Cao Yan, Taghvaie Nakhjiri Ali, Ghadiri Mahdi
School of Computer Science and Engineering, Xi'an Technological University, Xi'an, 710021, China.
Department of Petroleum and Chemical Engineering, Science and Research Branch, Islamic Azad University, Tehran, Iran.
Sci Rep. 2024 Feb 22;14(1):4340. doi: 10.1038/s41598-024-54061-5.
Sweeping gas membrane distillation (SGMD) is considered a membrane distillation configuration. It uses an air stream to collect the water vapour. A 2D mathematical model is prepared in the current study to predict the effect of various operating parameters on the SGMD performance. Also, the temperature distribution in the SGMD was obtained. The effect of air inlet temperature, salt concentration, feed and air flowrate on air and salted solution outlet temperature and vapour flux through the membrane is investigated. There was good agreement between experimental data and modelling outputs. It was found that increase in air inlet temperature from 40 to 72 °C was increased the outlet temperature of air stream and cold solution from 37 to 63 °C and 38 to 65 °C respectively. Furthermore, increase in air inlet temperature led to the enhancement of vapour flux in the membrane distillation. Also, the salt concentration and feed flow rate did not have meaningful influence on the outlet temperatures, however, the flux was increased by increasing feed flowrate.
吹扫气膜蒸馏(SGMD)被认为是一种膜蒸馏构型。它使用气流来收集水蒸气。在本研究中建立了一个二维数学模型,以预测各种操作参数对SGMD性能的影响。此外,还获得了SGMD中的温度分布。研究了进气温度、盐浓度、进料和空气流量对空气和盐溶液出口温度以及通过膜的蒸汽通量的影响。实验数据与模型输出结果吻合良好。结果发现,进气温度从40℃升高到72℃,分别使气流和冷溶液的出口温度从37℃升高到63℃、从38℃升高到65℃。此外,进气温度的升高导致膜蒸馏中蒸汽通量的增加。而且,盐浓度和进料流速对出口温度没有显著影响,然而,通量随着进料流速的增加而增加。