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蒸发式冷凝器传热传质数值模拟研究Numerical Simulation Investigation on Heat and Mass Transfer in Evaporative Condensers
尹应德, 朱冬生, 孙晋飞
蒸发式冷凝器, 传热传质, 顺流, 逆流, 数值模拟Evaporative Condensers, Unsaturated Evaporation, Parallel Flow, Counter Flow, Numerical Simulation
《Advances in Energy and Power Engineering》, Vol.4 No.4, 2016-08-30
The VOF (volume of fluid) method is used to establish a two-dimensional water vapor heat and mass transfer parallel flow and counter flow model. The deviation of calculated film thickness, which is changed with Re values, is greater than the experimental measurement’s value by 3.03% - 6.90%, and the predicted value of the Nusselt theory by 8.33% - 10.34%; it indicates that the model is feasible. The model is used to calculate and analyze liquid water flow distribution, air and water quality and velocity distribution, water vapor quality content distribution in the air, in water and air’s parallel flow and counter flow processes. The results show that: in gas-liquid two- phase counter flow process, the ratio of latent heat transfer rate in total heat transfer rate is above 90% at gas-liquid interface, higher than that of gas-liquid two-phase parallel flow; at air-liquid interface, the main heat transfer is latent heat transfer caused by water’s evaporation and mass transfer, and the supplemented heat transfer is sensible heat transfer caused by temperature difference; counter flow is more conducive to heat transfer than parallel flow.