NUMERICAL SIMULATION STUDY ON FALLING FILM EVAPORATION OF MOLASSES ETHANOL WASTEWATER
甘蔗糖蜜酒精废水降膜蒸发的数值模拟研究
DOI : https://doi.org/10.35633/inmateh-79-76
Authors
Abstract
To investigate the concentration of molasses ethanol wastewater, a two-dimensional numerical model of falling-film evaporation over horizontal tubes was developed. The model used the Volume of Fluid (VOF) method to capture the liquid-gas interface and was coupled with the Lee phase-change model. The model was validated by comparing the predicted liquid-film thickness and average heat-transfer coefficient with experimental data reported in the literature. The validated model was then used to systematically investigate the effects of spray density (0.10 ~ 0.30 kg/(m·s)) and heat-transfer temperature difference (2 ~ 8 °C) on the falling-film flow and evaporation performance of molasses ethanol wastewater. The results showed that the liquid-film thickness initially decreased and subsequently increased along the circumferential direction, reaching a minimum within the angular range of 90° ~ 120°. Increasing the spray density produced a thicker liquid film; nevertheless, the average heat-transfer coefficient increased monotonically by 23.0% ~ 27.2%, whereas the mass-transfer rate decreased by 19.3% ~ 25.1%. Increasing the heat-transfer temperature difference increased both the average heat-transfer coefficient and the mass-transfer rate. When the temperature difference increased from 2 to 8 °C, the mass-transfer rate increased 2.84 ~ 3.07-fold, and its effect on evaporation performance was substantially greater than that of spray density. Therefore, where operating conditions permit, a lower spray density combined with a higher heat-transfer temperature difference is recommended for the falling-film evaporative concentration of molasses ethanol wastewater.
Abstract in Chinese



