垂直条件下空气存在下蒸汽冷凝结构效应的数值研究

Shuhang Zhou, Xian-ke Meng, Haozhi Bian, M. Ding
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摘要

在各种工业应用中,存在不可冷凝气体的蒸汽冷凝是一种普遍现象。它已通过实验研究和数值分析进行了广泛的研究。以往的实验研究和数值分析都集中在单一结构上。为了评价蒸汽在不同冷凝结构下的冷凝换热特性,本文在较宽的参数范围内(压力为0.2 ~ 1.6 MPa,空气质量分数为0.16 ~ 0.71)对不同结构进行了数值模拟。在评价中,研究了不同冷凝结构(单管、平板、圆柱、球形)下的冷凝换热系数。结果表明,冷凝面结构对蒸汽冷凝换热特性有显著影响。在低压和高空气质量分数条件下,四种冷凝结构的换热性能几乎没有差异。随着压力的增大和空气质量分数的降低,筒形换热器的传热性能最好,其次是球形换热器和板形换热器,最差的是单管换热器。此外,在压力为1.6MPa,空气质量分数为0.16时,气缸的冷凝换热系数(CHTC)可比单管的冷凝换热系数(CHTC)大40%。
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Numerical Investigations on Structure Effect for Steam Condensation in the Presence of Air Under Vertical Condition
Steam condensation in the presence of non-condensable gas is a general phenomenon in various industrial applications. It has been broadly investigated by experimental studies and numerical analyses. Previous experimental studies and numerical analyses have focused on single structure. To evaluate the condensation heat transfer characteristics of steam for various condensation structure, the present work conducted numerical simulations based on various structure at a wide parameter range (pressure from 0.2 to 1.6 MPa and air mass fraction from 0.16 to 0.71). In the assessments, the condensation heat transfer coefficient with various condensation structure (single tube, plate, cylinder, spherical) were investigated. The results indicate that the structure of the condensation surface has a significant effect on the heat transfer characteristics of steam condensation. There is almost no difference in the heat transfer performance of the four condensation structures under the low pressure and high air mass fraction condition. With the increase of pressure and the decrease of air mass fraction, the heat transfer performance of the cylinder is the best, followed by the spherical and plate, and the worst is the single tube. In addition, the condensation heat transfer coefficient (CHTC) of the cylinder can be 40% greater than that of the single tube at a pressure of 1.6MPa and an air mass fraction of 0.16.
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