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首页> 外文期刊>Energies >Experimental Assessment of a Helical Coil Heat Exchanger Operating at Subcritical and Supercritical Conditions in a Small-Scale Solar Organic Rankine Cycle
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Experimental Assessment of a Helical Coil Heat Exchanger Operating at Subcritical and Supercritical Conditions in a Small-Scale Solar Organic Rankine Cycle

机译:小规模太阳能有机朗肯循环中亚临界和超临界条件下螺旋线圈换热器的实验评估

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In this study, the performance of a helical coil heat exchanger operating at subcritical and supercritical conditions is analysed. The counter-current heat exchanger was specially designed to operate at a maximal pressure and temperature of 42 bar and 200 °C, respectively. The small-scale solar organic Rankine cycle (ORC) installation has a net power output of 3 kWe. The first tests were done in a laboratory where an electrical heater was used instead of the concentrated photovoltaic/thermal (CPV/T) collectors. The inlet heating fluid temperature of the water was 95 °C. The effects of different parameters on the heat transfer rate in the heat exchanger were investigated. Particularly, the performance analysis was elaborated considering the changes of the mass flow rate of the working fluid (R-404A) in the range of 0.20–0.33 kg/s and the inlet pressure varying from 18 bar up to 41 bar. Hence, the variation of the heat flux was in the range of 5–9 kW/m 2 . The results show that the working fluid’s mass flow rate has significant influence on the heat transfer rate rather than the operational pressure. Furthermore, from the comparison between the experimental results with the heat transfer correlations from the literature, the experimental results fall within the uncertainty range for the supercritical analysis but there is a deviation of the investigated subcritical correlations.
机译:在这项研究中,分析了在亚临界和超临界条件下运行的螺旋盘管热交换器的性能。逆流热交换器经过专门设计,可分别在最高压力和42 bar和200°C的温度下运行。小型太阳能有机朗肯循环(ORC)装置的净功率输出为3 kWe。最初的测试是在实验室中进行的,该实验室中使用电加热器代替集中的光伏/热(CPV / T)收集器。水的入口加热流体温度为95°C。研究了不同参数对换热器传热率的影响。特别是,在考虑工作流体质量流量(R-404A)在0.20-0.33 kg / s范围内变化以及入口压力从18 bar到41 bar不等的情况下,对性能进行了详细的分析。因此,热通量的变化范围是5–9 kW / m 2。结果表明,工作流体的质量流率对传热率而不是工作压力有显着影响。此外,通过将实验结果与传热相关性进行比较,实验结果在超临界分析的不确定性范围内,但所研究的亚临界相关性存在偏差。

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