these systems. Phenomena of cavern segregation and internal flow compartmentalisation are revealed and explained in terms of expected flow patterns. Dual-RT stirrers are found to produce highly symmetrical flow patterns, influenced by the impeller separation, along with strong time-dependent compartmentalisation between the internal flows of both caverns. This flow compartmentalisation can be, however, avoided in dual-PBT systems due to the downward-pumping nature of this system, which also allows for the achievement of a state of full tank homogeneity through cavern engulfment. Comparing the total equivalent volumes of the caverns, Vctot, for the examined dual-impeller systems, the mixing effectiveness, as characterised by the growth of Vctot with Rem, is maximised for the RT-PBT and PBT-RT arrangements with a separation of G/D = 1.22, for which Vctot is 70–100 % larger at Rem = 18.5 compared to the dual-RT and dual-PBT arrangements. Although the RT-PBT arrangement performs well, it does not achieve a homogeneous mixing state of the viscoplastic fluid throughout the entire vessel within a reasonable time. Thus, the most efficient mixing system is that featuring a PBT rotor overlying a RT. The findings demonstrate the significant influence of the selection and geometrical arrangement of dual-impeller systems on the mixing of viscoplastic fluids.
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粘塑性流体在双叶轮搅拌系统中混合特性的实验研究
我们实验研究了粘塑性Carbopol™980 (C980)流体在2.5 l垂直无挡板圆柱形容器中的搅拌,使用中央双叶轮搅拌系统,研究了标准六叶Rushton涡轮机(RTs)和相同直径D = 41 mm的45°倾斜四叶涡轮机(pts)的不同组合的混合特性。我们考虑了转速(用修正幂律雷诺数Rem表示)、叶轮分离(G/D = 0.73和1.22)和各种转子布置对这些系统混合特性的影响。揭示了洞室离析和内部流动分区现象,并根据预期的流动模式进行了解释。发现双rt搅拌器产生高度对称的流动模式,受叶轮分离的影响,以及两个洞穴内部流动之间强烈的时间依赖性分区。然而,在双pbt系统中,由于该系统的向下泵送特性,可以避免这种流动分隔,这也允许通过洞穴吞没实现全罐均匀状态。通过对比所研究的双叶轮系统的洞室总当量Vctot,混合效率(以Vctot随Rem的增长为特征)在G/D = 1.22的分离下,RT-PBT和PBT-RT布置达到最大,在Rem = 18.5时,Vctot比双rt和双pbt布置大70-100 %。尽管RT-PBT布置性能良好,但它无法在合理的时间内实现粘塑性流体在整个容器内的均匀混合状态。因此,最有效的混合系统是PBT转子覆盖在rt上的混合系统。研究结果表明,双叶轮系统的选择和几何布置对粘塑性流体的混合有显著影响。
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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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