Sustainable operation of hybrid semi-batch/batch reverse osmosis by additional purge-and-refill phase: Optimization and life cycle assessment
- Authors
- Kim, Heun Se; Byun, Jaeeun; Jeong, Ahyeon; Kim, GunYoung; Lee, Juwon; Hwang, Tae-mun; Park, Yong-Gyun; PARK, Khio
- Issue Date
- Dec-2025
- Publisher
- ELSEVIER
- Keywords
- Desalination; HSBRO; High recovery; High energy efficiency; SEC; Salt retention; LCA
- Citation
- Desalination, v.616, pp 1 - 24
- Pages
- 24
- Indexed
- SCIE
SCOPUS
- Journal Title
- Desalination
- Volume
- 616
- Start Page
- 1
- End Page
- 24
- URI
- https://scholarworks.bwise.kr/hanyang/handle/2021.sw.hanyang/208754
- DOI
- 10.1016/j.desal.2025.119364
- ISSN
- 0011-9164
1873-4464
- 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<inf>2</inf>SO<inf>4</inf>-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<inf>2</inf>SO<inf>4</inf>, effectively minimizing internal salinity and operating pressure. Life cycle assessment (LCA) using the ReCiPe 2016 (H) method revealed that Na<inf>2</inf>SO<inf>4</inf>-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.
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