• 유기물자원화
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• 제19권2호
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• pp.49-54
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• 2011

본 연구는 혐기성 수소 발효 반응조의 유출수를 기질로 이용하여 anaerobic baffled reactor (ABR) 및 anaerobic sequencing batch reactor (ASBR) 형태에 따른 혐기성 메탄 발효 성능을 평가하였다. 두 개의 반응조는 유기물 부하율 $1.0kg\;COD/m^3{\cdot}d$와 수리학적 체류시간 20일에서 운전을 수행하였다. ABR과 ASBR의 초기 운전 기간에서 메탄 발생량은 각각 0.04 L/L/d와 0.19 L/L/d로 나타났으며, ABR과 ASBR의 최대 메탄 발생량은 각각 0.25 L/L/d와 0.31 L/L/d로 나타났다. ABR과 ASBR의 초기 운전 기간에서 COD 제거율은 각각 89%와 92%로 나타났다. 정상 상태에 도달한 후에는 ABR과 ASBR의 COD 및 VS의 제거율은 각각 90% 이상 유지되었다. 비메탄 활성도는 미생물이 기질에 적응함에 따라 반응조에 상관없이 증가하였다.

• 대한환경공학회지
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• 제31권12호
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• pp.1075-1080
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• 2009

혐기성 소화 시 산발효 단계에서 지질 성분이 부분적으로 분해되고 지질 내 이중 결합이 포화됨을 통해 후단의 메탄발효 효율이 향상됨이 보고된 바 있다. 본 연구에서는 혐기성 연속 회분식 반응조(anaerobic sequencing batch reactor, 이하 ASBR) 및 연속 흐름 교반 반응조(continuously stirred tank reactor, 이하 CSTR) 형태의 산생성조를 각각 운전하여 지질 분해 및 독성 저감 효율을 살펴보았다. 기질로는 두 가지 불포화(oleate and linoleate), 두 가지 포화(palmitate and stearate) 지방산(long-chain fatty acids, 이하 LCFA)로 구성된 LCFA 혼합물을 사용하였다. 반응조 내의 높은 미생물 보유량에 의해 ASBR이 수리학적 체류시간(hydraulic retention time, 이하 HRT) 12 hr 이하에서 우월한 성능을 보였다. HRT 9시간에서 ASBR은 36.7%의 LCFA 분해, 14.3%의 이중결합 포화, 43.8%의 산생성 효율을 보였으며, 이는 HRT 15시간의 CSTR 보다 각각 19%, 10%, 21% 높은 수치였다. 지질 함유 폐수의 혐기성 소화 시 ASBR을 이용한 산발효가 효과적일 것으로 판단된다.

• 한국환경과학회지
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• 제1권2호
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• pp.125-136
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• 1992

Digestion of a municipal wastewater sludge by the anaerobic sequencing batch reactor (ASBR) was investigated to evaluate the performance of the ASBR process at a critical condition of high-solids-content fined. The reactors were operated at an HRT of 10 days with an equivalent loading rate of 0.8-1.5 gVS/L/d at 35$^{\circ}C$ The main conclusions drawn from this study were as follows: 1. Digestion of a municipal wastewater sludge was possible using the ASBR in spite of high concentration of settleable solids in the sludge. The ASBRS with 3- and 4-day cycle period showed almost identical high digestion performances. 2. No adverse effect on digestion stability was observed In the ASBRS in spite of withdrawal and replenishment of 30% or 40% of liquid contents. A conventional anaerobic digester could be easily converted to the ASBR without any stability problem. 3. Flotation thickening occurred in thicken step of the ASBRS throughout steady state, and floating bed volume at the end of thicken period occupied about 70% of the working volume of the reactor Efficiency of flotation thickening in the ASBRS could be comparable to that of additional gravity thickening of a completely mixed digester. 4. Solids were accumulated rapidly in the ASBR during start-up period. Solids concentrations in the ASBRS were 2.6 times higher than that in the completely mixed control reactor at steady state. Dehydrogenase activity had a strong correlation with the solids concentration. Dehydrogenase activity of the digested flu형e in the ASBR was 2.9 times higher than that of the flu형e in the control reactor, and about 25 times higher than that of the subnatant in the ASBR. 5. Remarkable increase in equivalent gas production of 52% was observed at the ASBRS compared with the control reactor in spite of similar quality of clarified effluent from the ASBRS and control reactor. The increase in gas production from the ASBRS was believed to be combined results of accumulation of microorganisms, higher driving force applied, and additional long-term degradation of organics continuously accumulated.

