Thermally driven ultrapure water production for water electrolysis – A techno-economic analysis of membrane distillation

IF 8.3 1区 工程技术 Q1 ENGINEERING, CHEMICAL
R. Schwantes , Y. Morales , E. Pomp, J. Singer , K. Chavan , F. Saravia
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Abstract

The transition to hydrogen production with renewable energies necessitates ultrapure water (UPW) as a raw material for water electrolysis, which imposes stringent quality and economic demands on water treatment technologies. This study evaluates the techno-economic feasibility of membrane distillation (MD) as an alternative to reverse osmosis (RO) for UPW production. Utilizing waste heat from a 5 MW proton exchange membrane (PEM) electrolyzer, which would otherwise require active cooling to sustain operation of the electrolyzer, the proposed MD system employs permeate gap membrane distillation to treat feedwaters with brackish and seawater salinities (i.e., 5 g NaCl /kg and 34.3 g NaCl/kg, respectively). The study incorporates numerical simulations to analyse system design parameters and energy consumption of MD and RO systems designed to produce 1 t/h of distillate, as well as experimental data on distillate water quality. Results demonstrate that MD systems achieve high-quality distillate (<3 μS/cm) under the tested salinities and at competitive costs. Estimated unit costs per ton of produced distillate for MD range from €2.33 to €2.85 for either brackish or seawater feed at electricity prices of €0.10–€0.40/kWh, while RO costs range from €2.80 to €5.51 under comparable conditions. The presented annual costs also reflect the cost advantage, especially for seawater desalination with MD costs, approx. 40 % lower than RO. MD shows advantages in energy efficiency with thermal energy provided as low-grade heat. This work shows that MD can be a cost- efficient and versatile solution for UPW production powered by PEM electrolyzer waste heat.
向利用可再生能源制氢过渡需要超纯水(UPW)作为电解水的原材料,这对水处理技术提出了严格的质量和经济要求。本研究评估了用膜蒸馏(MD)替代反渗透(RO)生产超纯水的技术经济可行性。利用 5 兆瓦质子交换膜(PEM)电解槽的余热(否则需要主动冷却以维持电解槽的运行),拟议的 MD 系统采用渗透间隙膜蒸馏法处理咸水和海水盐度(即分别为 5 克氯化钠/千克和 34.3 克氯化钠/千克)的给水。研究结合数值模拟,分析了 MD 和反渗透系统的系统设计参数和能耗(设计产量为每小时 1 吨蒸馏水),以及蒸馏水水质的实验数据。结果表明,在测试的盐度条件下,MD 系统可以获得高质量的蒸馏水(3 μS/cm),而且成本具有竞争力。在电价为 0.10-€0.40/kWh 的条件下,无论是咸水还是海水进料,MD 生产每吨蒸馏物的估计单位成本为 2.33 至 2.85 欧元,而反渗透成本在可比条件下为 2.80 至 5.51 欧元。提出的年成本也反映了成本优势,特别是海水淡化的 MD 成本,比反渗透成本低约 40%。MD 以低品位热能形式提供热能,在能源效率方面具有优势。这项研究表明,在利用 PEM 电解槽废热生产 UPW 的过程中,MD 可以成为一种经济高效且用途广泛的解决方案。
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来源期刊
Desalination
Desalination 工程技术-工程:化工
CiteScore
14.60
自引率
20.20%
发文量
619
审稿时长
41 days
期刊介绍: Desalination is a scholarly journal that focuses on the field of desalination materials, processes, and associated technologies. It encompasses a wide range of disciplines and aims to publish exceptional papers in this area. The journal invites submissions that explicitly revolve around water desalting and its applications to various sources such as seawater, groundwater, and wastewater. It particularly encourages research on diverse desalination methods including thermal, membrane, sorption, and hybrid processes. By providing a platform for innovative studies, Desalination aims to advance the understanding and development of desalination technologies, promoting sustainable solutions for water scarcity challenges.
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