DOI QR코드

DOI QR Code

A study on breakthrough characteristics of ion exchange bed with H- and ETAH-form resins for cation exchange in NH3 and ETA solution including trace NaCl

미량의 NaCl을 포함하는 NH3 및 ETA 용액에서 H 및 ETAH 형 수지에 대한 이온교환 파과 특성 연구

  • Ahn, Hyun-Kyoung (Department of Energy & Environmental Engineering, Soonchunhyang University) ;
  • Kim, Youn-Su (Department of Energy & Environmental Engineering, Soonchunhyang University) ;
  • Park, Byung-Gi (Department of Energy & Environmental Engineering, Soonchunhyang University) ;
  • Rhee, In-Hyoung (Department of Energy & Environmental Engineering, Soonchunhyang University)
  • 안현경 (순천향대학교 에너지환경공학과) ;
  • 김윤수 (순천향대학교 에너지환경공학과) ;
  • 박병기 (순천향대학교 에너지환경공학과) ;
  • 이인형 (순천향대학교 에너지환경공학과)
  • Received : 2021.12.06
  • Accepted : 2021.12.15
  • Published : 2021.12.15

Abstract

Ion exchange (IX) performance on the exchanger bed is essentially evaluated for the generation of ultrapure water in electronics and chemical industries and for the corrosion control in nuclear power plants. The breakthrough characteristics of IX bed with multi-component were investigated with both cation- and mixed-IX beds of H- and ETAH-form for four kinds of cation exchange resins by using the combined solution of ethanolamine (ETA) and ammonia (NH3) at trace NaCl. Unlike major components (ETAH+ and NH4+ ), the phenomena of breakthrough and overshooting at bed outlet were not observed by Na+ over the test period (> 3 times theoretical exchange capacity of IX bed). The breakthrough from H-form resin bed was sequentially reached by ETAH+ and NH4+, while the overshooting was observed for ETAH+ at the breakthrough of NH4+. NH4+ was 51.5% higher than ETAH+ in terms of the relative selectivity determined with the width of breakthrough zone. At the increased concentration of Na+ at bed inlet, the selectivity and the overshooting were decreased and increased, respectively. Na+ leakage was higher from ETAH-form resin bed and was not identical for four kinds of cation-exchange resins, which may be reduced by improving the intrinsic property of IX resin.

전자 및 화학 산업의 초순수 생산 및 원자력 발전소의 부식 제어를 위해 이온교환 수지탑의 성능 파악이 필수적이다. 따라서 본 연구에서는 4종의 H 및 ETAH 형 양이온 교환수지가 채워진 양이온 및 혼상 이온교환수지탑에 미량의 NaCl를 포함하는 에탄올아민(ETA) 및 암모니아(NH3) 용액을 주입하여 양이온 파과특성을 조사하였다. 조사 결과, 주성분인 ETAH+ 및 NH4+와 달리, 미량성분인 Na+는 (이론적교환용량의 3배 이상) 시험기간 동안 수지탑 출구에서 파과 및 오버슈팅 현상이 나타나지 않았다. H형 수지탑의 파과현상은 ETAH+ 및 NH4+가 순서대로 일어났고, 오버슈팅은 NH4+가 파과할때 ETAH+에 대해서 발생했다. 파과영역의 너비로 결정되는 상대적 선택도는 NH4+가 ETAH+보다 최대 51.5 % 더 높았다. 유입수 Na+ 농도가 높을수록, 선택도는 감소하고 오버슈팅 현상은 증가하였다. 이온교환 수지의 고유 특성을 개선하여 감소시킬 수 있는 Na+ 누출은, ETAH형에서 높았고 4종의 양이온수지에 대해 동일하지 않은 것으로 조사되었다.

Keywords

Acknowledgement

This research was supported by Soonchunhyang University, Korea Hydro & Nuclear Power Central Research Institute (Grant No. L17S099001) and Korea Institute of Energy Technology Evaluation and Planning (Grant No. 20184030202130). The authors are thankful to Dr. Young-Jin Kim for providing the necessary advice.

