壳螺旋盘管热交换器中基于水和离子液体混合物的 MXene 纳米流体的热力学第二定律、传热和泵功率分析

L.S. Sundar, Sérgio M.O. Tavares, António M.B. Pereira, Antonio C.M. Sousa
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引用次数: 0

摘要

各行各业都广泛使用热交换器来实现两种流体之间的高效热(热)传递,特别是从热流体到冷流体。纳米流体是一种前景广阔的传热流体,在热交换器中表现出卓越的热性能。本研究对使用 MXene/80:20% 水+[MMIM][DMP](质量百分比)离子流体的壳式螺旋盘管热交换器进行了热力学第二定律效率分析。考虑到颗粒重量负载从 0.2% 到 1.0%,雷诺数从 500 到 4300,流速从 0.5 到 3.5 L/min,对壳体和螺旋盘管热交换器的传热系数、熵产生率和放能效率进行了分析研究。在基础流体中,当颗粒重量为 1.0%、雷诺数为 3598 时,传热系数、努塞尔特数、摩擦因数、压降、效率和摩擦生熵分别增加了 45.59%、28.27%、15.19%、12.56%、17.20% 和 16.21%。同时,产生的热熵和破坏的总放热量分别减少了 46.23% 和 20.08%。与基础流体相比,在 1.0 wt.%、雷诺数为 3598 时,第二定律(放能)效率和热性能系数分别提高了 34.04% 和 1.384 倍。本次研究的数据得到了现有文献的证实。根据计算的数据点建立了新的相关关系,以估算努塞尔特数和摩擦因数。
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Second law of thermodynamics, heat transfer, and pumping power analyses of water and ionic liquid mixture based MXene nanofluids in a shell and helical coil heat exchanger
Heat exchangers are extensively employed across diverse sectors for efficient thermal (heat)transfer between two fluids, specifically from a hot fluid to a cold fluid. Nanofluids are promising heat transfer fluids that exhibit exceptional thermal performance in heat exchangers. The present study examines the thermodynamic second law efficiency analysis of a shell and helical coil heat exchanger utilizing MXene/80:20% water+[MMIM][DMP] (mass percentage) based ionanofluids. An analytical investigation was conducted on the heat transfer coefficient, entropy generation rate, and exergy efficiency of a shell and helical coil heat exchanger, considering particle weight loadings from 0.2% to 1.0%, Reynolds numbers from 500 to 4300, and flow rates from 0.5 to 3.5 L/min. In the base fluid, at 1.0 wt.% and at a Reynolds number of 3598, the increase in heat transfer, Nusselt number, friction factor, pressure drop, effectiveness, and frictional entropy generation are 45.59%, 28.27%, 15.19%, 12.56%, 17.20%, and 16.21%, respectively. Concurrently, thermal entropy generation, and total exergy destruction were reduced by 46.23% and 20.08%, respectively. The second law (exergy) efficiency and thermal performance factor are improved by 34.04% and 1.384-times, respectively, at 1.0 wt.% and at a Reynolds number of 3598, compared to the base fluid. The data from the current study is corroborated by existing literature. New correlations were developed from the computed data points to estimate the Nusselt number and friction factor.
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