• 한국환경과학회지
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• 제7권6호
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• pp.867-873
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• 1998

Laboratory study was conducted to provide basic data for operating anaerobic sequencing batch reactor(ASBR) process for treatment of nightsoil. The experiments were concerned with digestion characteristics, settleabiltity and dewaterability of digested sludge in ASBR system. Completely-mixed dally-fed control reactor without solid-liquid separation step was also operated to evaluate the baseline performance since the nature of nightsoil was changed with time. In all case, gas production from the ASBR shows 1.3 to 1.44 times higher than that from control, in spite of almost similar trend in organics removal. During thickening period, remarkable decrease in surface settling velocity was observed at the ASBRs compared with the control. In case of the ASBR run, flotation of mixed digested sludge was not occurred. Also, ultimate thickened volume of ASBRs increased 1.2~1.5 times compared with control. Dewaterability of digested sludge without conditioning decreased when the completely-mixed daily-fed reactor for ASBR run was converted to the ASBR. However, improvement of dewaterability of digested sludge from the ASBRs was observed as a result of addition of FeCl$_3$ to digested sludge for conditioning.

• 한국환경보건학회지
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• 제28권5호
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• pp.77-85
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• 2002

중온과 고온의 혐기성 연속회분식 공정(anaerobic sequencing batch reactor ; ASBR)에서 소화슬러지의 고액분리특성이 처리효율에 미치는 영향을 규명하고자 하였다. 연구결과 침전가능 고형물농도가 높은 도시하수슬러지 처리시 고액분리특성 및 고액분리형태가 전체처리의 안정성 및 처리효율에 상당한 영향을 미쳤다. 중온ASBR에서는 부상농축현상이 일어났으나, 고온ASBR에서는 중력농축에 의한 고액분리가 일어났으며, 상대적으로 고온 ASBR의 처리효율이 우수하였다. 그리고 수리학적 체류시간, cycle period 및 고액분리형태는 소화슬러지의 농축 특성과 임계 고형물농축을 지배하는 중요한 인자였다. 중온ASBR에서 고액분리 후 농축슬러지베드용적(thickened sludge bed volume)은 매우 중요한 운전 요소이며, 소화슬러지의 중력농축특성은 배출시 농축고형물의 유실현상과 침전시 계속적으로 발생하는 소화가스에 의한 슬러지계면의 파괴현상 및 슬러지베드의 불안전성을 야기시켜 처리효율을 감소시켰다. 중력농축의 경우 소화가스와 슬러지농축용적간의 상호작용(cyclic mutual effect)이 주기적으로 일어났으나, 부상농축에서는 이러한 현상이 일어나지 않았다.

• 유기물자원화
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• 제12권1호
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• pp.75-83
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• 2004

혐기성 소화효율의 극대화를 위해 온도상분리 공정과 혐기성 회분식 공정을 음식물 쓰레기와 하수슬러지의 혼합기질에 적용한 온도상분리 혐기성 회분식 소화공정(TPAD-ASBR)의 거동 특성을 유기물부하의 변화에 따라 평가하여 다음과 같은 결론을 얻었다. TPAD-ASBR 과 대조구의 첫 단에서 대부분의 메탄생성과 유기물 제거가 이루어졌으며, 단위부피당 메탄발생량은 유기물부하 2.7 g VS/L/d에서 각각 0.79와 0.59L $CH_4/L/d$ 였다. 동일 부하에서 TPAD-ASBR의 유기물 제거효율은 61%이었으며 40%의 효율을 보인 대조구에 비해 고온조를 도입한 본 공정의 우수성을 확인하였다. 국내 하수슬러지는 상대적으로 낮은 VS 농도(1.5%, w/w)와 낮은 생분해 효율을 보이는데, 이러한 부정적 특성을 보완하기 위하여 투입된 음식물쓰레기에 의한 기질 특성의 효과적인 개선으로 인해 높은 유기물 감량과 메탄회수가 가능하였다. 또한, track study를 통해 연속회분식 운전방식에 의한 settling 단계의 도입으로 SRT를 HRT보다 길게 유지하여 미처리 입자와 active biomass의 효율적이고 지속적인 접촉을 도모하여 보다 높은 안정화효율 획득이 가능한 것으로 사료된다. 따라서, 혐기성소화공정에 TPAD-ASBR공정과 함께 음식물쓰레기와의 혼합소화를 도입하는 것은 처분이 까다로운 두 가지의 폐기물을 고효율로 처리함과 동시에 효율적인 에너지회수가 가능하여 경제적 운전이 가능하였다.

