농 축 수산 유통집하장에서 발생하는 유기질 폐기물의 메탄 전환 기초 연구로서 실험실 규모로 수행하였다. 선발된 Run B 시료는 분석 결과 C/N Ratio는 18.41, TCOD는 168,960mg/L의 것이 얻어졌다. 생화학적 메탄 생산성 실험에서 이론 생산량은 313.6mg/L VS added이었고 실질적인 생산량은 234.2mg/L VS added로 혐기성소화에 의한 74%의 메탄 전환이 일어났으며, 반응속도론적 고찰에서 속도 상수는 $0.2476d^{-1}$이었다. 그리고 3단 여과막 충진형 반응기는 공시험 반응기보다 메탄함량은 16% 높고, TCOD 및 SCOD는 각각 44.7% 및 44.2%가 감소되었다.
농 축 수산 유통집하장에서 발생하는 유기질 폐기물의 메탄 전환 기초 연구로서 실험실 규모로 수행하였다. 선발된 Run B 시료는 분석 결과 C/N Ratio는 18.41, TCOD는 168,960mg/L의 것이 얻어졌다. 생화학적 메탄 생산성 실험에서 이론 생산량은 313.6mg/L VS added이었고 실질적인 생산량은 234.2mg/L VS added로 혐기성소화에 의한 74%의 메탄 전환이 일어났으며, 반응속도론적 고찰에서 속도 상수는 $0.2476d^{-1}$이었다. 그리고 3단 여과막 충진형 반응기는 공시험 반응기보다 메탄함량은 16% 높고, TCOD 및 SCOD는 각각 44.7% 및 44.2%가 감소되었다.
A fundamental study on methane conversion for the collection organic wastes of agriculture, forestry and fishers was performed in a laboratory scale. As a result, selected Run B sample were obtained 18.41 C/N Ratio and 168.96 mg/L TCOD; Under the biochemical methane potential test, theoretical and a...
A fundamental study on methane conversion for the collection organic wastes of agriculture, forestry and fishers was performed in a laboratory scale. As a result, selected Run B sample were obtained 18.41 C/N Ratio and 168.96 mg/L TCOD; Under the biochemical methane potential test, theoretical and actual methane generation was 313.6 mg/L VS added and 234.2 mg/L VS added, respectively; However, methane conversion from Run B were occurred 74% by anaerobic digestion. By the first order reaction kinetics, kinetic constant were $0.2476d^{-1}$ for Run B. Three steps fill-up filter reactor was evaluated methane content 16% up to promote than blank reactor; TCOD and SCOD have reduced 44.7% and 44.2%, respectively.
A fundamental study on methane conversion for the collection organic wastes of agriculture, forestry and fishers was performed in a laboratory scale. As a result, selected Run B sample were obtained 18.41 C/N Ratio and 168.96 mg/L TCOD; Under the biochemical methane potential test, theoretical and actual methane generation was 313.6 mg/L VS added and 234.2 mg/L VS added, respectively; However, methane conversion from Run B were occurred 74% by anaerobic digestion. By the first order reaction kinetics, kinetic constant were $0.2476d^{-1}$ for Run B. Three steps fill-up filter reactor was evaluated methane content 16% up to promote than blank reactor; TCOD and SCOD have reduced 44.7% and 44.2%, respectively.
※ AI-Helper는 부적절한 답변을 할 수 있습니다.