References

  1. Alfredo, E.L. (1960). Diffusion in Ion-Exchange Resins, Ph.D. Thesis, Imperial College of Science and Technology, London, U.K.
  2. Ali, I. and Gupta, V.K. (2007). Advances in water treatment by adsorption technology, Nat. Protoc, 1, 2661-2667. https://doi.org/10.1038/nprot.2006.370
  3. ASTM. (2017). Standard Test Methods for Operating Performance of Particulate Cation-Exchange Materials1, ASTM D1782-17.
  4. ASTM. (2017). Standard Test Methods and Practices for Evaluating Physical and Chemical Properties of Particulate Ion-Exchange Resins1, ASTM D2187-17.
  5. Bashir, W., Tyrrell, E., Feeney, O. and Paull, B. (2002). Retention of alkali, alkaline earth and transition metals on an itaconic acid cation-exchange column Eluent pH, ionic strength and temperature effects upon selectivity, J. Chromatogr. A, 964, 113-112. https://doi.org/10.1016/S0021-9673(02)00652-0
  6. Boyd, G.E. and Lindenbaum, S. (1965). A thermodynamic calculation of the ionic strength dependence of ion-exchange reaction selectivity coefficients, J. Phys. Chem., 2378-2382.
  7. Calmon, C. (1986). Recent developments in water treatment by ion exchange, React. Polym. Ion Exch. Sorbents, 4, 2, 131-146. https://doi.org/10.1016/0167-6989(86)90008-5
  8. Carlos, I. Cabrera-Rodriguez, Carlos, M. Cartin-Caballero, Evgenia Platarou, Florence A. de Weerd, Luuk, A.M. van der Wielen, and Adrie J.J. Straathof. (2018). Recovery of acetate by anion exchange with consecutive CO2-expanded methanol desorption: A model-based approach, Sep. Purif. Technol., 203, 56-65. https://doi.org/10.1016/j.seppur.2018.03.068
  9. Dupont., Resource Center, Ion Exchange Resin Product Data Sheet (2021). https://www.dupont.com/resource-center.html?BU=water-solutions&tagId=DuPont:pcg/ion_exchange_resins (Novemver 1, 2021).
  10. Fukumura T. and Arioka K., (2009). "Influence of ETA Injection on Flow Accelerated Corrosion of PWR Secondary System", Proceedings of NACE Corrosion 2009 international Conference & Expo, 22-26 March, 2009, Atlanta, Georgia, NACE.
  11. Ivona Nui'c, Marina Trgo, Nediljka Vukojevi'c Medvidovi'c and Marin Ugrina. (2019). A Mass Transfer Analysis of Competitive Binding of Pb, Cd, and Zn from Binary Systems onto a Fixed Zeolite Bed, Int. J. Environ. Res. Public Health, 16(3), 426. https://doi.org/10.3390/ijerph16030426
  12. Marks, C. (2010). "Amine Effect on Corrosion Product Transports and Steam Generator Fouling", Proceedings of Steam Generator Management Program 2010 Steam Generator Secondary Side Management Conference, 2-4 March, 2010, EPRI.
  13. Mark E.D. and Robert J.D. (2003). Fundamentals of Chemical Reaction Engineering. McGraw-Hill, New York. 384.
  14. Reinhard, F.P. (1993). "Utilization and Practical Application of Ion Exchange, A critical Review", Proceedings of 14th Annual AESF/EPA Conference on Environmental Control for the Surface Finishing Industry, 1993, Orlando, Florida, EPA.
  15. Rhee, I.H. and Dzombak, D.A. (1999). Binary and Ternary Cation Exchange on Strong Acid Cation Exchange Resin Involving Na, Mg, and Zn in Single and Binary Backgrounds of Chloride, Perchlorate, and Sulfate, Langmuir, 15, 6875-6883. https://doi.org/10.1021/la970031g
  16. Salem, B.S., Asli, A.S. and Ahmet, O. (2007). Fixed-bed ion exchange columns operating under non-equilibrium conditions: Estimation of mass transfer properties via non-equilibrium modeling, React. Funct. Polym., 67, 12, 1540-1547. https://doi.org/10.1016/j.reactfunctpolym.2007.07.040
  17. Stanley, M.W., James, R.C., Penney, W.R. and James, R.F. (2010). Chemical Process Equipment (Revised Second Edition): Selection and Design. Gulf Professional Pub, 840.
  18. Sudhir, K.P. (1992). Mixed Bed Ion-Exchange Modeling for Divalent Ions in a Ternary System, Ph.D. Thesis, Andhra University, Visakhapatnam, AP, India.
  19. Valentina, A.N. (2012). About Mathematical Modeling and Calculation of Dynamic Ion- Exchange Processes on Natural Zeolites. Handbook of Natural Zeolites. Bentham Science Pub, 750.
  20. Woodard, F. and Curran, I. (2005). Industrial Waste Treatment Handbook 2nd Edition. Butterworth-Heinemann, 532.
  21. Yi, J. and Gary, L.F. (2004). True multi-component mixed-bed ion-exchange modeling, React. Funct. Polym., 60, 121-135. https://doi.org/10.1016/j.reactfunctpolym.2004.02.017