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진양오,윤철종,우성훈,최성우,김익성,박승조 동아대학교 환경문제연구소 1999 硏究報告 Vol.22 No.1
The objective of this study were to treat waste paper with waste acid and alkali so to enhance maturity of the wastes. The sample was office paper and news paper which ratio was 1:1 and the reagents for pre-treatment were sulfuric acid and sodium hydroxide for waste acid and alkali. The maturity indices were taken volatile solid. cation exchange capacity, and gas production variation. The pre-treatment method was to dip the sample in the reagent according to time, concentration, and dosage. The methods of treatment were to dip the wastes in leachate and to landfill in soil. The result of this study were as follow. When waste paper was treated by acid and alkali, the proper treatment condition was 24hours and 0.1 normality of acid and alkali. The pre-treated samples with acid and alkali such as RSN and RSH were more effective in maturity than non-treated sample such as RS. The post-treated sample such as RSL, RSNL, and RSHL was more effective than nonpost-treated sample such as RS, RSN, and RSH.
16인치 막을 사용한 부산 기장 해수 담수 플랜트 소개
진양오,최현성,이우녕 한국막학회 2015 한국막학회 총회 및 학술발표회 Vol.2015 No.11
본 발표는 45,460 m³/d (10 Million Imperial Gallons per Day (MIGD)) 규모를 가진 한국 최초 및 최대 대규모인 부산 기장 해수담수화 플랜트에 대한 소개이다. 본 플랜트는 2010년부터 건설 되어 2015년 말에는 상업 운전이 시작될 예정이다. 플랜트의 특징으로는 국산화된 다양한 전처 리 기술 (DABF, MF, DMF)의 적용, 대용량 16인치 RO 막 적용, 에너지 소모량을 줄이기 위한 대 용량 8 MIGD RO train의 one module화 이다. 16인치 RO 막은 평균 48%의 high recovery rate 과 14.7 LMH high flux의 성능을 보였으며, 최종 power consumption은 약 3.98 kWh/m³을 기록 하였다.
진양오,최성우,김성우,김익성,신남철,박승조 동아대학교 환경문제연구소 1999 硏究報告 Vol.22 No.2
The purpose of thus study were to investigate the proper conditions of struvite formation in synthetic wastewater and then to apply these conditions to effluent of anaerobic digester of livestock wastewater The conditions of struvite formation had been studied by many researchers. But a little conditions were different among them. Especially, according to suspended solid variation in livestock wastewater was investigated by few researchers. In experiment of synthetic wastewater, the proper conditions of struvite formation were pH 105, l50rpm of mixing rate, 10 minutes of reaction time, and 20 minutes of precipitation time. At same time, the ammonia nitrogen removal rates were about 99.7%, 95.5%, and 96% of synthetic wastewater, raw wastewater, and effluent of anaerobic digester of livestock wastewater at molar ratio of 2(Mg):l(N)2(P) respectively. The larger factor of NH₄/SS constant was, the more effective the removal rate of ammonium nitrogen, SS was, but the less effective COD_(cr), and TOC was. By using XRD analysis, the most certain compound in precipitate of synthetic wastewater was struvite.
윤철종,진양오,박승조 한국자원리싸이클링학회 1999 資源 리싸이클링 Vol.8 No.3
폐주물사 재이용 방안으로 하수처리시 폐주물사를 여재로써 이용하여 인제거에 적용하고져 하였다. 용액의 pH를 2, 6, 11로 조정하여 인제거 실험한 결과 pH2에서 가장 우수한 제거율을 나타내었으며 폐주물산 100g 으로 반응시켰을 경우 2시간의 반응에서 99.9% 이상의 인제거율은 나타내었다. 또한 Langmuir 등온 흡착 모델에 적용한 결과 ${\Gamma}=0.0005{\theta}$/(1+2.4987 $\theta$)의 등온흡착식을 얻었으며 연속식 실험에서 파괴농도를 8mg/l로 하였을 경우 폐주물사의 파과시산은 25hrs으로 나타났다. The removal of phosphorus was investigated from sewage waste water (SWW) using the used foundry sand (UFS). The optimal pH occurred at pH 2 for adsorption of phosphorus species in batch test. Phosphorus could be recovered with 99.9% from SWW in two hours at pH 2 using 100 g of UFS per liler of SWW. The adsorption of phosphorus species on UFS obeyed Langmuir isotherm, whose equation could be expressed by 1= 0.00059/(1+2.49878). Continuous column test for adsorption showed that breakthrough point appeared In 25 hours on the condition of breakthrough concentration of 8 mg/l
암모니아 산화균 및 아나목스균의 배양을 통한 파일롯 규모 단일 아나목스 반응기의 성공적인 시운전
최대희,진양오,이철우,정진영 대한상하수도학회 2018 상하수도학회지 Vol.32 No.5
The lack of seed sludges for Ammonium Oxidizing Bacteria (AOB) and slow-growing ANaerobic AMMonium OXidation (ANAMMOX) bacteria is one of the major problem for large-scale application. In this study, 24m3 of single-stage SBR (Sequencing Batch Reactor) was operated to remove nitrogen from reject water using AOB and ANAMMOX bacteria cultivated from activated sludge in the field. The ANAMMOX activity was found after 44 days of cultivation in the ANAMMOX cultivation reactor, and then 0.66 kg N/m3/d of the nitrogen removal rate was achieved at 0.78 kg N/m3/d of the nitrogen loading rate at 153 days of cultivation. The AOB cultivation reactor showed 0.2 kg N/m3/d of nitrite production rate at 0.4 kg N/m3/d of nitrogen loading rate after 36 days of operation. The cultivated ANAMMOX bacteria and AOB was mixed into the single-stage SBR. The feed distribution was applied to remove total nitrogen stably in the single-stage SBR. The nitrogen removal rate in the single-stage SBR was gradually enhanced with an increase of specific activities of both AOB and ANAMMOX bacteria by showing 0.49 kg N/m3/d of the nitrogen removal rate at 0.56 kg N/m3/d of the nitrogen loading rate at 54 days of operation.