Numerical and Experimental Study of Thermal-Hydraulic Processes in the Convergent-Divergent Channels of Plate Heat Exchangers with Etched Channels

IF 1.3 Q4 ENERGY & FUELS
V. O. Kindra, I. A. Maksimov, D. V. Patorkin, O. V. Zlyvko, I. I. Komarov
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Abstract

The cost and efficiency of power installations depend to a great extent on the design characteristics of heat transfer equipment. These characteristics are especially important for gas turbine units with regenerators operating on low boiling working fluids with low temperature differences and high pressure differences. For such highly efficient energy systems with regeneration, the use of plate heat exchangers containing microchannels obtained by chemical etching of their surface holds promise. For improving their thermal-hydraulic efficiency, versions of extended heating surfaces with convergent-divergent channels are proposed in the article. A set of calculated and experimental studies of the newly developed channels for plate heat exchangers was carried out. Convective heat transfer was numerically simulated, the results of which made it possible to determine the influence of key geometrical parameters, namely, the relative segment length L/H and expansion amplitude A/H on the thermal-hydraulic characteristics in a wide range of Reynolds number values (2500 ≤ Re ≤ 15 000). It is shown that with a periodically narrowed and widened channel cross section, flow acceleration and deceleration zones are produced; directed action on the boundary layers takes place, and turbulent mixing is enhanced. This helps eliminate stagnant zones and obtain more uniform distribution of heat removal over the surface. Based on mathematical modeling, correlation dependences for the Nusselt number and the friction coefficient as functions of the Reynolds number have been obtained, which are suitable for engineering assessments of the efficiency of heat exchangers with similar geometrical parameters of the channels. To verify the numerical study results, an experimental setup was developed, and tests of channel models with recording the heat transfer and pressure losses were carried out, which have confirmed the correctness of the theoretical approach and repeatability of the revealed regularities. The obtained results can serve for confirming the rational choice of geometrical parameters and practical applicability of modified plate heat exchangers with chemically etched channels as part of compact regenerators of advanced power facilities.

Abstract Image

刻蚀板式换热器收敛-发散通道热工过程的数值与实验研究
电力装置的成本和效率在很大程度上取决于传热设备的设计特点。这些特性对于在低温差和高压差的低沸点工作流体上运行的蓄热器的燃气轮机机组尤其重要。对于这种具有再生能力的高效能源系统,使用含有微通道的板式热交换器,通过化学蚀刻其表面来获得它们是有希望的。为了提高热工效率,本文提出了带收敛-发散通道的扩展受热面形式。对新开发的板式换热器通道进行了一系列的计算和实验研究。对对流换热进行了数值模拟,得到了相对管段长度L/H和膨胀幅值A/H等关键几何参数在大雷诺数范围内(2500≤Re≤15 000)对对流换热特性的影响。结果表明:沟道截面周期性变窄和变宽,形成了水流加减速带;边界层发生定向作用,湍流混合增强。这有助于消除停滞区,并在表面上获得更均匀的热量去除分布。在数学建模的基础上,得到了努塞尔数和摩擦系数随雷诺数的相关关系,适用于具有相似通道几何参数的换热器效率的工程评价。为了验证数值研究结果,建立了实验装置,并进行了记录传热和压力损失的通道模型测试,验证了理论方法的正确性和揭示规律的可重复性。所得结果可为先进电力设施紧凑型蓄热器中带有化学腐蚀通道的改进型板式换热器几何参数的合理选择和实际适用性提供依据。
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来源期刊
CiteScore
1.30
自引率
20.00%
发文量
94
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