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Simulation and Experiment Study of Flow Field and Dynamic Performance in Stirred Reactor

机译:搅拌釜流场和动态性能的模拟与实验研究。

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The flow field character and dynamic performance of flat blade impeller and 45° angle pitched impeller in the stirred reactor have been researched by Computational Fluid Dynamics (CFD) numerical simulation and Digital Particle Image Velocimetry (DPIV) measuring experiment. The numerical simulation treated the region around stirring impeller with Multi-Reference Frame method, and analyzed the flow field with RNG k-ε turbulence model. It was found that the simulation result was basically same with experiment result, so the numerical simulation method used in this paper was feasible, and the results were reliable; the turbulent energy mainly generated in the region around impeller, and the turbulent performance of flat blade impeller was obviously better than that of 45° angle pitched impeller; the flat blade impeller and 45° angle pitched impeller had different mixing operating characters; it was showed that 45° angle pitched impeller could save almost 40% power consumption than flat blade impeller, through comparison between simulation results and Yong Tian formulas. It could be more economical, fast and reliable to design, optimize and select for the stirred reactor using FLUENT software combining with PIV system.
机译:通过计算流体动力学(CFD)数值模拟和数字粒子图像测速(DPIV)测量实验研究了平板式叶轮和45°角螺距叶轮在搅拌反应器中的流场特性和动力学性能。数值模拟采用多参考框架法处理搅拌叶轮周围区域,并用RNGk-ε湍流模型分析流场。结果表明,仿真结果与实验结果基本相同,因此本文所采用的数值仿真方法是可行的,并且结果可靠。湍流能量主要在叶轮周围产生,平板叶轮的湍流性能明显优于45°角节距叶轮。扁平叶轮和45°角桨叶轮具有不同的混合运行特性。通过仿真结果与永田公式的比较,表明45°角节距叶轮比平叶轮节电近40%。使用FLUENT软件结合PIV系统,对搅拌反应器进行设计,优化和选择可能更加经济,快速和可靠。

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