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Convective Bubbly Flow of Water in an Annular Pipe: Role of Total Dissolved Solids on Heat Transfer Characteristics and Bubble Formation

机译:环形管道中的对流泡沫流动:总溶解固体对传热特性和泡沫形成的作用

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摘要

Formation of bubbles in water inside an annulus pipe in a flow boiling regime was experimentally investigated. The effect of various variables, such as total dissolved solid materials (TDS) in terms of mass fraction, flow rate of water, and applied heat flux (HF) on the heat transfer coefficient (HTC) and bubble behavior of water, was experimentally investigated. A regression formula was fitted to estimate the average bubble diameter at various TDS values, with accuracy of <4.1% up to heat flux of 90 kW/m2. Results show that the presence of TDS materials can increase the contact angle of bubble and bubble diameter, and also promotes the HTC value of the system. However, flow rate of water suppressed bubble generation, and increased the heat transfer coefficient due to the renewal of the thermal boundary layer around the boiling surface. Likewise, it was identified that forced convective and nucleate boiling heat transfer mechanisms contribute to the flow of boiling water, and heat flux is a key parameter in determining the mechanism of heat transfer. In the present study, heat flux of 15 kW/m2 at 50 °C was the heat flux in which onset of nucleate boiling was identified inside the annulus pipe. The contact angle of water at TDS values of 300 mg/L and 1200 mg/L was 74° and 124°, respectively, showing the improvement in heat transfer characteristics of water due to the presence of TDS materials.
机译:实验研究了流动沸腾制度的环管内的水中泡沫的形成。实验研究了各种变量,例如总溶解的固体材料(TDS)的效果,诸如总溶解的固体材料(TDS),水的流速和施加的热通量(HF)和水的泡沫行为的施加热通量(HF),进行了实验研究。回归配方拟合以估计各种TDS值的平均气泡直径,精度为90 kW / m 2的热通量<4.1%。结果表明,TDS材料的存在可以增加气泡和气泡直径的接触角,并促进系统的HTC值。然而,由于沸腾表面周围的热边界层更新,水抑制气泡产生的流速增加,并增加了传热系数。同样,鉴定出强制对流和核心沸腾的传热机制有助于沸水的流动,​​热通量是确定热传递机制的关键参数。在本研究中,在50℃下15千瓦/平方米的热通量为在其中发生泡核沸腾的被确定的环管内的热通量。 TDS值为300mg / L和1200mg / L的水的接触角分别为74°和124°,显示出由于TDS材料的存在而导致的水的热传递特性的改善。

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