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학술연구/단체지원/교육 등 연구자 활동을 지속하도록 DBpia가 지원하고 있어요.
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연구자들이 자신의 연구와 전문성을 널리 알리고, 새로운 협력의 기회를 만들 수 있는 네트워킹 공간이에요.
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In the organic waste, food waste is the most difficult controls. In the study, food waste was treatmented to removal only the dockage. To decrease the hydrogen sulfide(H₂S) in the produced biogas, iron chloride put in the anaerobic digester. Respectively treatment quantity of the food waste, content of the methane(CH₄) gas in the biogas, produced gases quantity, put in the quantity of the Iron chloride, pH, TS, Alkalinity, VFA, Ammonia.
The results obtained from the experiment are as follows:
1. The produced biogases quantity/the treatment quantity of the food waste was 83.82～129.41㎥/ton.
2. The content of the hydrogen sulfide(H₂S) in the produced biogas is below of the 500ppm. The iron chloride put in the anaerobic digester. 200～300㎏ of the iron chloride put in the anaerobic digester at the steady-state. 400～850㎏ of the iron chloride put in the anaerobic digester at the unsteady-state.
3. Factor of the operator was the pH: 7.7～8.4, content of mathane: 55～65%.
4. TS(total solid) of the digestor sludge was 17～20%, Alkalinity was 38,500～41,750ppm, VFA(Volatile Fatty Acids) was 2,800～2,420ppm, Ammonia was 4,300～3,650ppm.
The results obtained from the experiment are as follows:
1. The produced biogases quantity/the treatment quantity of the food waste was 83.82～129.41㎥/ton.
2. The content of the hydrogen sulfide(H₂S) in the produced biogas is below of the 500ppm. The iron chloride put in the anaerobic digester. 200～300㎏ of the iron chloride put in the anaerobic digester at the steady-state. 400～850㎏ of the iron chloride put in the anaerobic digester at the unsteady-state.
3. Factor of the operator was the pH: 7.7～8.4, content of mathane: 55～65%.
4. TS(total solid) of the digestor sludge was 17～20%, Alkalinity was 38,500～41,750ppm, VFA(Volatile Fatty Acids) was 2,800～2,420ppm, Ammonia was 4,300～3,650ppm.
목차
Abstract
Ⅰ. 서론
Ⅱ. 실험방법
Ⅲ. 결과 및 고찰
Ⅵ. 결론
감사의 글
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