• Environmental Sciences Bulletin of The Korean Environmental Sciences Society
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• 제1권2호
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• pp.125-136
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• 1997

Digestion of a municipal wastewater sludge by the anaerobic sequencing batch reactor(ASBR) was investigated to evaluate the performance of the ASBR process at a critical condition of high-solids-content feed. The reactors were operated at an HRT of 10 days with an equivalent loading rate of 0.8-1.5 gVS/L/d at $35^{\circ}C.$ The main conclusions drawn from this study were as follows: 1. Digestion of a municipal wastewater sludge was possible using the ASBR in spite of high concentration of settleable solids in the sludge. The ASBRS with 3- and 4-day cycle period showed almost identical high digestion performances. 2. No adverse effect on digestion stability was observed in the ASBRS in spite of withdrawal and replenishment of $30\%\;or\;40\%$ of liquid contents. A conventional anaerobic digester could be easily converted to the ASBR without any stability problem. 3. Flotation thickening occurred in thicken step of the ASBRS throughout steady state, and floating bed volume at the end of thicken period occupied about $70\%$ of the working volume of the reactor. Efficiency of flotation thickening in the ASBRS could be comparable to that of additional gravity thickening of a completely mixed digester. 4. Solids were accumulated rapidly in the ASBR during start-up period. Solids concentrations in the ASBRS were 2.6 times higher than that in the completely mixed control reactor at steady state. Dehydrogenase activity had a strong correlation with the solids concentration. Dehydrogenase activity of the digested sludge in the ASBR was 2.9 times higher than that of the sludge in the control reactor, and about 25 times higher than that of the subnatant in the ASBR. 5. Remarkable increase in equivalent gas production of $52\%$ was observed at the ASBRS compared with the control reactor in spite of similar Quality of clarified effluent from the ASBRS and control reactor. The increase in gas production from the ASBRS was believed to be combined results of accumulation of microorganisms, higher driving force applied, and additional long-term degradation of organics continuously accumulated.

• 환경위생공학
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• 제9권1호
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• pp.29-37
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• 1994

