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采用电渗析法进行微咸水淡化:运行参数对能耗和可扩展性的影响

Brackish Water Desalination Using Electrodialysis: Influence of Operating Parameters on Energy Consumption and Scalability.

作者信息

Medina-Toala Angie N, Valverde-Armas Priscila E, Mendez-Ruiz Jonathan I, Franco-González Kevin, Verdezoto-Intriago Steeven, Vitvar Tomas, Gutiérrez Leonardo

机构信息

Faculty of Engineering in Earth Sciences, ESPOL Polytechnic University, Campus Gustavo Galindo, Km. 30.5 Vía Perimetral, Guayaquil 090902, Ecuador.

Department of Geography, Faculty of Science, Humanities and Education, Technical University of Liberec, Komenského 2, 46005 Liberec, Czech Republic.

出版信息

Membranes (Basel). 2025 Jul 31;15(8):227. doi: 10.3390/membranes15080227.

DOI:10.3390/membranes15080227
PMID:40863588
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC12388712/
Abstract

Groundwater is one of the main water sources for consumption, domestic use, agriculture, and tourism in coastal communities. However, high total dissolved solids (TDS) levels in the water (700-2000 mg L TDS) and electrical conductivity (3000-5000 µS cm) threaten the health and economic growth opportunities for residents. This research aims to evaluate the performance of a laboratory-scale electrodialysis system as a technology for desalinating brackish water. For this purpose, water samples were collected from real groundwater sources. Batch experiments were conducted with varying operational parameters, such as voltage (2-10 V), feed volume (100-1600 mL), recovery rate (50-80%), and cros-flow velocity (1.3-5.1 cm s) to determine the electrodialysis system setup that meets the requirements for drinking water in terms of TDS and energy efficiency. A total specific energy consumption of 1.65 kWh m, including pumping energy, was achieved at a laboratory scale. The conditions were as follows: flow velocity of 5.14 cm s, applied voltage of 6 V, feed volume of 1.6 L, and a water recovery of 66%. Furthermore, increasing the flow velocity and the applied voltage enhanced the desalination kinetics and salt removal. Additionally, the system presented opportunities for scalability. This research aims to evaluate a sustainable membrane-based treatment technology for meeting the growing demand for water resources in coastal communities, particularly in developing countries in South America.

摘要

地下水是沿海社区消费、家庭用水、农业和旅游业的主要水源之一。然而,水中高总溶解固体(TDS)水平(700 - 2000 mg/L TDS)和电导率(3000 - 5000 μS/cm)威胁着居民的健康和经济增长机会。本研究旨在评估实验室规模的电渗析系统作为一种淡化微咸水技术的性能。为此,从实际地下水源采集水样。通过改变运行参数进行批次实验,如电压(2 - 10 V)、进料体积(100 - 1600 mL)、回收率(50 - 80%)和错流速度(1.3 - 5.1 cm/s),以确定在TDS和能源效率方面符合饮用水要求的电渗析系统设置。在实验室规模下,包括泵送能量在内的总比能耗为1.65 kWh/m³。条件如下:流速5.14 cm/s、施加电压6 V、进料体积1.6 L、水回收率66%。此外,提高流速和施加电压可增强脱盐动力学和盐分去除效果。此外,该系统具有可扩展性。本研究旨在评估一种基于膜的可持续处理技术,以满足沿海社区,特别是南美洲发展中国家对水资源不断增长的需求。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/6fe8896b1391/membranes-15-00227-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/8586e992f18f/membranes-15-00227-g0A1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/bd6271f7177c/membranes-15-00227-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/1426c6d831b5/membranes-15-00227-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/99ecafff5e09/membranes-15-00227-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/9823332ae190/membranes-15-00227-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/32e4aea5f237/membranes-15-00227-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/cd79c6a3c57b/membranes-15-00227-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/6fe8896b1391/membranes-15-00227-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/8586e992f18f/membranes-15-00227-g0A1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/bd6271f7177c/membranes-15-00227-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/1426c6d831b5/membranes-15-00227-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/99ecafff5e09/membranes-15-00227-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/9823332ae190/membranes-15-00227-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/32e4aea5f237/membranes-15-00227-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/cd79c6a3c57b/membranes-15-00227-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/3760/12388712/6fe8896b1391/membranes-15-00227-g007.jpg

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