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Numerical investigations on steam condensation in the presence of air on external surfaces of 3 × 3 tube bundles

机译:3×3管束外表面上存在空气时蒸汽冷凝的数值研究

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Previous investigations on steam condensation in the presence of air have revealed general heat transfer characteristics in vertical plates and single tubes. However, there remains limited knowledge regarding the thermal-hydraulic phenomena and heat transfer properties of tube bundles. In order to evaluate steam condensation on the external surfaces of tube bundles, STAR-CCM + code with a diffusion boundary layer steam condensation model was employed in this work. In the assessments, 3 × 3 tube bundles with various tube pitches (from 1.5d to 5d) were investigated, and the results were compared to those of a single tube. The data analyses mainly focused on three aspects: (i) global and local condensation phenomena in tube bundles; (ii) heat transfer characteristics in tube bundles; and (iii) influences of tube pitches and global parameters (such as pressure and air mass fraction) on the condensation heat transfer. The phenomena analyses indicate that the axial field profiles are mainly determined by the development of a concentration boundary layer, while the radial field profiles are mostly affected by the tube pitches. Local heat flux analyses indicate that the condensation heat flux exhibits a significant reduction downwards along the vertical tube. In comparison, the condensation heat flux fluctuates in the tube peripheral direction. In the latter case, heat transfer enhancement and inhibition regions are identified and classified. For the tube average heat transfer, only the central tube is significantly affected by the tube pitches, and the degradation may be more than 30% at a tube pitch of 1.5d. The tube pitch effect is almost independent of the bulk air mass fraction and changes slightly with an increase in the wall sub-cooling and bulk pressure.
机译:先前对存在空气的情况下蒸汽凝结的研究表明,垂直板和单管的传热特性一般。然而,关于管束的热工现象和传热特性的知识仍然有限。为了评估管束外表面上的蒸汽冷凝,在这项工作中采用了带有扩散边界层蒸汽冷凝模型的STAR-CCM +代码。在评估中,研究了3×3个具有不同管距(从1.5d到5d)的管束,并将结果与​​单个管的结果进行了比较。数据分析主要集中在三个方面:(i)管束中的整体和局部凝结现象; (ii)管束中的传热特性; (iii)管间距和整体参数(例如压力和空气质量分数)对冷凝传热的影响。现象分析表明,轴向场轮廓主要由浓度边界层的形成决定,而径向场轮廓主要受管间距影响。局部热通量分析表明,冷凝热通量沿垂直管向下显着减小。相比之下,冷凝热通量在管圆周方向上波动。在后一种情况下,对传热增强和抑制区域进行识别和分类。对于管子的平均传热,仅中心管子受管子间距的影响很大,在1.5d的管子间距下,降级可能超过30%。管间距效应几乎与整体空气质量分数无关,并且随着壁过冷和整体压力的增加而略有变化。

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