Journal of Korean Society of Water and Wastewater (상하수도학회지)

The Korean Society of Water and Wastewater (대한상하수도학회)
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The design parameter evaluation of ion exchange process for ultra pure water production

초순수 생산을 위한 이온교환공정 설계특성 평가

  • Received : 2014.12.04
  • Accepted : 2015.02.06
  • Published : 2015.02.15
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Abstract

In this study, cation and anion exchange process for performance evaluation was conducted. A pilot plant for the ultrpure water production was installed with the capacity of $25m^3/d$. The various production rate and regeneration of ion exchange rate were tested to investigate the design parameters. The test resulst was applied to calculate the operating costs. Changing the flow rate of the ion exchange capacity of the reproduction reviewed the cation exchange process as opposed to the design value is 120 to 164% efficiency, whereas both anion exchange process is 82 to 124% efficiency, respectively. This results can be applied for more large scale plant if the scale up parameters are consdiered. The ion exchange capacity of the application in accordance with the design value characteristic upon application equipment is expected to be needed. In this study, the performance of cation and anion exchange resin process was evaluated with pilot plant($25m^3/d$). The ion exchange capacity along with space velocity and regeneration volume was evaluated. In results, the operation results was compared with design parameters.

Keywords

References

  1. Choi, Byeong-Seup (2013), Issue Report of Ultrapure Water Industry and Technology Trends, Korea Agency for Infrastructure Technology Advancement, 2013, 1-16
  2. David, K., Brad, M., Michael, B. and Rick L. (2009) Inovations In Ion Exchange Technology For The Removal of Sulfate, Ultra Pure Water Journal Sept 2009, Vol. 29, No. 9, pp. 21-28
  3. David, K., David, S., Songlin Y., and Teryl M. (2010) Innovative IX Systems For Cost-Effective Increase In Water Reuse In Power Plants, Ultra Pure Water Journal Sep 2010, Vol. 27, No. 9, pp. 20-27
  4. GWI (2010) Global Water Market2011, GWI, Oxford, UK, 2010
  5. K-water (2007), Industrial Water Research of Pure and Ultrapure Water, 2007
  6. K-water (2010(a)), Market Analysis and Efficiency Supply of Industrial Water, 2010
  7. K-water (2010(b)), Understanding of Ultrapure Water Technology,, 2010.12
  8. K-water (2011), The research of Based on Technology for Pure and Ultrapure water treatment plant, 2011.11
  9. Motomura, Y. (1990) Science of Ultrapure water(The Science of Ultrapure water), Research of Based technology for the semiconductor, Realize, Tokyo Japan. 1990
  10. Shaoying, Q., Lance, C. S., and Treavor, H. B. (2012) Determining Minimum Ion Exchange Resin Usage for NOM Removal, Journal of Environmental Engineering Oct 2012, Vol. 138, No. 10, pp. 1058-1066 https://doi.org/10.1061/(ASCE)EE.1943-7870.0000569
  11. Ted, C., Kevin, H. and Paul, T. (2009) A Why to Optimize Cation/Anion Resin Replacement Frequency, Ultra Pure Water Journal Opt 2008, Vol. 25, No. 7, pp. 24-
  12. Yabe, K., Motomura, Y., Mizuniwa, T. (2004) Pure and Ultrapure water Technology, Japanese Industrial Standards Committee (JISC),, Tokyo Japan, 2004
  13. Yoshimura, F., Kitagawa, M.(2003) Design of Water Treatment, Japanese Industrial Standards Committee(JISC), Tokyo Japan, 2003
  14. Yoshimura, F. (2002) Technology of Water Treatment, Japanese Industrial Standards Committee(JISC), Tokyo Japan, 2002

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