An optimisation framework for minimising power consumption, dead volume, and shear rate of mixing tanks containing shear-thinning fluids utilising CFD

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Liam Merrick Boston, Jos Derksen, Aniruddha Majumder
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Abstract

A hydrodynamic model of a laminar mixing tank containing a shear-thinning power-law fluid stirred by a helical ribbon impeller is created using the Lattice Boltzmann Method and used to train regression models to predict power number, percentage of dead volume, and shear rate statistics. A Reduced Gradient Algorithm is used to maximise a Composite Desirability Function, composed of the regression models, to optimise impeller geometry for selected flow behaviour indices following a Design of Experiments methodology. The regression models are trained on sixty simulations, and validated on eight separate simulations. The range of deviation between regression models and each output response are as follows: impeller power number = 0.047 % to 18 %, percentage of tank dead volume = 0.34 % to 18 %, average shear rate = 0.56 % to 9.0 %, maximum shear rate = 0.46 % to 11 %, and standard deviation of shear rate = 0.69 % to 5.5 %. This is found to be an efficient methodology for optimising mixing conditions, when only a hydrodynamic model is available.

Abstract Image

一个优化框架,用于最大限度地减少功耗,死体积和剪切速率的混合罐包含剪切稀化流体利用CFD
采用格子玻尔兹曼方法建立了包含剪切变薄幂律流体的层流混合槽的水动力模型,并用于训练回归模型,以预测功率数、死体积百分比和剪切率统计数据。减少梯度算法用于最大化复合可取性函数,该函数由回归模型组成,以优化实验设计方法后选定流动行为指数的叶轮几何形状。回归模型在60个模拟上进行了训练,并在8个单独的模拟上进行了验证。回归模型与各输出响应的偏差范围为:叶轮功率数= 0.047% ~ 18%,罐体死体积百分比= 0.34% ~ 18%,平均剪切率= 0.56% ~ 9.0%,最大剪切率= 0.46% ~ 11%,剪切率标准差= 0.69% ~ 5.5%。当只有水动力模型可用时,发现这是优化混合条件的有效方法。
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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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