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Seawater-to-Resource Technology

Author(s)
Jeong, Seongwoo
Advisor
Kim, Youngsik
Issued Date
2026-02
URI
https://scholarworks.unist.ac.kr/handle/201301/91529 http://unist.dcollection.net/common/orgView/200000964476
Abstract
Seawater that contains water and dissolved salt (35 kg in 1 m3), represents a vast feedstock for producing high-value resources such as freshwater, sodium hydroxide (NaOH), chlorine (Cl2), and hydrogen (H2). These resources are essential across a wide range of industries including agriculture, power generation, paper and pulp, polyvinyl chloride (PVC), steel, and energy. However, conventional technologies for freshwater extraction and brine treatment rely on pressure- or heat- driven processes, requiring as much as 75.9 kWh m-3 of energy. Moreover, in the electrolysis of salt for NaOH, Cl2, and H2 production, the net NaOH yield is limited to only about 7 kg per 10 kAh, corresponding to 47 % of the theoretical value, due to NaOH consumption during impurity removal. In this study, a new electrochemical platform—referred to as the seawater-to-resource technology—was developed by integrating and adapting electrochemical processes with conventional systems. The first approach, an ion-exchange desalination battery integrated with conventional freshwater extraction, utilizes the 1 wt% brackish water generated during charge–discharge cycling as RO feedwater, reducing the desalination energy from 2.98 kWh m⁻³ to 0.96 kWh m⁻³. Although the conventional system suffered from poor Cl⁻ capture reversibility (<30 %), this study introduced an ion-exchange-based method that enhanced reversibility to 99.9 %, achieving stable cyclic performance. The second approach, electrodialysis (ED) integrated with conventional brine treatment, addressed the high energy burden of evaporation-based salt recovery (≈73 kWh m⁻³). By selectively removing ions rather than evaporating the entire brine, the ED process successfully reduced the total energy requirement to 36.8 kWh m⁻³, while maintaining effective salt concentration and reducing the subsequent evaporation load. Finally, in the electrolysis with a solid electrolyte, a Na⁺-conductive ceramic (NASICON) membrane was introduced in place of conventional polymeric Nafion to enable selective sodium transport without brine purification. This design increased Na⁺ utilization and enabled the production of approximately 14.9 kg of NaOH per 10 kAh, corresponding to 99.6 % of the theoretical yield. These results demonstrate that the seawater-to-resource technology, based on integrative and adaptive electrochemical processes, provides a highly efficient and sustainable pathway for simultaneous freshwater generation and chemical resource production from seawater.
Publisher
Ulsan National Institute of Science and Technology
Degree
Doctor
Major
School of Energy and Chemical Engineering

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