摘要
为定量考察气体流速、壁面过冷度、换热面高度和气体压力对含空气蒸汽冷凝换热的影响,本文采用数值模拟的方法进行了分析。计算了基于COPAIN试验装置和CFD软件STAR-CCM+中的扩散理论冷凝模型,在主流流速0. 1~3 m/s、壁面过冷度4℃~50℃、换热面高度0. 5~6 m以及气体压力0. 1~0. 6 MPa的条件下讨论了冷凝换热特性。研究表明:冷凝换热系数在主流流速小于0. 5 m/s的自然对流主导区内几乎不受速度的影响,换热系数相对偏差在6. 7%以内;壁面过冷度的幂指数可用空气质量份额和过冷度的函数来表示且幂指数范围为-0. 008 3~-0. 367;换热面高度在1 m以内时对冷凝换热性能有明显影响;不同蒸汽质量份额条件下,冷凝换热系数与压力的0. 64次方成正比。通过对计算结果的分析得到了冷凝传热性能与各影响因素之间的量化关系,这对进一步认识含空气蒸汽冷凝现象有一定的指导意义。
Numerical simulations are conducted to quantitatively evaluate the effects of gas velocity,wall sub-cooling,condensation wall height,and gas pressure on condensation heat transfer. The calculations are based on COPAIN experimental facility and diffusion theory-based condensation model incorporated in the CFD software STARCCM +. Condensation heat transfer property is evaluated in terms of velocity from 0. 1 m/s to 3 m/s,wall subcooling from 4 ℃ to 50 ℃,condensation wall height from 0. 5 to 6 m,and pressure from 0. 1 MPa to 0. 6 MPa.Results indicate that the condensation heat transfer coefficient is hardly affected by the mainstream gas velocity in the natural convection-dominated region with velocities less than 0. 5 m/s. Furthermore,the power exponent of wall sub-cooling can be described by a function in terms of air mass fraction and wall sub-cooling,which ranges from-0. 008 3 to-0. 367. The condensation wall height has an obvious effect on the condensation heat transfer when it is less than 1 m,and the heat transfer coefficient has a 0. 64 power direct proportion to the gas pressure.Via numerical results analysis,the quantitative relationship between the condensation heat tranfer porperty and the influencing parameters were concluded,which can to a certain degree promote the understanding of steam condensaiton phenomena in the presence of air.
引文
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