DOI QR코드

DOI QR Code

초순수 제조 공정의 폐수발생량 저감을 위한 역삼투 공정 고회수율 설계

High recovery reverse osmosis design to minimize wastewater of ultra-pure water production process

  • 이현우 (부경대학교 토목공학과) ;
  • 김동건 (부경대학교 토목공학과) ;
  • 전종민 (부경대학교 토목공학과) ;
  • 김수한 (부경대학교 토목공학과)
  • Hyunwoo Lee (Department of Civil Engineering, Pukyong National University) ;
  • Dongkeon Kim (Department of Civil Engineering, Pukyong National University) ;
  • Jongmin Jeon (Department of Civil Engineering, Pukyong National University) ;
  • Suhan Kim (Department of Civil Engineering, Pukyong National University)
  • 투고 : 2023.05.22
  • 심사 : 2023.06.13
  • 발행 : 2023.06.15

초록

The production process of ultra-pure water (UPW) involves dozens of unit processes such as reverse osmosis (RO), pretreatments, membrane degasifier, and several ion exchange processes. Recently, continuous electrodeionization (CEDI) has replaced the 2-bed and 3-tower (2B3T) ion exchange process. As a result, the majority of wastewater in UPW production now comes from the RO concentrate. The important of RO in UPW production is to produce high-quality water with a low ion concentration (around 1 mg/L) for CEDI feed water. Minimizing RO concentrate is essential to reduce the wastewater produced in the UPW production process. This can be achieved by maximizing the recovery of the RO system. However, increasing the recovery is limited by the water quality of the RO permeate. To ensure high-quality permeate water, the RO system is designed with a two-pass configuration. The recovery of each pass in the RO system is limited (e.g., < 85%) due to the expected increase in permeate water concentration at higher RO feed water concentrations. Interestingly, tests using 4-inch RO modules with low concentration feed water (≤ 35 mg/L as NaCl) revealed that the permeate concentration remains almost constant regardless of the feed water concentration. This implies that the recovery of the first RO pass can be increased as long as the average feed/concentrate concentration of the second RO pass is less than 35 mg/L. According to this design criterion for the RO system, the recovery of the first and second RO pass, with a feed water concentration of 250 mg/L as NaCl, can be increased up to 94.8% and 96.0%, respectively. Compared to the conventional RO system design (e.g., 70% and 80% for the first and second RO pass) for UPW production, this maximum recovery design reduces the volume of RO feed and concentrate by up to 38.4% and 89.2%, respectively.

키워드

과제정보

본 연구는 환경부의 재원으로 한국환경산업기술원의 고순도 공업용수 생산공정 국산화 플랜트 설계/시공기술 개발 사업의 지원을 받아 연구되었습니다(2021003210007).

참고문헌

  1. Choi, B.S. (2013). Ultrapure water industry and technology trends, korea agency for infrastructure Technology Advancement, Issue Report of KAIA, 1-16.
  2. DUPONT Water Solutions FilmTecTM Reverse Osmosis Membranes Technical Manual, https://www.dupont.com/content/dam/dupont/amer/us/en/water-solutions/public/documents/en/RO-NF-FilmTec-Manual-45-D01504-en.pdf (May 19, 2023).
  3. Hwang, J.S. (2020). The Korea Economic Daily, https://www.hankyung.com/economy/article/202305195887i (May 19, 2023).
  4. Jeon, J.M., Kim, D.K., Kim, N.R., and Kim, S.H. (2023). Applicability and limitation of the industrial reverse osmosis system simulators, Desalination, 549, 116358.
  5. Jeon, J.M., Kim, S.S., Seo, I.S., and Kim, S.H. (2020). Considerations to design high-pressure membrance system to produce high quality potable water with lower organic matter concentration, J. Korean Soc. Water Wastewater, 34(6), 473-480. https://doi.org/10.11001/jksww.2020.34.6.473
  6. Jung, J.H., Kim, N.R., Jeon, J.M., and Kim, S.H. (2019). Reliability assessment of reverse osmosis system projection programs, J. Korean Soc. Environ. Eng., 41(1), 42-47. https://doi.org/10.4491/KSEE.2019.41.1.42
  7. Kim, K.S., Moon, D.S., Kim, H.J., Lee, S.W., Ji, H., Jung, H.J., and Won, H.J. (2014). The effect of feed temperature on premeate flux during membrane separation, J. Korean Soc. Mar. Environ. Energy., 17(1), 13-19. https://doi.org/10.7846/JKOSMEE.2014.17.1.13
  8. Kim, S.H., Kang, S.T., and Park, H.K. (1998). A study of optimal pretrreatment system for the desalination using reverse osmosis, J. Korean Soc. Environ. Eng., 20(10), 1367-1375.
  9. Lee, C.S. (1996). The current of ultra water system, Membr. J., 6(3), 127-140.
  10. Lee, H.J., and Kim, S.H. (2014). Removal of low concentration organic matter by reverse osmosis membranes in ultrapure water production process, J. Korean Soc. Water Wastewater, 28(4), 391-396. https://doi.org/10.11001/jksww.2014.28.4.391
  11. Lee, H.K., Jin, Y.X., and Hong, S.K. (2016). Recent transitions in ultrapure water (UPW) technology: Rising role of reverse osmosis (RO), Desalination, 399, 185-197. https://doi.org/10.1016/j.desal.2016.09.003
  12. OEM Engineering Manual ElectropureTM XL & EXL Series EDI, https://www.snowpure.com/docs/Electropure-EDI-Engr-OEM-Manual-v3.5.0-(CE)-A4.pdf (May 19, 2023).
  13. Park, S.K. (2021). THE SEOUL SHINMUN, https://www.seoul.co.kr/news/newsView.php?id=20210728022002 (May 19, 2023).
  14. Sheikholeslami, R., Al-Mutaz, I.S., Koo, T., and Young, A. (2001). Pretreatment and the effect of cations and anions on prevention of silica fouling, Desalination, 139, 83-95. https://doi.org/10.1016/S0011-9164(01)00297-1
  15. Song, J.H., Yeon, K.H., Kim, J.B., Cho, J.W., and Moon, S.H. (2002). A study on production of high purity water for a power plant using an RO-CEDI (Reverse osmosis-Continuous electroceionization), Theor. Appl. Chem. Eng., 8(2), 4189-4192.