Anaerobic treatment of wastewater of the red- bean processing industry was carried out and discussed an anaerobic sludge bed reactor( ASBR) as a preliminary study to evaluate applicability of given processes. The dimension of reactor were same as 0.09m- ID$\times $1.5m- height. The type of substrate and the hydraulic retention time( HRT) were considered as experimental variables. The synthetic wastewater with glucose in the laboratory, the wastewater from the red bean processing industry mixed with synthetic wastewater with variation of mixing percent were fed as substrate. The hydraulic retention time was changed from one day to five days. The gas production, the methane content in produced gas, efficiencies of COD removal and 55 removal were evaluated as principal characteristics. With synthetic wastewater as a substrate and at a hydraulic retention time of one day, characteristics of ASBR was the gas production(12$\ell$/day ), the methane content of produced gas(60%), the efficiency of COD removal(92%) and 55 removal(30%). With the real wastewater and at a hydraulic retention time of one day, the gas production and the efficiency of COD removal of the ASBR decreased with the proportion of real wastewater. The gas production and the efficiency of COD removal with real wastewater only was decreased to 70% and 87% of those with synthetic wastewater only, respectively. However, the methane content in produced gas and the efficiency of 55 removal with real wastewater only was increased significantly by 1.25 times and two times of those with synthetic wastewater only, respectively. However, the methane content in produced gas and the efficiency of 55 removal with real wastewater only was increased significantly by 1.25 times and two times of those with synthetic wastewater only, respectively. With real wastewater only as a substrate in the ASBR, the gas production was decreased with an increase of HRT, but the efficiency of COD removal increased with HRTI like the usual trend reported. As a conclusion, the wastewater of the red- bean Processing industry could be treated by anaerobic digestion successfully in the ASBR.Anaerobic treatment of wastewater of the red- bean processing industry was carried out and discussed an anaerobic sludge bed reactor( ASBR) as a preliminary study to evaluate applicability of given processes. The dimension of reactor were same as 0.09m- ID$\times $1.5m- height. The type of substrate and the hydraulic retention time( HRT) were considered as experimental variables. The synthetic wastewater with glucose in the laboratory, the wastewater from the red bean processing industry mixed with synthetic wastewater with variation of mixing percent were fed as substrate. The hydraulic retention time was changed from one day to five days. The gas production, the methane content in produced gas, efficiencies of COD removal and 55 removal were evaluated as principal characteristics. With synthetic wastewater as a substrate and at a hydraulic retention time of one day, characteristics of ASBR was the gas production(12$\ell$/day ), the methane content of produced gas(60%), the efficiency of COD removal(92%) and 55 removal(30%). With the real wastewater and at a hydraulic retention time of one day, the gas production and the efficiency of COD removal of the ASBR decreased with the proportion of real wastewater. The gas production and the efficiency of COD removal with real wastewater only was decreased to 70% and 87% of those with synthetic wastewater only, respectively. However, the methane content in produced gas and the efficiency of 55 removal with real wastewater only was increased significantly by 1.25 times and two times of those with synthetic wastewater only, respectively. However, the methane content in produced gas and the efficiency of 55 removal with real wastewater only was increased significantly by 1.25 times and two times of those with synthetic wastewater only, respectively. With real wastewater only as a substrate in the ASBR, the gas production was decreased with an increase of HRT, but the efficiency of COD removal increased with HRTI like the usual trend reported. As a conclusion, the wastewater of the red- bean Processing industry could be treated by anaerobic digestion successfully in the ASBR.

• 환경위생공학
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• 제10권1호
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• pp.98-105
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• 1995

In the treatment of wastewater or sewage plant sludge with high solid concentration, high rate digestion process in which heating and mixing occur at a time is mainly used, and in the case of wastewater containing solid matter below 1000mg/ℓ the recently developed AF or UASB is developed Recently and commonly utilized. But these processes have weakpoints such as clogging of packing media and need of long period of trial run after microorganism granulation. In this point of view, there are active researches on the ASBR( anaerobic sequence batch reaction ) that is capable of treating of organic matter with reactor that has no packing materials and controlling the inflow time, reaction time sedimentation time and outflow time by time control without loss of microorganisms. The objectives of this study are to evaluate the efficiency of ASBR process according to the reaction time, change of treated water quality and gas output rate in the treatment of wheat plant wastewater.

• 한국축산시설환경학회지
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• 제13권3호
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• pp.219-232
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• 2007

Odors from manures are a major problem for livestock production. The most significant odorous compounds in animal manure a.e volatile fatty acids(VFAs). This work reviews the VFAs from the anaerobic sequencing biofilm batch reactor(ASBBR), anaerobic sequencing batch reactor(ASBR), solid compost batch reactor(SCBR), and aerobic sequencing batch reactor(SBR) associated with the animal manure biological treatment. First, we describe and quantify VFAs from animal manure biological treatment and discuss biofiltration for odor control. Then we review certain fundamentals aspects about Anaerobic and aerobic SBR, composting of animal manure, manure compost biofilter for odorous VFAs control, SBR for nitrogen removal, and ASBR for animal wastewater treatment systems considered important for the resource recovery and air quality. Finally, we present an overview for the future needs and current experience of the biological systems engineering for animal manure management and odor control.