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首页> 外文期刊>International Journal of Heat and Mass Transfer >Local heat transfer coefficient during stratified flow in large, flattened- tube steam condensers with non-uniform heat flux and wall temperature
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Local heat transfer coefficient during stratified flow in large, flattened- tube steam condensers with non-uniform heat flux and wall temperature

机译:具有不均匀热通量和壁温的大型扁平管式蒸汽冷凝器在分层流动过程中的局部传热系数

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摘要

Steam condensation heat transfer coefficient (HTC) in a large, flattened tube with non-uniform heat flux and wall temperature, and variable inclination angle is determined experimentally. The condenser tube is that typically used in an air-cooled condenser for power plants. The steel tube has an elongated-slot cross section with inner dimensions of 216 x 16 mm. Water vapor and liquid flow co-currently through a 5.7 m long air-cooled conditioning section, followed by a 0.12 m long water-cooled test section. The long conditioning section creates conditions in the test section that mimic the conditions in an operating condenser - allowing for the realistic development of flow regime and void fraction. HTC is then determined in the water-cooled section. The water-cooled section is designed as a crossflow heat exchanger to match the temperature and heat flux conditions of an air-cooled condenser. Visualization sections at the tube inlet and outlet allow determination of flow regime and void fraction. The flow is found to be stratified for all conditions. Tube inclination angle is varied from 0 to 38 degrees downwards. Inlet quality in the water-cooled section ranges from 0 to 0.74. HTC is found to increase by more than 400% along the condenser height. In addition, inclination angle, wall-steam temperature difference, inlet water-steam temperature difference, water temperature glide and vapor quality are all found to affect the condensation HTC. (C) 2019 Elsevier Ltd. All rights reserved.
机译:实验确定了大的扁平管中的蒸汽凝结传热系数(HTC),该管的热通量和壁温不均匀,并且倾角可变。冷凝器管通常用于发电厂的风冷冷凝器中。钢管具有细长的横截面,内部尺寸为216 x 16 mm。水蒸气和液体并流通过一个5.7 m长的空气冷却调节段,然后是一个0.12 m长的水冷测试段。长的调节段会在测试段中创建条件,该条件模仿正在运行的冷凝器中的条件-从而使流动状态和空隙率得到切实的发展。然后在水冷部分确定HTC。水冷段设计为横流热交换器,以匹配风冷冷凝器的温度和热通量条件。管子入口和出口处的可视化部分可以确定流态和空隙率。发现在所有条件下流量都是分层的。管的倾斜角度从0到38度向下变化。水冷段的入口质量范围为0到0.74。发现HTC沿冷凝器高度增加了400%以上。此外,发现倾斜角度,壁蒸汽温度差,进水蒸汽温度差,水温滑动和蒸汽质量都会影响冷凝HTC。 (C)2019 Elsevier Ltd.保留所有权利。

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