국문목차
표제지=0,1,4
목차=i,5,2
List of Tables=iii,7,1
List of Figures=iv,8,4
Abstract=viii,12,1
I. 서론=1,13,3
II. 이론적 배경=4,16,1
1. 광촉매 반응(Photocatalytic reaction)=4,16,1
1) 광촉매(Phtocatalyst)=4,16,3
2) 광촉매 반응(Photocatalytic reaction)=6,18,5
3) 광촉매의 고정화 기술=10,22,2
4) 광촉매의 연구 동향=12,24,2
2. 이ㆍ취미 물질=14,26,1
1) 이ㆍ취미 유발물질의 종류 및 특성=14,26,4
2) Geosmin=18,30,1
3) 2-MIB=18,30,1
III. 재료 및 방법=19,31,1
1. TiO2의 입상 활성탄 고정화=19,31,5
2. 광촉매를 고정화한 활성탄을 이용한 유해화합물의 기초분해 실험=23,35,3
3. 활성탄 유동층 수처리 장치=26,38,1
1) 활성탄 유동층 수처리장치의 개요=26,38,11
2) 15톤/일 처리규모 및 30톤/일 처리규모 활성탄 유동층 수처리장치 제작=37,49,1
IV. 결과 및 고찰=38,50,1
1. 광촉매를 고정화한 활성탄을 이용한 이ㆍ취미 물질의 분해실험=38,50,1
1) Geosmin의 분해=38,50,3
2) 2-MIB의 분해=41,53,3
2. 활성탄 유동층 수처리장치를 이용한 이ㆍ취미 물질의 분해=44,56,13
V. 결론=57,69,1
VI. 참고문헌=58,70,4
감사의 글=62,74,1
Table1. Major quantum efficiency(ф) of the product in accordance with the investigation of semiconductor materials=6,18,1
Table2. Properties of odorous compounds by biomass=15,27,1
Table3. Odorous compounds associated with representative algae=16,28,1
Table4. Critical concentration of algae that produce odorous metabolites=17,29,1
Fig1. Formation of radicals and reaction mechanism of Tio₂=8,20,1
Fig2. SEM photograph of fiuidized with Tio₂-coated activated carbon=20,32,1
Fig3. TEM photograph of fiuidized with Tio₂-coated activated carbon=21,33,1
Fig4. Schematics of the reactor=24,36,1
Fig5. Emission spectrum of Black light lamp=25,37,1
Fig6. Emission spectrum of Low pressure mercury lamp=25,37,1
Fig7. Systematics of the continuous flow fluidized bed water treatment equipment=27,39,1
Fig8. Details of fluidized bed water=29,41,1
Fig9. The plane figure of the section D(33:lamp)=30,42,1
Fig10. Vltraviolet lamp at the section D=31,43,1
Fig11. Strainer sheets installed at the section D(35:스트레이너 판, 351:스트레이너)=32,44,1
Fig12. The pilot scale, fluidized bedwater treatment equipment with activated carbon, designed by this investigation=33,45,1
Fig13. Enfire figure of fluidized bed water treatment equipment=34,46,1
Fig14. The core fluidized photocatalytic reactors with activated corbon of confinnous fluidized bed water freatment equipment=35,47,1
Fig15. The figure of fluidized photocatalyfic reactors with ultraviolet lamp installed inside=36,48,1
Fig16. The change of Goesmin's density according to existence of GAC or vltraviolet(Black light lamp)=39,51,1
Fig17. The removal efficiency of Goesmin according to existence of vltraviolet(Black light lamp) on GAC-Ti=39,51,1
Fig18. The change of Goesmin's density according to existence of GAC or vltraviolet(Low pressure mercury lamp)=40,52,1
Fig19. The removal efficiency of Goesmin according to existence of vltraviolet(Low pressure mercury lamp) on GAC-Ti=40,52,1
Fig20. The change of 2-MIB's density according to existence of GAC or vltraviolet(Black light lamp)=42,54,1
Fig21. The removal efficiency of 2-MIB according to existence of vltraviolet(Black light lamp) on GAC-Ti=42,54,1
Fig22. The change of 2-MIB's density according to existence of GAC or vltraviolet(Low pressure mercury lamp)=43,55,1
Fig23. The removal efficiency of 2-MIB according to existence of vltraviolet(Low pressure mercury lamp) on GAC-Ti=43,55,1
Fig24. The removal efficiency of 2-MIB by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 156㎤/sec, Low pressure mercury lamp)=45,57,1
Fig25. The removal efficiency of 2-MIB by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 156㎤/sec, Low pressure mercury lamp)=45,57,1
Fig26. The removal efficiency of 2-MIB by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 185㎤/sec, Low pressure mercury lamp)=46,58,1
Fig27. The removal efficiency of 2-MIB by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 185㎤/sec, Low pressure mercury lamp)=46,58,1
Fig28. The removal efficiency of 2-MIB by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 198㎤/sec, Low pressure mercury lamp)=47,59,1
Fig29. The removal efficiency of 2-MIB by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 198㎤/sec, Low pressure mercury lamp)=47,59,1
Fig30. The removal efficiency of 2-MIB by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 283㎤/sec, Low pressure mercury lamp)=48,60,1
Fig31. The removal efficiency of 2-MIB by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 283㎤/sec, Low pressure mercury lamp)=48,60,1
Fig32. The removal efficiency of 2-MIB by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 315㎤/sec, Low pressure mercury lamp)=49,61,1
Fig33. The removal efficiency of 2-MIB by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 315㎤/sec, Low pressure mercury lamp)=49,61,1
Fig34. The removal efficiency of 2-MIB by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 332㎤/sec, Low pressure mercury lamp)=50,62,1
Fig35. The removal efficiency of 2-MIB by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 332㎤/sec, Low pressure mercury lamp)=50,62,1
Fig36. The removal efficiency of Goesmin by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 156㎤/sec, Low pressure mercury lamp)=51,63,1
Fig37. The removal efficiency of Goesmin by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 156㎤/sec, Low pressure mercury lamp)=51,63,1
Fig38. The removal efficiency of Goesmin by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 185㎤/sec, Low pressure mercury lamp)=52,64,1
Fig39. The removal efficiency of Goesmin by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 185㎤/sec, Low pressure mercury lamp)=52,64,1
Fig40. The removal efficiency of Goesmin by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 198㎤/sec, Low pressure mercury lamp)=53,65,1
Fig41. The removal efficiency of Goesmin by use of 15㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 198㎤/sec, Low pressure mercury lamp)=53,65,1
Fig42. The removal efficiency of Goesmin by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 283㎤/sec, Low pressure mercury lamp)=54,66,1
Fig43. The removal efficiency of Goesmin by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 283㎤/sec, Low pressure mercury lamp)=54,66,1
Fig44. The removal efficiency of Goesmin by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 315㎤/sec, Low pressure mercury lamp)=55,67,1
Fig45. The removal efficiency of Goesmin by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 315㎤/sec, Low pressure mercury lamp)=55,67,1
Fig46. The removal efficiency of Goesmin by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC, 332㎤/sec, Low pressure mercury lamp)=56,68,1
Fig47. The removal efficiency of Goesmin by use of 30㎥/day capacity equipment with Tio₂-coated activated carbon(GAC-Ti, 332㎤/sec, Low pressure mercury lamp)=56,68,1