共查询到20条相似文献,搜索用时 548 毫秒
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冷却水流速是影响凝汽器性能的主要因素之一,为了实现基于冷却水流速实际分布的凝汽器性能模拟,借鉴多孔介质的阻力源项加载思想提出了基于冷却管入口实体建模的凝汽器水侧流动计算模型,以某600MW火电机组的低压凝汽器为例,在设计工况下对该凝汽器水侧流动进行了数值模拟,获得了凝汽器水侧管束截面上的冷却水流速分布,并基于上述冷却水流速分布的模拟结果,分别数值计算了冷却水流速均匀分布和不均匀分布两种情况下凝汽器汽侧的蒸汽流动,获得了相应情况下的凝汽器性能。计算结果表明:对于本文研究的凝汽器,基于多孔介质模型和基于冷却管入口实体建模的凝汽器水侧流动模拟得到的管束截面上的冷却水流速分布在流动细节上存在差异;冷却水流速均匀分布和不均匀分布两种情况下获得的凝汽器性能有差异,凝汽器压力相差10.9Pa,总平均传热系数相差12.6W/(m2·K)。建议对于冷却水流速不均匀分布比较严重的情况,在研究凝汽器性能时考虑冷却水流速不均匀分布的影响。 相似文献
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建立了某一凝汽器实际管束的流动计算模型,运用计算流体力学的方法,对该凝汽器水侧流场进行了三维数值模拟。采用分区对称计算方法,大大降低网格数量,从而详细预测了凝汽器水侧进出口水室以及其连接管和冷却水管束内的流动特性。计算结果可以清楚地表明:该凝汽器进口水室存在大量漩涡,使流动阻力增加,流动恶化;水室速度分布不均匀,进口水室管板中心区域流体流速较高而边缘区域较低,结构上存在一定问题;而出口水室的结构较为合理。这与采用多孔介质模型模拟的结论一致,进一步验证了采用多孔介质模型对凝汽器进行计算是正确可行的。计算结果同时表明,冷却水管束内流量和流速的分布是不均匀的,位于中心位置的冷却水管流量较大,而周边区域较小,最大流量差别可达到38%,且相邻管路的流量减小幅度与冷却水管布置有关。冷却水管内冷却水流量和流速的差异将会影响换热器的换热性能。计算结果可为分析研究管排流动不均而引起的换热效率问题提供条件,也可为凝汽器设计和结构优化提供依据。 相似文献
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电站凝汽器蒸汽流动和换热的数值模拟 总被引:14,自引:3,他引:11
提出了一种凝汽器的准三维模拟方法,它可以考虑冷却水温度变化产生的三维影响,也能反映冷却水流程布置对冷凝器性能的影响。用多孔介质及分布阻力等概念模拟凝汽器中的管束和折流板等几何形状。所得的控制方程组用SIMPLE方法求解。针对1台200MW凝汽器进行了数值分析,计算结果与实验数据作了对比,结果是令人满意的。图11表2参7 相似文献
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The effect of the cooling water flow path on the flow and heat transfer in a double tube-pass condenser for a 660 MW power plant unit was numerically investigated based on a porous medium model. The results were used to analyze the streamline, velocity, air mass fraction and heat transfer coefficient distributions. The simulations indicate that the cooling water flow path is important in large condensers. For the original tube arrangement, the heat transfer with the lower-upper cooling water flow path is better than that with the upper-lower cooling water flow path. The reason is that the steam cannot flow into the internal of upper tube bundle and the air fractions are higher in the upper tube bundle with the upper-lower cooling water flow path. An improvement tube arrangement was developed for the upper-lower cooling water flow path which reduced the back pressure by 0.47 kPa compared to the original scheme. Thus, the results show that the tube arrangements should differ for different cooling water flow paths and the condenser heat transfer can be improved for the upper-lower cooling water flow path by modifying the tube arrangement. 相似文献
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火电站直接空冷凝汽器积灰是影响传热性能的重要因素,研究直接空冷凝汽器积灰对传热性能的影响规律并提出监测措施具有重要意义。通过分析汽轮机背压与汽轮机排汽量、冷却空气流量、凝汽器传热系数、凝汽器总传热面积以及环境温度之间的关系,得到了空冷凝汽器在维持汽轮机排汽量和冷却空气量不变时,汽轮机背压和传热系数之间的关系以及凝汽器积灰对汽轮机背压的影响。研究表明:凝汽器积灰会导致凝汽器传热系数降低,汽轮机背压升高,机组运行经济性下降。设计工况下,当蛇形翅片扁平管结构凝汽器积灰厚度达到1.2 mm时,汽轮机背压将增加50%左右。通过监测空冷机组运行过程中汽轮机背压的变化,可预报积灰的程度,为直接空冷凝汽器清洗提供一定的理论依据。 相似文献
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《Applied Thermal Engineering》2014,62(1):37-47
In this paper heat transfer models for large power plant condenser were examined. The goal was to develop a model capable of predicting not only the condenser pressure but the overall heat transfer coefficient. Such a model can be used for condenser condition monitoring. The results of a two-dimensional (2-D) condenser heat transfer model and single-point, zero-dimensional (0-D) model are presented together with the results from Heat Exchanger Institute (HEI) standards curves. Both 0-D and 2-D models can account for the effects of steam-side pressure drop and in a simplified manner also some effects of tube bundle geometry. For all models an experimental correction as a function of cooling water temperature was implemented to improve their accuracy. The results are presented in comparison with the measured plant data for three different tube bundle geometries, with and without the experimental correction factor. The 2-D model proved to be the most consistently accurate of the models both without the correction, and at varying steam and coolant flow with the correction applied. The results indicate significant local variation of pressure drop related effects, which the 0-D model failed to accurately predict particularly in cases of close temperature approach. In predicting the heat transfer coefficient the HEI model was the least accurate, significantly overestimating the impact of coolant flow rate change, and failing to match the measurements even with a correction applied. 相似文献
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