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Pressure drop analysis of steam condensation in air-cooled circular tube bundles

机译:风冷圆管束中蒸汽凝结的压降分析

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Pressure losses on the condensing-side of an air-cooled condenser (ACC) have the potential to inhibit condenser performance and, ultimately, curtail plant efficiency. However, little information is available on the magnitude and effect of these losses in an ACC under typical Rankine cycle operating conditions. This article seeks to improve current understanding on steam-side pressure losses in ACCs by presenting an experimental study on the losses in a full-scale ACC circular tube bundle. Saturated steam at low pressure was condensed by a cross flow of cooling air, provided by a bank of axial fans. Full condensation occurred in all measurements, which were carried-out over a steam pressure and temperature range of approximately 0.05-0.14 bar absolute and 33-55 degrees C, respectively. These test parameters ensured that measurement program test conditions were representative of those expected in an operational thermoelectric power plant. Experimental mass fluxes, per individual tube, varied from 0.7 to 2 kg/m(2) s during testing. The pressure drop characteristics were, therefore, analysed over a vapour Reynolds numbers range of 1890-5150 and liquid Reynolds number range of 25-95. Results indicate that the measured pressure drop through the tube bundle was relatively small, in the range of 130-250 Pa. As shown in this article, the reason for this was due to momentum recovery as the steam condenses to form liquid condensate. This phenomenon offsets the frictional losses, which are shown to be comparable in magnitude to momentum recovery in a condensing flow. However, this may not always be the case. Therefore, since the frictional component is traditionally the most problematic to predict, a range of liquid gas two-phase frictional pressure drop predictive models were reviewed, and are presented herein. Comparisons between these models and the experimental data show that the most applicable model was found to be that of Lockhart & Martinelli. This demonstrated reasonable accuracy of +/- 18%. (C) 2015 Elsevier Ltd. All rights reserved.
机译:风冷冷凝器(ACC)冷凝侧的压力损失可能会抑制冷凝器性能,并最终降低设备效率。但是,在典型兰金循环操作条件下,关于ACC中这些损失的大小和影响的信息很少。本文旨在通过对全尺寸ACC圆管束中的压力损失进行实验研究,来提高对ACC中蒸汽侧压力损失的当前了解。低压饱和蒸汽由一排轴流风扇提供的冷却空气的交叉流冷凝。在所有测量中均发生完全凝结,这些测量分别在绝对压力约为0.05-0.14 bar和33-55℃的蒸汽压力和温度范围内进行。这些测试参数确保测量程序的测试条件能够代表运行中的热电厂所预期的条件。在测试过程中,每根管的实验质量通量从0.7到2 kg / m(2)s不等。因此,在蒸气雷诺数范围为1890-5150和液体雷诺数范围为25-95的情况下分析了压降特性。结果表明,通过管束测得的压降相对较小,在130-250 Pa范围内。如本文所示,其原因是由于蒸汽冷凝形成液体冷凝物而导致的动量恢复。这种现象抵消了摩擦损失,摩擦损失的大小与冷凝流中的动量恢复相当。但是,并非总是如此。因此,由于摩擦分量传统上是最难以预测的,因此对液化气两相摩擦压降预测模型的范围进行了回顾,并在此进行了介绍。这些模型与实验数据之间的比较表明,最适用的模型是Lockhart&Martinelli。这证明了+/- 18%的合理精度。 (C)2015 Elsevier Ltd.保留所有权利。

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