首页> 外文会议>ASME international technical conference and exhibition on packaging and integration of electronic and photonic microsystems >THERMAL-HYDRAULIC PERFORMANCE AND OPTIMIZATION OF TUBE ELLIPTICITY IN A PLATE FIN-AND-TUBE HEAT EXCHANGER
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THERMAL-HYDRAULIC PERFORMANCE AND OPTIMIZATION OF TUBE ELLIPTICITY IN A PLATE FIN-AND-TUBE HEAT EXCHANGER

机译:板翅管换热器的热液性能和管椭圆率的优化

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The flow field inside the heat exchangers is associated with maximum heat transfer and minimum pressure drop. Designing a compact heat exchanger and employing various techniques to enhance its overall performance has been widely investigated and still an active research field. However, few researches deal with thermal optimization. The application of elliptic tube is an effective alternative to circular tube which can reduce the pressure drop significantly. In this study, numerical simulation and optimization of variable tube ellipticity is studied at low Reynolds numbers. The three-dimensional numerical analysis and a multi-objective genetic algorithm (MOGA) with surrogate modelling is performed. Two row tubes in staggered arrangement in fin-and-tube heat exchanger is investigated for combination of various elliptic ratio (e =minor axis/major axis) and Reynolds number. Tube elliptic ratio ranges from 0.2 to 1 and Reynolds number ranges from 150 to 750. The tube perimeters are kept constant while changing the elliptic ratio. The numerical model is derived based on continuum flow approach and steady-state conservation equations of mass, momentum and energy. The flow is assumed as incompressible and laminar due to low inlet velocity. Results are presented in the form of Colburn factor, friction factor, temperature contours and streamline contours. Results show that increasing elliptic ratio increases the friction factor due increased flow blocking area, however, the effect on the Colburn factor is not significant. Moreover, tube with lower elliptic ratio followed by higher elliptic ratio tube has better thermal-hydraulic performance. To achieve maximum heat transfer enhancement and minimum pressure drop, the Pareto optimal strategy is adopted for which the CFD results, Artificial neural network (ANN) and MOGA are combined. The tubes elliptic ratio (0.2 ≤ e ≤ 1.0) and Reynolds number (150 ≤ Re ≤ 750) are the design variables. The objective functions include Colburn factor (j) and friction factor (f). The CFD results are input into ANN model. Once the ANN is computed and its accuracy is checked, it is then used to estimate the model responses as a function of inputs. The final trained ANN is then used to drive the MOGA to obtain the Pareto optimal solution. The optimal values of these parameters are finally presented.
机译:热交换器内的流场与最大传热和最小压降相关联。设计紧凑型换热器并采用各种技术来提高其整体性能,已被广泛调查和仍然是一个活跃的研究领域。然而,很少有研究处理热优化。椭圆管的应用是圆形管的有效替代方案,可以显着降低压降。在该研究中,在低雷诺数中研究了可变管椭圆形的数值模拟和优化。进行三维数值分析和具有代理建模的多目标遗传算法(MOGA)。对翅片管热交换器中交错布置的两条排管进行了各种椭圆比(E =短轴/长轴)和雷诺数的组合。管椭圆形比率为0.2至1,雷诺数范围为150至750.管周长在改变椭圆比时保持恒定。基于连续的流动方法和质量,动量和能量的稳态保护方程来源的数值模型。由于低入口速度,该流动被假定为不可压缩和层流。结果以科兰因子,摩擦因子,温度轮廓和流线轮廓的形式提出。结果表明,椭圆形比率的增加增加了摩擦因子增加的流量阻塞区域,然而,对COLBurn因子的影响并不重要。此外,具有较低椭圆比的管之后具有更高的椭圆比管具有更好的热液压性能。为了实现最大传热增强和最小压​​降,采用帕累托最佳策略,CFD结果,人工神经网络(ANN)和MOGA组合。管椭圆形比(0.2≤e≤1.0)和雷诺数(150≤Re≤750)是设计变量。目标功能包括COLBurn因子(J)和摩擦系数(F)。 CFD结果输入了ANN模型。一旦计算了ANN并检查了其准确度,然后使用它来估计模型响应作为输入的函数。然后使用最终培训的ANN来驱动MOGA以获得Pareto最佳解决方案。最终呈现这些参数的最佳值。

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