Fouling, performance and cost analysis of membrane-based water desalination technologies: A critical review

海水淡化 反渗透 结垢 膜污染 环境工程 盐水 环境科学 废水 微咸水 电渗析 纳滤 膜蒸馏 工艺工程 水处理 废物管理 工程类 化学 盐度 生物 生物化学 生态学
作者
Lebea N. Nthunya,Mokgadi F. Bopape,Oranso T. Mahlangu,Bhekie B. Mamba,Bart Van der Bruggen,Cejna Anna Quist-Jensen,Heidi Richards
出处
期刊:Journal of Environmental Management [Elsevier]
卷期号:301: 113922-113922 被引量:124
标识
DOI:10.1016/j.jenvman.2021.113922
摘要

While water is a key resource required to sustain life, freshwater sources and aquifers are being depleted at an alarming rate. As a mitigation strategy, saline water desalination is commonly used to supplement the available water resources beyond direct water supply. This is achieved through effective advanced water purification processes enabled to handle complex matrix of saline wastewater. Membrane technology has been extensively evaluated for water desalination. This includes the use of reverse osmosis (RO) (the most mature membrane technology for desalination), pervaporation (PV), electrodialysis (ED), membrane distillation (MD), and membrane crystallization (MCr). Though nanofiltration (NF) is not mainly applied for desalination purposes, it is included in the reviewed processes because of its ability to reach 90% salt rejection efficiency for water softening. However, its comparison with other technologies is not provided since NF cannot be used for removal of NaCl during desalination. Remarkably, membrane processes remain critically affected by several challenges including membrane fouling. Moreover, capital expenditure (CAPEX) and operating expenditure (OPEX) are the key factors influencing the establishment of water desalination processes. Therefore, this paper provides a concise and yet comprehensive review of the membrane processes used to desalt saline water. Furthermore, the successes and failures of each process are critically reviewed. Finally, the CAPEX and OPEX of these water desalination processes are reviewed and compared. Based on the findings of this review, MD is relatively comparable to RO in terms of process performance achieving 99% salt rejections. Also, high salt rejections are reported on ED and PV. The operation and maintenance (O&M) costs remain lower in ED. Notably, the small-scale MD OPEX falls below that of RO. However, the large-scale O&M in MD is rarely reported due to its slow industrial growth, thus making RO the most preferred in the current water desalination markets.
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