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동전기와 생물학적 복원방법을 혼용한 토양 중의 styrene 정화

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Alternative Title
Combined process of electrokinetic and biological remediation technologies on styrene-contaminated Soil
Abstract
Up to recently, many researchers showed that the bioremediaton methods adopted to the soil contaminated by diverse organic compounds have excellent efficiencies and also, several of them adopted electrokinetic treatment methods to the heterogeneous and/or low-permeable soil media. They concluded that the electrokinetic treatment raises the temperature of the media(soil) and this could affect the conductivity, ion mobility, electric osmosis and adsorption reactions in the electrokinetic processes.
Styrene, the target material of this paper, is one of the major raw material in the petroleum refinery industries. And so, the petrochemical complex may have the intrinsic hazard of the soil contamination by this compound. The specific circumstance might force the industry complex employ the in-situ treatment method.
In this study, to treat the styrene contaminated soil, we introduced the bioremediation method utilizing the endogenous microbes and the electrokinetic process enhancing the mobility of microbes in the process. Lastly, we combined the two processes and tested the electrokinetic bioremediation method.
Consequently, to treat the styrene contaminated soils of petrochemical complex, we adopted electrokinetic bioremediation method utilizing endogenous microbes. We concluded as follows;
We employ the purge&trap-GC/FID method to quantify the styrene in the soil. The recovery, relative standard deviation, and detection limit of the method is 9.61~116.4%, 1.15~6.14(less 10%), and 0.6㎍/㎏( 99%). Styrene consumable microbes are identified as gram-positive Entrococcus faecium. These microbes proliferated at 25℃(15~25℃), pH of 9.0~9.8(pH of 6.8~10) and 0.05% of substrate(styrene) concentration.
In electrokinetic bioremediation combined process, the temperatures of each process tended to increase with the supply of electric current(2.5~1.0mA or 0.16~0.63mA/㎠), and this thaught to be the adiabatic character of the media(soil).
The microorganism culture fluid of the process seemed to raised the pH than the electrokinetic single process, but additional increase of pH, like supplement of appropriate electrolyte, needed to achieve the optimum biological condition.
Electric voltage of the process showed decreasing with time because of the circulation of microorganism culture fluid. Lower voltage in constant current system meas the cut down of the operation cost(decrease of electric power). The accumulated electroosmotic flow was a little decreased, and showed good correlation with the electric current(R2=0.9818). The mobility of the contaminant(s), including electrolyte, was improved with the electric current.
As the microbes traveled to anode by electrophoresis and electroosmosis, almost no microbes were detected in the cathode sector of the process. But, the microbes were abundant in the anode and intermediate sectors.
The mean removal efficiencies was 42.8%, 54.5%, and 75.0% at the electric current of 2.5mA, 5mA, and 10mA, respectively and the removal efficiency showed good correlation with electric current(R2=0.9996). In comparison with bioremediation single process, the mean removal efficiencies was 120%, 140%, and 190% at the electric current of 2.5mA, 5mA, and 10mA, respectively. And in comparison with electorkinetic single process, the mean removal efficiencies was 148%, 710%, and 250% at the electric current of 2.5mA, 5mA, and 10mA, respectively.
In summary, electorkinetic process using circulating endogenous microbes thought to be suitable to the treatment of styrene contaminated soil, but long-term treatment time needed to achieve the foreign purification criteria of 50㎎/㎏. In the treatment of biologically recalcitrant contaminants, the stable optimum pH condition adjustment seemed to be the major design parameter, the further research ought to be concentrated at proper pH adjustment, which might enhance the activation of microbes.
