气隙膜蒸馏(AGMD)用于从含抗生素和腐植酸的模型废水中回收水和去除抗生素的膜堵塞分析。

Chemosphere Pub Date : 2024-09-01 Epub Date: 2024-07-24 DOI:10.1016/j.chemosphere.2024.142942
Pyae Phyo Kywe, Chavalit Ratanatamskul
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引用次数: 0

摘要

该研究调查了气隙膜蒸馏(AGMD)在废水中水回收和抗生素去除方面的效率,重点是高浓度情况。实验结果表明,随着进料温度的升高,膜的性能也会增强,在较高温度下,蒸汽渗透通量可达 5 kg/m2.h。尽管进料抗生素溶液中的腐植酸(HA)污垢导致通量减少,但抗生素在 48 小时内始终保持接近完全的排斥率(>99%)。膜表面的污垢通过扫描电镜成像得到了说明。为了了解温度极化和污垢阻力,使用了数学模型,它验证了实验结果,阐明了温度极化效应和传质系数。进料流速的增加减少了热边界层,提高了热通量。更高的温度降低了 HA 的防污能力。因此,AGMD 在水回收和抗生素去除方面证明是有效的,其数学模型有助于对污垢的理解,有利于未来的研究和详细的计算流体动力学 (CFD) 模型。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Membrane fouling analysis of air-gap membrane distillation (AGMD) for recovery of water and removal of antibiotics from a model wastewater containing antibiotics and humic acid.

The study investigates the efficiency of air-gap membrane distillation (AGMD) in water recovery and antibiotics removal from wastewater, focusing on high-concentration scenarios. Experimental findings reveal enhanced membrane performance with increasing the feed temperature, resulting in vapor permeate fluxes of up to 5 kg/m2.h at higher temperatures. Despite experiencing flux reduction caused by fouling from humic acid (HA) in the feed antibiotics solution, the antibiotics consistently maintain near-complete rejection rates (>99%) over 48 h. The foulant on the membrane surface was illustrated by SEM imaging. To know the temperature polarization and the fouling resistance, mathematical modeling was used, and it validates experimental results, elucidating temperature polarization effects and mass transfer coefficients. An increase in feed flow rates reduced thermal boundary layers, enhancing heat flux. Higher temperatures reduced HA fouling resistance. Therefore, AGMD proves effective in water recovery and antibiotics removal, with mathematical models aiding fouling understanding for future research and detailed computational fluid dynamics (CFD) models.

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