Sustainable operation of hybrid semi-batch/batch reverse osmosis by additional purge-and-refill phase: Optimization and life cycle assessment

Hybrid semi-batch/batch reverse osmosis (HSBRO) has been recently proposed as a high-recovery, low-energy, and compact desalination system. In this study, we introduce an additional purge-and-refill phase to minimize internal salt accumulation while enhancing energy efficiency and permeate quality. Experiments were conducted using NaCl- and Na 2 SO 4 -based feedwaters under varying semi-batch operation times, purge-and-refill times, and permeate flux conditions. The results show that extending the purge-and-refill first phase effectively reduces residual brine, thereby mitigating the initial total dissolved solids (TDS) spike, defined as the increase in internal salinity at the start of the semi-batch phase. However, an excessively long purge-and-refill first phase reduces recovery. This trade-off was addressed by compensating with a longer semi-batch operation time, which enabled high recovery with minimal increase in specific energy consumption (SEC). At a concentration of 4000 ppm NaCl, recovery dropped to 84 % with a 60 s purge-and-refill first phase, but was restored to 91 % by adjusting the semi-batch operation time, confirming that careful balancing of operational phases is critical for maintaining system performance. Experimental results identified optimal purge-and-refill first phase times of approximately 20 s for both NaCl and Na 2 SO 4 , effectively minimizing internal salinity and operating pressure. Life cycle assessment (LCA) using the ReCiPe 2016 (H) method revealed that Na 2 SO 4 -based wastewater treatment yielded up to 10 % higher environmental impacts compared to NaCl, highlighting the need for salt-specific operational strategies. These findings establish a practical operational framework for HSBRO, enabling high recovery and low energy demand while incorporating salt-specific environmental considerations. • A novel HSBRO system incorporating an additional purge-and-refill strategy was proposed. • Na 2 SO 4 and NaCl-based feedwaters were tested using a pilot-scale HSBRO system. • The purge-and-refill first phase controlled internal salt accumulation, mitigating TDS spikes. • Recovery increased by 5.5% with no significant rise in SEC when the purge-and-refill first phase time was reduced from 60 s to 20 s. • LCA quantified the environmental impacts of HSBRO operation, supporting energy-efficient and sustainable desalination strategies.

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Publication Details

Journal
Desalination
Published
2025-09-02
DOI
https://doi.org/10.1016/j.desal.2025.119364
Citations
1
Primary Topic
Membrane Separation Technologies
Type
article
Field-Weighted Citation Impact
0.82

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Sustainable operation of hybrid semi-batch/batch reverse osmosis by additional purge-and-refill phase: Optimization and life cycle assessment

Tae-Mun Hwang, A.R. Jeong, Jaeeun Byun, Heun Se Kim et al.
1 citations
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Membrane Separation Technologies
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article

Sustainable operation of hybrid semi-batch/batch reverse osmosis by additional purge-and-refill phase: Optimization and life cycle assessment

Tae-Mun Hwang, A.R. Jeong, Jaeeun Byun, Heun Se Kim, Juwon Lee, Yong-Gyun Park, Kiho Park, GunYoung Kim
article en
1 citations

Abstract

Hybrid semi-batch/batch reverse osmosis (HSBRO) has been recently proposed as a high-recovery, low-energy, and compact desalination system. In this study, we introduce an additional purge-and-refill phase to minimize internal salt accumulation while enhancing energy efficiency and permeate quality. Experiments were conducted using NaCl- and Na 2 SO 4 -based feedwaters under varying semi-batch operation times, purge-and-refill times, and permeate flux conditions. The results show that extending the purge-and-refill first phase effectively reduces residual brine, thereby mitigating the initial total dissolved solids (TDS) spike, defined as the increase in internal salinity at the start of the semi-batch phase. However, an excessively long purge-and-refill first phase reduces recovery. This trade-off was addressed by compensating with a longer semi-batch operation time, which enabled high recovery with minimal increase in specific energy consumption (SEC). At a concentration of 4000 ppm NaCl, recovery dropped to 84 % with a 60 s purge-and-refill first phase, but was restored to 91 % by adjusting the semi-batch operation time, confirming that careful balancing of operational phases is critical for maintaining system performance. Experimental results identified optimal purge-and-refill first phase times of approximately 20 s for both NaCl and Na 2 SO 4 , effectively minimizing internal salinity and operating pressure. Life cycle assessment (LCA) using the ReCiPe 2016 (H) method revealed that Na 2 SO 4 -based wastewater treatment yielded up to 10 % higher environmental impacts compared to NaCl, highlighting the need for salt-specific operational strategies. These findings establish a practical operational framework for HSBRO, enabling high recovery and low energy demand while incorporating salt-specific environmental considerations. • A novel HSBRO system incorporating an additional purge-and-refill strategy was proposed. • Na 2 SO 4 and NaCl-based feedwaters were tested using a pilot-scale HSBRO system. • The purge-and-refill first phase controlled internal salt accumulation, mitigating TDS spikes. • Recovery increased by 5.5% with no significant rise in SEC when the purge-and-refill first phase time was reduced from 60 s to 20 s. • LCA quantified the environmental impacts of HSBRO operation, supporting energy-efficient and sustainable desalination strategies.

DesalinationVol. 616
Chonnam National University (KR), Korea Institute of Civil Engineering and Building Technology (KR), Hanyang University (KR), Anyang University (KR)
Ministry of Environment, Ministry of Land, Infrastructure and Transport, National Research Foundation of Korea, Korea Agency for Infrastructure Technology Advancement, Ministry of Science and ICT, South Korea, Korea Environmental Industry and Technology Institute
Openalex Percentile: Top 23%
Membrane Separation Technologies
0.82
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