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Mathematical modelling and simulation of multiphase flow in a flat plate solar energy collector

机译:平板太阳能集热器中多相流的数学建模与仿真

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Non-conventional collectors where organic fluid or refrigerant experience a phase change have many advantages over conventional collectors which have either air or relatively high temperature boiling liquid. Increase in heat transfer coefficient and system efficiency, corrosion prevention and freeze protection are the main benefits of the first type. In this study, a detailed numerical model of a flat plate collector is developed to investigate the fluid mean temperature, useful heat gain and heat transfer coefficient along the collector tube. The refrigerant HFC-134a was used in the simulation as the working fluid of the collector. The model can both predict the location where the fluid undergoes a phase change in the tube and the state at the exit under given inlet conditions. The effect of boiling on the heat transfer coefficient of the fluid is also investigated. Simulations were performed at three different mass flow rates (0.001, 0.005 and 0.01 kg/s) and three different operating pressures (4, 6 and 8 bar) to be able to see the effect of mass flow rate and pressure on plate temperature, heat loss coefficient, efficiency of the collector and the heat transfer coefficient of the fluid. The simulation results indicate that the heat transfer coefficient of the fluid increases from 153.54 W/m(2) K to 610.27 W/m(2) K in multiphase flow region. In the liquid single phase region, the collector efficiency rises from 60.2% to 68.8% and the heat transfer coefficient of the fluid increases from 39.24 W/m(2) K to 392.31 W/m(2) K with an increased flow rate whereas the collector efficiency decreases from 72.5% to 62.3% as the operating pressure increases from 4 bar to 8 bar. In order to validate the simulation model an experimental test rig was built and the experiments were performed with HFE 7000 as working thermo-fluid. A new simulation model utilizing HFE 7000 has been developed and the outlet temperature of the fluid was compared with the measured outlet temperature. Both measured and simulated results have shown close conformity. (C) 2015 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/4.0/).
机译:有机流体或制冷剂经历相变的非常规收集器比具有空气或相对高温沸腾液体的常规收集器具有许多优势。传热系数和系统效率的提高,防腐和防冻是第一类产品的主要优点。在这项研究中,开发了平板集热器的详细数值模型,以研究流体平均温度,有用的热增益和沿集热管的传热系数。模拟中使用制冷剂HFC-134a作为收集器的工作流体。该模型既可以预测流体在管中发生相变的位置,又可以预测给定入口条件下出口处的状态。还研究了沸腾对流体传热系数的影响。在三种不同的质量流量(0.001、0.005和0.01 kg / s)和三种不同的工作压力(4、6和8 bar)下进行了模拟,以了解质量流量和压力对板温度,热量的影响损耗系数,收集器的效率以及流体的传热系数。仿真结果表明,在多相流区域中,流体的传热系数从153.54 W / m(2)K增加到610.27 W / m(2)K。在液相单相区域,收集器效率从60.2%提高到68.8%,流体的传热系数从39.24 W / m(2)K增加到392.31 W / m(2)K,流量增加,而当工作压力从4 bar增加到8 bar时,收集器效率从72.5%降低到62.3%。为了验证仿真模型,建立了实验测试台,并以HFE 7000作为工作热流体进行了实验。已经开发了一种使用HFE 7000的新仿真模型,并将流体的出口温度与测得的出口温度进行了比较。测量结果和模拟结果均显示出高度一致性。 (C)2015作者。由Elsevier Ltd.发布。这是CC BY许可下的开放访问文章(http://creativecommons.org/licenses/by/4.0/)。

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