국문목차
표제지=0,1,3
목차=i,4,2
List of Tables=iii,6,1
List of Figures=iv,7,3
Abstract=vii,10,2
I. 서론=1,12,3
II. 이론적 배경=4,15,1
1. 광촉매(Photocatalyst)=4,15,4
2. 광촉매 반응(Photocatalytic reaction)=7,18,1
1) 광촉매 산화반응의 원리=7,18,4
2) 활성탄에 담지된 TiO₂촉매상에서의 광촉매 반응 원리=10,21,2
3) 광촉매의 고정화 기술=11,22,3
4) 광촉매의 연구동향=13,24,2
3. 남조류=15,26,1
1) 남조류의 특성=15,26,4
2) 독소물질과 Microcystin-LR=18,29,6
III. 재료 및 방법=24,35,1
1. TiO₂의 입상활성탄 고정화=24,35,5
2. 광촉매가 고정화된 활성탄을 이용한 회분식 반응기 기초분해실험=28,39,3
3. 유동층 반응기의 설계=31,42,1
1) 유동화 실험=31,42,2
2) 15톤/일 처리규모 활성탄 유동층 수처리 설비 설계인자의 산출=33,44,1
3) 30톤/일 처리규모 활성탄 유동층 수처리 설비 설계인자의 산출=34,45,4
IV. 결과 및 고찰=38,49,1
1. Microcystin-LR의 회분식 반응기 분해실험=38,49,1
1) Black light 램프(4-Watt)를 이용한 분해실험=38,49,3
2) 저압수은램프(15-Watt)를 이용한 분해실험=41,52,2
2. 연속 유동층 수처리 장치를 이용한 Microcystin-LR의 제거=43,54,7
V. 결론=50,61,1
VI. 참고문헌=51,62,6
감사의 글=57,68,2
Table1. Toxigenic cyanobacteria species and toxin material=19,30,1
Table2. Toxin material and their effect produced by cyanobacteria=20,31,1
Table3. Toxigenic cyanobacteria species discovered in the Korea=20,31,1
Table4. A species of Microcystin=23,34,1
Fig.1. Crystalization structure of Anatase and Rutile=6,17,1
Fig.2. Formation of radicals and reaction mechanism of TiO₂=8,19,1
Fig.3. General structure of cyanobacteria=15,26,1
Fig.4. Chemical structure of Microcystin=22,33,1
Fig.5. Scanning electron microscope picture of activated carbon fill TiO₂=25,36,1
Fig.6. Transmission electron microscope picture of activated carbon fill TiO₂=26,37,1
Fig.7. Schematics of the reactor=29,40,1
Fig.8. Wave special quality of Black light lamp=30,41,1
Fig.9. Wave special quality of low pressure mercury lamp=30,41,1
Fig.10. Schematics of fluidization experiment equipment=31,42,1
Fig.11. Fluidization experiment result by the fluidization speed velocity=32,43,1
Fig.12. The diagram of activated carbon fluidized bed water treatment equipment=35,46,1
Fig.13. The detail drawing of fluidized bed reactor=36,47,1
Fig.14. The detail drawing of fluidized bed water treatment equipment=37,48,1
Fig.15. Concentration change of Microcystin-LR by existence and non existence of granular activated carbon or ultraviolet rays(black light lamp)=38,49,1
Fig.16. Microcystin-LR removal efficiency by existence and non existence of ultraviolet rays(black light lmap) in GAC-Ti(granular activated carbon-Ti)=39,50,1
Fig.17. Effect of ultraviolet irradiation in microcystin-LR removal=40,51,1
Fig.18. Concentration change of microcystin-LR by existence and non existence of granular activated carbon or ultraviolet rays(low pressure mercury lamp)=41,52,1
Fig.19. Microcystin-LR removal efticiency by existence and non existence of ultraviolet rays(low pressure mercury lamp) in GAC-Ti.(granular activated carbon-Ti)=42,53,1
Fig.20. Microcystin-LR removal efficiency change that use 15 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC, processing velocity of flow : 155㎤/sec, black light lamp)=44,55,1
Fig.21. Microcystin-LR removal efficiency change that use 15 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC-Ti, processing velocity of flow : 155㎤/sec, black light lamp)=44,55,1
Fig.22. Microcystin-LR removal efficiency change that use 15 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC, processing velocity of flow : 184㎤/sec, black light lamp)=45,56,1
Fig.23. Microcystin-LR removal efficiency change that use 15 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC-Ti, processing velocity of flow : 184㎤/sec, black light lamp)=45,56,1
Fig.24. Microcystin-LR removal efficiency change that use 15 tons/day processing scsle activated carbon fluided bed water treatment equipment(GAC, processing velocity of flow : 199㎤/sec, black light lamp)=46,57,1
Fig.25. Microcystin-LR removal efficiency change that use 15 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC-Ti, processing velocity of flow : 199㎤/sec, black light lamp)=46,57,1
Fig.26. Microcystin-LR removal efficiency change that use 30 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC, processing velocity of flow : 283㎤/sec, black light lamp)=47,58,1
Fig.27. Microcystin-LR removal efficiency change that use 30 tons/day processing scale activated carbon fluided bed water treatment eguipment(GAC-Ti, processing velocity of flow : 283㎤/sec, black light lamp)=47,58,1
Fig.28. Microcystin-LR removal efficiency change that use 30 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC, processing velocity of flow : 315㎤/sec, black light lamp)=48,59,1
Fig.29. Microcystin-LR removal efficiency change that use 30 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC-Ti, processing velocity of flow : 315㎤/sec, black light lamp)=48,59,1
Fig.30. Microcystin-LR removal efficiency change that use 30 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC, processing velocity of flow : 332㎤/sec, black light lamp)=49,60,1
Fig.31. Microcystin-LR removal efficiency change that use 30 tons/day processing scale activated carbon fluided bed water treatment equipment(GAC-Ti, processing velocity of flow : 332㎤/sec, black light lamp)=49,60,1