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파일롯 플랜트 운전을 통한 고도정수처리공정의 최적화

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Author(s)
임형복
Issued Date
2018
Keyword
파일롯플랜트, 맛냄새물질, 고도정수처리공정
Abstract
The unpleasant taste and odor in the tap water cause various problems for both citizens and water supplier. These days, taste and odor problems are often reported in some water purification plants. Geosmin and 2-MID are known as the major taste and odor causing materials in water purification plants. There are many ways to remove these materials such as advanced oxidation process, activated carbon adsorption and its combination process. In order to apply such a process to water purification plants, pilot plant experiments must be carried out first. Dongbok-Ho is one of the water source of Gwangju city and has a possibility of taste and odor causing potential. Gwangju city plans to retrofit the conventional water purification system into a advanced water purification system in order to prepare for such taste and odor problems.
Ozone alone process, Ozone and hydrogen peroxide combination process, activated carbon adsorption process are considered as advanced water purification process. Pilot scale experiments were carried out to find the appropriate processes and to obtain the design and operation parameters. Ozone alone could remove 50% of geosmin. On the other hand, the combination of ozone and 3mg/L of hydrogen peroxide could remove 90% of geosmin and 90% of 2-MIB, simultaneously.
Residual ozone is harmful to citizens. Therefore, ozone quenching step is necessary after ozone oxidation process. Considering residual ozone and oxidation efficiency, the optimal ozone dosage is obtained as 0.3 to 2.0mg/L with the 15 minutes of contact time as the result of the experiments.
Manganese also threatened water quality. Very often, manganese concentration of the source water exceed 0.05mg/L but it reduced less than 0.0lmg/L by the conventional rapid sand filtration. However, 0.3mg/L of ozone could remove 60% more manganese.
Biological activated carbon(BAC) adsorption increased the removal rate of both turbidity and dissolved organic Carbon(DOC).
Alternative Title
Optimization of Advanced Water Treatment Process by Pilot Plant Operation
Alternative Author(s)
Im, Hyeong Bog
Affiliation
조선대학교 일반대학원
Department
일반대학원 토목공학과
Advisor
김성홍
Awarded Date
2018-08
Table Of Contents
ABSTRACT
제 1 장 서 론 1
1.1 연구배경 및 목적 1
1.2 연구내용 및 범위 3

제 2 장 이론적 고찰 4
2.1 오존에 의한 고도정수처리 4
2.1.1 개 요 4
2.1.2 오존처리 Mechanism 6
2.2 과산화수소()를 이용한 잔류오존 제거 10
2.2.1 과산화수소() 10
2.2.2 과산화수소를 이용한 오존 Quenching 11
2.3 고도산화공정(AOP)에 의한 고도정수처리 14
2.3.1 개 요 14
2.3.2 AOP 종류별 특징 15
2.4 활성탄(Activated Carbon)에 의한 고도정수처리 19
2.4.1 개 요 19
2.4.2 분말활성탄(Powdered Activated Carbon) 공정 21
2.4.3 입상활성탄(Granular Activated Carbon) 공정 22
2.4.4 입상활성탄(GAC) 공정 배열 25
2.4.5 생물활성탄(Biological Activated Carbon) 흡착공정 26
2.5 조류에 의한 맛․냄새 현황 29
2.5.1 기후변화와 조류발생 29
2.5.2 2-MIB와 Geosmin의 발생특성 31
2.5.3 2-MIB와 Geosmin의 발생사례 33
2.6 국내 고도정수처리시설 운영현황 35
2.7 중점 제거대상 물질 37

제 3 장 모형실험장치 및 방법 38
3.1 모형실험장치(Pilot Plant) 38
3.1.1 모형실험장치 구성 38
3.1.2 모형실험장치 원수 주입 38
3.1.3 모형실험장치 설치 39
3.2 실험방법 42
3.2.1 강제투입실험 42
3.2.2 연속모형실험 43
3.2.3 분석방법 43

제 4 장 연구결과 고찰 45
4.1 실험대상 정수장 유입수질 현황 45
4.2 강제투입실험 결과 47
4.2.1 1계열 모형실험 결과 47
4.2.2 2계열 모형실험 결과 49
4.2.3 과산화수소 AOP의 맛・냄새물질 강제투입실험 51
4.3 연속모형실험 결과 54
4.3.1 수질항목별 연속모형실험 결과 54
4.3.2 입상활성탄 흡착효율 변화 60
4.4 AOP 및 전 오존공정 적용성 62
4.4.1 AOP 도입 필요성 검토결과 62
4.4.2 전 오존공정 추가도입 필요성 검토결과 66

제 5 장 결 론 68
참고문헌 70
Degree
Doctor
Publisher
조선대학교 일반대학원
Citation
임형복. (2018). 파일롯 플랜트 운전을 통한 고도정수처리공정의 최적화.
Type
Dissertation
URI
https://oak.chosun.ac.kr/handle/2020.oak/13682
http://chosun.dcollection.net/common/orgView/200000267009
Appears in Collections:
General Graduate School > 4. Theses(Ph.D)
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