Author(s)
이정만
Issued Date
2007
Awarded Date
2007. 8
Type
Dissertation
Keyword
생물학적복원 토양 styrene 동전기 미생물 배양액
Publisher
부경대학교 대학원
URI
https://repository.pknu.ac.kr:8443/handle/2021.oak/3800
http://pknu.dcollection.net/jsp/common/DcLoOrgPer.jsp?sItemId=000001953752
Alternative Author(s)
Lee, Joung-Man
Affiliation
부경대학교 대학원
Department
대학원 환경공학과
Advisor
박청길
Table Of Contents
Ⅰ. 서론 = 1
1. 연구배경 = 1
2. 연구목적 = 6
Ⅱ. 문헌연구 = 8
1. Styrene의 개요 = 8
1.1 일반성상 = 8
2. 동전기 정화기술 = 10
2.1 동전기 원리 = 10
2.2 토양 내 동전기 현상 = 13
2.3 동전기 정화작용 = 18
2.4 동전기 정화기술 개발현황 = 25
2.5 동전기 기술 활용분야 = 26
3. 생물학적 복원 = 36
3.1 생물학적복원의 원리 = 36
3.2 생물학적복원의 종류 = 38
4. 동전기와 생물학적 복원방법의 혼용 = 43
4.1 전기장이 미생물의 활성과 거동에 미치는 영향 = 43
4.2 석유계 탄화수소 오염토양에 대한 동전기 생물학적복원에 적용 = 44
Ⅲ. 재료 및 방법 = 45
1. 토양 중 styrene 분석 = 45
1.1 실험시약 및 분석기기 = 45
1.2 시료의 전처리 = 46
2. 토양에 대한 styrene 흡착실험 = 47
3. 토양 중 styrene 분해 미생물의 분리ㆍ동정 및 특성연구 = 47
3.1 Styrene 분해 균주의 분리ㆍ동정 = 48
3.2 Styrene 분해 균주의 토양적용 가능성 = 49
3.3 Styrene 분해 균주의 특성 = 50
4. 증류수를 순환하지 않은 바탕실험과 동전기 단일 정화공정 = 51
4.1 실험재료 = 51
4.2 실험장치 = 51
4.3 실험조건 = 53
5. 미생물 배양액을 순환한 미생물 단일정화공정 = 54
5.1 실험재료 = 54
5.2 실험장치 = 54
5.3 실험조건 = 55
6. 미생물 배양액을 순환하여 동전기와 혼용한 정화공정 = 56
6.1 실험재료 = 56
6.2 실험장치 = 56
6.3 실험조건 = 57
Ⅳ. 결과 및 고찰 = 58
1. 토양 중 styrene 분석 = 58
1.1 정확도와 정밀도 = 58
1.2 표준검정선 및 검출한계 = 59
2. 토양에 대한 styrene 흡착실험 = 61
3. 토양 중 styrene 분해 미생물의 분리ㆍ동정 및 특성연구 = 64
3.1 Styrene 분해 균주의 분리 = 64
3.2 Styrene 분해 균주의 동정 = 65
3.3 Styrene 분해 균주의 토양적용 가능성 = 67
3.4 Styrene 분해 균주의 특성 = 68
3.4.1 pH 변화에 따른 증식 특성 = 68
3.4.2 온도 변화에 따른 증식 특성 = 69
3.4.3 Styrene 농도에 따른 증식 특성 = 71
4. 증류수를 순환하지 않은 바탕실험과 동전기 단일정화공정 = 73
4.1 토양의 투수계수 = 73
4.2 전류세기별 온도 변화 = 73
4.3 전류세기별 pH 변화 = 79
4.4 전류세기별 전압과 전류 변화 = 86
4.4.1 전압변화 = 86
4.4.2 전류변화 = 90
4.5 전류세기별 삼투유량 = 90
4.6 전류세기별 제거율 = 92
4.7 전류에 대한 삼투유량과 제거율의 상관관계 = 92
5. 미생물 배양액을 순환한 미생물 단일정화공정 = 95
5.1 온도 변화 = 95
5.2 pH 변화 = 97
5.3 삼투유량 = 99
5.4 미생물농도 = 99
5.5 제거율 = 100
6. 미생물 배양액을 순환하여 동전기와 혼용한 정화공정 = 101
6.1 전류세기별 온도 변화 = 101
6.2 전류세기별 pH 변화 = 105
6.3 전류세기별 전압과 전류 변화 = 112
6.3.1 전압 변화 = 112
6.3.2 전류 변화 = 117
6.4 각 실험조건의 삼투유량 = 118
6.5 전류세기별 미생물농도 = 122
6.6 전류세기별 제거율 = 125
6.7 전류에 대한 삼투유량과 제거율의 상관관계 = 129
7. 현장적용 = 131
Ⅴ. 결론 = 135
참고문헌 = 157
Degree
Doctor
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산업대학원 > 환경공학과
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