Hybrid Water Treatment of Photocatalyst Coated Polypropylene Beads and Ceramic Membranes: Effect of Membrane and Water Back-flushing Period

광촉매 코팅 폴리프로필렌 구와 세라믹 분리막의 혼성수처리: 분리막과 물 역세척 주기의 영향

  • Park, Jin Yong (Department of Environmental Sciences & Biotechnology, Hallym University) ;
  • Hwang, Jung Hye (Department of Environmental Sciences & Biotechnology, Hallym University)
  • 박진용 (한림대학교 환경생명공학과) ;
  • 황정혜 (한림대학교 환경생명공학과)
  • Received : 2013.05.31
  • Accepted : 2013.06.13
  • Published : 2013.06.30

Abstract

Effect of water back-flushing period (FT) was investigated in hybrid water treatment process of carbon ultrafiltration and polypropylene (PP) beads coated with photocatalyst, and membrane effect was studied by comparing the previous studies with carbon microfiltration or alumina ultrafiltration, microfiltration membranes. FT 6 min was the most effective to control initial membrane fouling and optimal condition because the membrane fouling resistance was low until initial 60 min and the maximum total permeate volume was acquired at this FT. The turbidity treatment efficiency was high beyond 98.6%, and did not depend on FT, which was same with the previous result of carbon or alumina microfiltration. The organic matters treatment efficiency was the highest value of 98.2% at FT 6 min, which was almost same trend with the previous result of alumina microfiltration. Then the organic matters treatment efficiency of carbon microfiltration was the minimum at no back-flushing (NBF) and increased as decreasing FT, but that of alumina ultrafiltration was the maximum at NBF and also increased as decreasing FT. Therefore it means that water back-flushing effect on the organic matters treatment efficiency had a different mechanism depending on pore size in spite of the same material membranes.

탄소 한외여과 및 광촉매 코팅 폴리프로필렌(PP) 구의 혼성수처리 공정에서 물 역세척 주기(FT)의 영향을 알아보고, 탄소 정밀여과막 또는 알루미나 한외여과막 및 정밀여과막을 사용한 기존 결과들과 비교하여 분리막의 영향을 고찰하였다. FT 6분일 때 초기 60분까지 최소 막오염 저항을 보이고 최대 총여과부피를 얻어서, FT 6분이 초기 막오염의 억제에 가장 효과적이고 최적 조건이다. 탁도의 처리효율은 98.6% 이상이며 FT 변화의 영향이 보이지 않았는데, 탄소 또는 알루미나 정밀여과막을 사용한 기존 연구와 일치하는 것이다. 유기물의 처리효율은 FT 6분에서 98.2%로 최대값을 보였는데, 알루미나 정밀여과막의 결과와 유사하다. 반면에 탄소 정밀여과막에서는 유기물의 처리효율이 비역세척(NBF)에서 최소이고 FT가 감소할수록 증가하였으나, 알루미나 한외여과막에서는 NBF에서 최대이고 FT가 감소할수록 역시 증가하였다. 따라서 유기물 처리효율에 대한 물 역세척 주기의 영향은 동일한 재질의 분리막이라도 기공 크기에 따라 다른 기작을 보인다는 것을 알 수 있었다.

