하수슬러지를 이용한 생물담체의 개발 및 적용
- Alternative Title
- Development and application of biomedia using the waste sewage sludge
- Abstract
- To present new way of sewage sludge recycling method, feasibility of making and using porous biological support media was investigated. Porous biological support media was made of sludge cake from sewage treatment plant and loess, clay. They were mixed in varying ratio and burnt in high temperature to ensure sufficient mechanical strength. The results obtained from experiments were summarized as follows :
1. It was evaluated that optimum mixing ratio of sewage sludge cake, loess and clay was 75 : 10 : 15 and optimum burning temperature was 950 ℃. Compressive strength, void ratio, water absolute and specific surface area were 39.36 ㎏/㎠, 66.3 %, 51.7 % and 8.364 ㎡/g, respectively.
2. It was calculated that about 2.3 ton of sludge cake can be used to produce 1 m3 of biological support media. In other words, 2.1 m3 of sludge can be consumed for producing 1 m3 of biological support media when considering specific gravity of sludge as 1.1
3. It can be evaluated that maximum microbial retain capacity of biological support media was 20 ㎎ of microorganism/g of support media and maximum MLSS concentration of reactor was about 10,000 ㎎/ℓ. Successful formation of biofilm on support media was observed through scanning electronic microscope.
4. Biological support media prepared in this experiments were applied as packing material in intermittently aerated biofilm process and feasibility of simultaneous removal of organic and nitrogen was evaluated. It was evaluated that optimum oxic/anoxic time ratio was 40 min/80 min under the operating conditions of 0.804 g COD/day and 0.174 g NH4+-N/day. COD and nitrogen removal efficiencies were 96 % and 72 %, respectively.
5. Pilot scale experiment was conducted using biological support media made in this experiment to testify the feasibility of applying this system as water reusing process by treating effluent of sewage treatment plant. Optimum surface filtrating velocity and surface organic loading rate were 7~13 ㎥/㎡-hr and 1.95 g BOD/㎡/day, respectively. It can be evaluated that effluent from sewage treatment plant can be treated successfully as reusing purpose if the height of packed bed is maintained higher than 1.0 m and applied surface organic loading rate is maintained lower than 2.0 g BOD/㎡-day.
6. Waste sludge from sewage treatment plant can be reused successfully by applying it as raw material of porous biological support media made of sludge cake, loess and clay. It can be concluded that porous biological support media prepared in this experiment can be applied wastewater treatment plant as promising packing material.
- Author(s)
- 정수일
- Issued Date
- 2007
- Awarded Date
- 2007. 8
- Type
- Dissertation
- Keyword
- 하수슬러지 생물담체 생물막 생물학적 질소 질산화
- Publisher
- 부경대학교 대학원
- URI
- https://repository.pknu.ac.kr:8443/handle/2021.oak/3938
http://pknu.dcollection.net/jsp/common/DcLoOrgPer.jsp?sItemId=000001953910
- Alternative Author(s)
- Jeong, Soo-Il
- Affiliation
- 부경대학교 대학원
- Department
- 대학원 토목공학과
- Advisor
- 손인식
- Table Of Contents
- 제 1 장 서론 = 1
1.1 연구배경 = 1
1.2 연구목적 = 3
제 2 장 문헌연구 = 4
2.1 담체의 물리·화학적 특성이 생물막 형성에 미치는 영향 = 4
2.1.1 생물막 담체 필요조건 = 6
2.1.2 생물막 담체로 사용되는 물질 = 6
2.1.3 생물막 담체의 물리적 특성 = 7
2.1.4 생물막 담체의 화학적 특성 = 12
2.1.5 담체표면의 개질 = 16
2.1.6 요약 = 17
2.2 하수슬러지의 발생 및 처리현황 = 19
2.2.1 이론적인 하수슬러지의 원단위 발생량 = 19
2.2.2 실제 하수처리장의 발생량 = 20
2.2.3 하수슬러지의 처리현황 = 25
2.3 생물막 공정 = 29
2.4 생물학적 질소제거 = 30
2.4.1 질산화(nitrification) = 30
2.4.2 탈질(denitrification) = 32
2.5 간헐폭기법(Intermittent aeration system) = 36
제 3 장 재료 및 실험방법 = 42
3.1 생물담체 제조 = 42
3.1.1 원료의 화학조성 분석 = 42
3.1.2 생물담체 제조 및 물성분석 = 42
3.2 미생물 부착 특성 실험 = 45
3.2.1 실험장치 = 45
3.2.2 담체 충진 및 미생물 부착 = 46
3.3 생물담체의 성능평가 = 47
3.3.1 간헐폭기 운전방법 = 47
3.3.2 분석방법 = 49
3.4 현장 적용 실험 = 50
3.4.1 실험장치 = 50
3.4.2 실험방법 = 51
3.4.3 분석방법 = 51
제 4 장 결과 및 고찰 = 52
4.1 생물담체 제조 재료의 화학조성 = 52
4.2 생물담체 제조 = 54
4.2.1 황토 혼합비 결정 = 54
4.2.2 황토 및 점토 혼합비 결정 = 62
4.2.3 소성온도의 결정 = 70
4.2.4 제조된 담체의 물성 및 총괄 = 77
4.3 미생물 부착 특성 = 80
4.3.1 미생물고정화 능력 = 80
4.3.2 미생물탈리현상 = 83
4.4 유기물질 및 질소제거 성능 = 86
4.4.1 COD제거 = 88
4.4.2 NH^(+)₄-N제거율 = 90
4.4.3 T-N제거율 = 92
4.5 현장 적용 사례 = 97
4.5.1 유기물 부하에 따른 처리 특성 = 97
4.5.2 표면 여과속도에 따른 처리 특성 = 100
4.5.3 생물 담체 충진층 높이에 다른 처리 특성 = 103
제 5 장 결론 = 107
참고문헌 = 109
- Degree
- Doctor
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