板式换热器通道内的热状态

Y. Elistratova, A. Seminenko, V. Uvarov, V. Minko
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摘要

在热点上配置板式换热器是第三代热电网络不可缺少的结构要素,也是整个供热系统可靠性的重要组成部分。由于不依赖于换热器结构空间中通道之间的传热和水力阻力,这种类型的换热器的优化计算是困难的。研究目的。澄清板式换热器的计算方法,在普遍接受的假设中排除热工和水力条件相等的情况。研究方法是基于使用质量守恒定律来确定每个通道中工质的温度参数。该问题的解以方程组的形式提出,其中每个方程都表示所考虑的通道的热平衡。为了对换热器的热态进行数值研究,建立了换热器的计算机模型。结果表明,作为众所周知的板式换热器热态计算数学模型中的一个假设,通道间流体流量均匀分布的条件是可以接受的。这种限制导致了每个通道中液体温度的均衡。考虑到通道的几何布置,第一和最后通道中加热和加热冷却剂的最终温度相对于已知数据的过剩量高达10%。研究结果证实了由于通道间流动分布不均匀导致冷却剂沿板包长度受热不均匀的假设。在SolidWorks环境中对板式换热器通道内的温度状况进行了分析计算和建模,结果表明几何布置对通道内的温度状况有显著影响。建议在改进板式换热器的设计参数时,考虑到板的位置,采用对换热通道热态不均匀性的数学描述的制定规定。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Thermal Condition in the Channels of Plate Heat Exchangers
Equipping heat points with plate-type heat exchangers is an integral structural element of the 3rd generation heat and power network and a component of the reliability of the heat supply system as a whole. It has been established that the optimization calculations of heat exchangers of this type are difficult due to the absence of dependences on heat transfer and hydraulic resistance between the channels in the structural space of the heat exchanger.Purpose of research. To clarify the method of calculating plate heat exchangers, excluding the equality of thermal and hydraulic conditions from the generally accepted assumptions.Methods. The research methodology is based on the use of the law of conservation of mass in order to determine the temperature parameters of working fluids in each channel. The solution of this problem is proposed in the form of a system of equations, each of the equations of which characterizes the thermal balance of the channel under consideration. A computer model of the heat exchanger is constructed in order to conduct a numerical study of the thermal regime of the heat exchanger.Results. It is indicated that as an assumption in the well-known mathematical model for calculating the thermal regime of a plate-type heat exchanger, the condition of equal distribution of fluid flows between channels is accepted. This restriction leads to equalization of liquid temperatures in each channel. Taking into account the geometric arrangement of the channels, the excess of the final temperature of the heating and heated coolant in the first and last channels with respect to known data is up to 10%. The results of the study confirm the hypothesis of uneven heating of the coolant along the length of the plate package due to the uneven flow distribution between the channels.Conclusion. The results of analytical calculation and modeling in the SolidWorks environment of the temperature regime in the channels of a plate-type heat exchanger indicate a significant influence of the geometric arrangement on the thermal regime in the channels. The formulated provisions of the mathematical description of the unevenness of the thermal regime of heat exchange channels, taking into account the location of the plates, are recommended to be used when improving the design parameters of plate-type heat exchangers.
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