Keywords

References

  1. H. Zhang, X. Quan, S. Chen, H. Zhao, and Y. Zhao, "Fabrication of photocatalytic membrane and evaluation its efficiency in removal of organic pollutants from water", Sep. Pur. Tech., 50, 147 (2006). https://doi.org/10.1016/j.seppur.2005.11.018
  2. H. Yamashita, H. Nakao, M. Takeuchi, Y. Nakatani, and M. Anpo, "Coating of TiO2 photocatalysts on super-hydrophobic porous teflon membrane by an ion assisted deposition method and their self-cleaning performanc", Nucl. Instr. Meth. Phys. Res., 206, 898 (2003). https://doi.org/10.1016/S0168-583X(03)00895-4
  3. K. W. Park, K. H. Choo, and M. H. Kim, "Use of a combined photocatalysis/microfiltration system for natural organic matter removal", Membrane Journal, 14, 149 (2004).
  4. H. C. Oh, "Photocatalytic degradation characteristics of organic matter by highly pure $TiO_{2}$ nanocrystals", Master Dissertation, Kangwon National Univ., Chuncheon, Korea (2006).
  5. J. U. Kim, "A study on drinking water treatment by using ceramic membrane filtration", Master Dissertation, Yeungnam Univ., Daegu, Korea (2004).
  6. C. K. Choi, "Membrane technology", Chem. Ind. & Tech., 3, 264 (1985).
  7. I. R. Bellobono, B. Barni and F. Gianturco, "Preindustrial experience in advanced oxidation and integral photodegradation of organics in potable waters and wastewaters by PHOTOPERMTM membranes immobilizing titanium dioxide and promoting photocatalysts", J. Membr. Sci., 102, 139 (1995). https://doi.org/10.1016/0376-7388(94)00273-2
  8. R. Molinari, C. Grande, E. Driloli, L. Palmisano, and M. Schiavello, "Photocatalytic membrane reactors for degradation of organic pollutants in water", Cata. Today, 37, 273 (2001).
  9. R. Molinari, F. Pirillo, M. Falco, V. Loddo, and L. Palmisano, "Photocatalytic degradation of dyes by using a membrane reactor", Chem. Eng. Proc., 43, 1103 (2004). https://doi.org/10.1016/j.cep.2004.01.008
  10. K. Azrague, E. Puech-Costes, P. Aimar, M. T. Maurette, and F. Benoit-Marquie, "Membrane photoreactor (MPR) for the mineralisation of organic pollutants from turbid effluents", J. Membr. Sci., 258, 71 (2005). https://doi.org/10.1016/j.memsci.2005.02.027
  11. M. Pidou, S. A. Parsons, G. Raymond, P. Jeffery, T. Stephenson, and B. Jefferson, "Fouling control of a membrane coupled photocatalytic process treating greywater", Wat. Res., 43, 3932 (2009). https://doi.org/10.1016/j.watres.2009.05.030
  12. G. S. Cong and J. Y. Park, "Advanced water treatment of high turbidity source by hybrid process of ceramic ultrafiltration and photocatalyst: 1. effects of photocatalyst and water-back-flushing condition", Membrane Journal, 21, 127 (2011).
  13. G. S. Cong and J. Y. Park, "Advanced water treatment of high turbidity source by hybrid process of ceramic ultrafiltration and photocatalyst: 2. effect of photo-oxidation and adsorption", Membrane Journal, 21, 201 (2011).
  14. J. Y. Park and G. S. Lee, "Advanced water treatment of high turbidity source by hybrid process of ceramic microfiltration: effect of organic materials in water-back-flushing", Membrane Journal, 21, 72 (2011).
  15. J. Y. Park and G. H. Cho, "Effect of water backflushing condition in hybrid water treatment process of carbon fiber microfiltration membrane and photocatalyst", Membrane Journal, 22, 216 (2012).
  16. J. Y. Park and S. W. Park, "Advanced water treatment of high turbidity source by hybrid process of photocatalyst and ceramic microfiltration: effect of water back-flushing period", Membrane Journal, 22, 243 (2012).
  17. D.-J. Kim, J.-Y. Kang, and K.-S. Kim, "Preparation of $TiO_{2}$ thin films on glass beads by a rotating plasma reactor", J. Ind. & Eng. Chem., 16, 997 (2010). https://doi.org/10.1016/j.jiec.2010.07.005
  18. H. C. Lee and J. Y. Park, "Advanced water treatment of high turbidity source by hybrid process of ceramic microfiltration and activated carbon adsorption: effect of GAC packing fraction", Membrane Journal, 18, 191 (2008).