Friction loss for newtonian and power – Law fluids in expanding and contracting duct flows using the lattice boltzmann method

Q1 Chemical Engineering
José Luis Velázquez Ortega
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Abstract

This study investigates the hydrodynamic behavior of Newtonian and power-law non-Newtonian fluids in a channel with a contraction–expansion–contraction configuration, using the Lattice Boltzmann Method (LBM). Unlike previous research focused on isolated discontinuities, this work introduces a more realistic geometry to capture complex transient phenomena such as vortex formation, flow separation, and shear stress redistribution. Numerical simulations were conducted on a two-dimensional domain and validated against the analytical Poiseuille solution, showing relative errors below 2 %. The analysis was divided into three zones: entrance (A), expansion (B), and contraction (C). In Zone A, the product fRe converged toward the theoretical value of 64, confirming fully developed laminar flow. The head loss coefficient K exhibited a decreasing trend with the generalized Reynolds number, depending on the flow behavior index n. A two-K model was fitted to the data with excellent agreement (relative error below 0.001 %), and the parameters were generalized as functions of n, allowing predictions for fluids beyond those explicitly simulated. In Zone B, the sudden expansion induced complex flow reorganizations, with vortex formation and local recirculation. Although no predictive model was established for this region due to nonlinear and transient effects, the behavior was interpreted using rheological principles. Unlike conventional approaches that artificially fix the Reynolds number, this study applies a constant body force (F) —physically equivalent to a pressure gradient— allowing the generalized Reynolds number (Reg) to emerge naturally from fluid rheology (n, k) and flow geometry. This approach demonstrates how rheology modulates flow reorganization under realistic driving conditions, offering a more faithful representation of flow-rheology interactions in CEC configurations. Overall, the results provide a predictive framework for energy loss assessment in systems combining abrupt geometric discontinuities (sudden expansions/contractions) with complex rheological behavior (from pseudoplastic to dilatant fluids), with direct applications in biomedical devices, food processing, and non-Newtonian fluid transport systems.
用晶格玻尔兹曼方法计算牛顿和幂律流体在膨胀和收缩管道流动中的摩擦损失
本研究使用晶格玻尔兹曼方法(LBM)研究了牛顿流体和幂律非牛顿流体在具有收缩-膨胀-收缩构型的通道中的流体动力学行为。不像以前的研究专注于孤立的不连续面,这项工作引入了更现实的几何结构来捕捉复杂的瞬态现象,如漩涡形成、流动分离和剪应力重分布。在二维域上进行了数值模拟,并与泊泽维尔解析解进行了验证,相对误差在2%以下。分析分为三个区域:入口(A),扩张(B)和收缩(C)。在A区,积fRe向理论值64收敛,证实层流充分发展。水头损失系数K随广义雷诺数的变化呈下降趋势,这取决于流动行为指数n。2 -K模型与数据拟合的一致性非常好(相对误差低于0.001 %),并且参数被广义为n的函数,从而可以对超出明确模拟的流体进行预测。在B区,突然膨胀引起复杂的流动重组,形成涡旋和局部再循环。虽然由于非线性和瞬态效应,没有建立该区域的预测模型,但使用流变学原理解释了该行为。与人为固定雷诺数的传统方法不同,本研究应用恒定的身体力(F) -物理上等同于压力梯度-允许广义雷诺数(Reg)自然地从流体流变学(n, k)和流动几何中出现。该方法展示了流变学如何在现实驾驶条件下调节流动重组,为CEC配置中的流动-流变学相互作用提供了更忠实的表示。总的来说,研究结果为结合突然几何不连续(突然膨胀/收缩)和复杂流变行为(从假塑性到膨胀流体)的系统的能量损失评估提供了预测框架,可直接应用于生物医学设备、食品加工和非牛顿流体输运系统。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
International Journal of Thermofluids
International Journal of Thermofluids Engineering-Mechanical Engineering
CiteScore
10.10
自引率
0.00%
发文量
111
审稿时长
66 days
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