基于CFD的高原室内烟雾箱温场分布和扰流特性数值模拟

Numerical simulation of temperature field distribution and turbulence characteristics of plateau indoor smog chamber based on CFD

  • 摘要: 烟雾箱模拟实验是研究大气污染机理进而制定有效的污染控制对策的一种手段。利用计算流体动力学(CFD)软件Fluent中Realizable k-ε模型模拟高原室内烟雾箱实验系统内传热过程以及不同风扇转速条件下的扰流混合过程,得到烟雾箱实验系统内部温度分布情况以及反应器内的物质浓度分布,分析内部整体空间温度分布的均匀性和反应器内的物质混合程度,并将温度模拟结果与实验结果进行对照。结果表明,根据Realizable k-ε模型通过仿真模拟研究烟雾箱实验系统的流场特性、温场分布以及反应器内物质混合程度,对烟雾箱实验系统性能进行验证,并通过现场实验,测得实测值与仿真值最大误差不超过8.59%;烟雾箱实验系统箱体内部空间温场分布较为均匀,反应器内温度相较箱体内部更难达到温度稳定状态,实际温度呈梯度分布,中心位置温度与设定目标温度相差不超过±1 ℃;反应器内部空间整体物质混合程度较好,但在棱边、顶点以及壁面位置分别出现混合不均和物质聚集现象,风扇转速对混合时间影响较小,过高的转速条件反而会增大反应器内物质的壁损失。

     

    Abstract: The smog chamber simulation experiment is a method for studying the mechanisms of atmospheric pollution and formulating effective pollution control strategies. The Realizable k-ε model in the computational fluid dynamics (CFD) software Fluent was used to simulate the heat transfer process in the plateau indoor smog chamber experimental system and the turbulent mixing process under different fan speeds. The internal temperature distribution of the smog chamber experimental system and the material concentration distribution in the reactor were obtained. The uniformity of the overall spatial temperature distribution and the degree of material mixing in the reactor were analyzed, and the temperature simulation results were compared with the experimental results. The results showed that according to the Realizable k-ε model, the flow field characteristics, temperature field distribution and material mixing degree in the reactor of the smog chamber experimental system were studied by simulation, and the performance of the smog chamber experimental system was verified; through field experiments, the maximum error between the measured value and the simulated value was not more than 8.59%. The temperature field distribution in the chamber of the smog chamber experimental system was relatively uniform, and the temperature in the reactor was more difficult to reach a temperature-stable state than that in the chamber. The actual temperature was distributed in a gradient, and the difference between the temperature value at the center and the set target temperature was less than ±1 ℃. The overall material mixing degree in the internal space of the reactor was good, but the mixing unevenness and material aggregation appeared at the edges, vertices and wall positions, respectively. The fan speed had little effect on the mixing time, and too high speed conditions would increase the wall loss of the material in the reactor.

     

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