Parameters of the plain weave meshfor the nozzle of a regenerative heat exchanger

Ya. H. Dvoinos, Pavlo Yevziutin
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Abstract

Regenerative heat exchangers have disadvantages such as low heat transfer coefficient from the nozzle to the gas and high hydraulic resistance due to the design of the nozzles. Wire-mesh nozzles can eliminate these shortcomings of regenerators. Wire-mesh nozzles have low hydraulic resistance and large heat transfer surface. The process of heat and mass transfer in a regenerative heat exchanger is considered. A series of numerical simulation experiments was performed. Theoretically, the optimal configuration of the nozzle was calculated: a plain weave mesh with a wire diameter of 0.4 mm, a weaving step of 2 mm, and a step of placing nets of 1 mm. The operational modes for the regenerator are considered, taking into account the period for drying the nozzle from moisture and the maximum mass of water that can hold the nozzle without the formation of drops. Given the condensation of moisture on the nozzle, the following assumptions are made: There is no temperature and concentration inhomogeneity in the cross section of the regenerator channel; The effect of thermal conductivity in the axial direction in contact between the nozzle elements on the temperature profile of the nozzle is insignificant; The time over which the regenerator is operated between the nozzle drying periods is quite short, and the thickness of the condensate layer does not affect the hydrodynamic mode of the heat regeneration process and the value of the heat transfer coefficient. The duration of the cooling and drying period depends on the humidity of the inlet air and the area of the nozzle. This is due to the need to prevent the accumulation of moisture in the device, which can lead to the reproduction of harmful bacteria and contamination of the nozzle. In the SolidWorks Flow Simulation application, simulation experiments were performed for a regenerator model accounting for the influence of compressed air motion resulting from grouped location of the nozzle elements, and the results are shown in the figures. Comparison of the results from analytical calculations and simulation experiments showed the efficiency of the mathematical model and the possibility of its use in the design calculation of regenerators. Correlation dependences have been established to determine the heat transfer coefficient and hydraulic resistance depending on the hydrodynamic conditions. The mathematical and physical model taking into account the condensation of moisture on the nozzle has been specified. Calculations have been performed for the optimal nozzle made in the form of a plain weave mesh with a wire diameter of 0.4 mm, a weaving step of 2 mm, and a step of placing nets of 1 mm.
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蓄热式换热器喷嘴用平纹编织网的参数
蓄热式换热器由于喷嘴的设计存在喷嘴到气体的传热系数低、水力阻力大等缺点。金属丝网喷嘴可以消除蓄热器的这些缺点。金属丝网喷嘴液压阻力小,传热面大。研究蓄热式换热器的传热传质过程。进行了一系列数值模拟实验。理论上,计算出喷嘴的最优配置:丝径0.4 mm的平纹编织网,编织步长2 mm,放网步长1 mm。考虑了蓄热器的操作模式,考虑了喷嘴从水分中干燥的时间和可以保持喷嘴而不形成水滴的最大水质量。考虑水气在喷嘴上的凝结,作如下假设:蓄热槽截面内不存在温度和浓度的不均匀性;喷嘴元件接触轴向导热系数对喷嘴温度分布的影响不显著;在喷嘴干燥周期之间的蓄热器运行时间很短,并且冷凝层的厚度不影响热再生过程的水动力模式和传热系数的值。冷却和干燥周期的持续时间取决于入口空气的湿度和喷嘴的面积。这是由于需要防止设备内水分的积累,这可能导致有害细菌的繁殖和喷嘴的污染。在SolidWorks Flow Simulation应用程序中,对考虑喷嘴元件分组位置对压缩空气运动影响的再生器模型进行了仿真实验,结果如图所示。分析计算结果与仿真实验结果的比较表明了该数学模型的有效性和在蓄热器设计计算中应用的可能性。建立了根据水动力条件确定传热系数和水力阻力的相关关系式。建立了考虑水气在喷嘴上凝结的数学和物理模型。计算了最优喷嘴的形状为丝径为0.4 mm的平纹编织网,编织步长为2mm,放网步长为1mm。
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