• 한국물환경학회지
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• 제21권3호
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• pp.256-262
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• 2005

The purpose of this study is to investigate the performances of organic removal and methane recovery by using a full scale two-phase anaerobic system. The full scale two-phase anaerobic process was consists of an acidogenic anaerobic baffled reactor (ABR) and a methanognic upflow anaerobic sludge blanket (UASB) reactor. The volumes of acidogenic and methanogenic reactors were designed to $28.3m^3$ and $75.3m^3$. The two-phase anaerobic system represented 60-82% of COD removal efficiency when the influent COD concentration was in the range of 7,150 to 16,270 mg/L after screening (average concentration is 10,280 mg/L). After steady-state, the effluent COD concentration in the methanogenic reactor showed $2,740{\pm}330 mg/L$ by representing average COD removal efficiency was $71.4{\pm}8.1%$ when the operating temperature was in the range of $19-32^{\circ}C$. The effluent SCOD concentration was in the range of 2,000-3,000 mg/L at the steady state while the volatile fatty acid concentration was not detected in the effluent. Meanwhile, the COD removal efficiency in the acidogenic reactor showed less than 5%. The acidogenic reactor played key roles to reduce a shock-loading when periodic shock loading was applied and to acidify influent organics. Due to the high concentration of alkalinity and high pH in the effluent of the methanogenic reactor, over 80% of methane in the biogas was produced consistently. More than 70% of methane was recovered from theoretical methane production of TCOD removed in this research. The produced gas can be directly used as a heat source to increase the reactor temperature.

• 한국물환경학회지
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• 제22권4호
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• pp.599-604
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• 2006

Nitrogen removal with the combined SHARON (Single reactor system for high ammonium removal over nitrite)ANAMMOX (Anaerobic ammonium oxidation) process using the effluent of ADEPT (Anaerobic digestion elutriated phased treatment) slurry reactor with very low C/N ratio for piggery waste treatment was investigated. For the preceding SHARON reactor, ammonium nitrogen loading and removal rate were $0.97kg\;NH_4-N/m^3_{reactor}/day$ and $0.68kg\;NH_4-N/m^3_{reactor}/day$ respectively. In steady state, bicarbonate alkalinity consumption for ammonium nitrogen converted to $NO_2-N$ or $NO_3-N$ was 8.4 gram per gram ammonium nitrogen. The successive ANAMMOX reactor was fed with the effluent from SHARON reactor. The loading and removal rate of the soluble nitrogen defined as the sum total of $NH_4-N$, $NO_2-N$ and $NO_3-N$ in ANAMMOX reactor were $1.36kg\;soluble\;N/m^3_{reactor}/day$ and $0.7kg\;soluble\;N/m^3_{reactor}/day$, respectively. The average $NO_2-N/NH_4-N$ removal ratio by ANAMMOX was 2.41. Fluorescence in situ hybridization (FISH) analysis verified that Candidatus Kuenenia stuttgartiensis were dominate, which means that they played an important role of nitrogen removal in ANAMMOX reactor.

• Carbon letters
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• 제7권2호
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• pp.105-113
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• 2006

The electro-chemical removal (ECR) of water pollutants by metal-ACF electrodes from wastewater was investigated over wide range of ECR time. The ECR capacities of metallic ACF electrodes were related to physical properties such as adsorption isotherm, surface area and pore size and to reaction time. Surface morphologies and elemental analysis for the metal supported ACFs after electro-catalytic reaction were investigated by scanning electron microscopy (SEM) and energy disperse X-ray (EDX) to explain the changes in adsorption properties. The IR spectra of metallic ACFs for the investigation of functional groups show that the electro-catalytic treatment is consequently associated with the removal of pollutants with the increasing surface reactivity of the activated carbon fibers. The metal-ACFs were electro-catalytically reacted to waste water to investigate the removal efficiency for the COD, T-N, $NH_4$-N, $NO_3$-N and $NO_2$-N. From these removal results of the piggery waste using metallic ACFs substrate, satisfactory removal performance was achieved. The removal efficiency of the metallic ACFs substrate was mainly determined by the properties of the material for adsorption and trapping of organics, and catalytic effects.

• 한국물환경학회지
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• 제22권3호
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• pp.482-491
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• 2006

The anaerobic ammonium oxidation (ANAMMOX) from substrates with various $NO_2-N$ and $NH_4-N$ concentationes, which were generated from piggery waste was accomplished by using anaerobic granular sludge as seeding sludge. As the result of operation, when $NO_2-N/NH_4-N$ ratios of ANAMMOX influent were 0.6~1.5, $NO_2-N/NH_4-N$ removal ratios were exhibited 1.19~2.07 (average 1.63). The higher influent $NO_2-N/NH_4-N$ ratios resulted in higher $NO_2-N/NH_4-N$ removal ratios by ANAMMOX. It means that $NO_2-N$ concentration is very important factor in ANAMMOX. Specific ammonium removal rate was constantly as $0.03{\sim}0.04gNH_4-N/g$ VSS-day at $35^{\circ}C$ while it was $0.01gNH_4-N/g$ VSS-day at $20{\sim}30^{\circ}C$. Thus, in order to reduce the effluent N concentration, either an increase of ANAMMOX reactor HRT or more biomass accumulation at the optimal temperature can be considered.

• 환경위생공학
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• 제10권3호
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• pp.67-77
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• 1995

This study was performed for minimization of excessive biofilm effects at the high strength organic wastewater treatment. As a results of biofilm attachment experiment using piggery wastewater, aggravation of water quality due to excessive biofilm showed after 15 days of operating times.4 excessive biofilm phase, the equivalent biofilm thickness and VSS contents per unit aura were observed in the range of 1,100 to $1,200{\mu}m$ and 2.5 to 3.0mg $VSS/cm^{2}$, respectively. In the aerobic fixed biofilm reactor/anoxic fixed biofilm reactor(AFBR/ANFBR) process with endogenous respiration phase, the BOD removal efficiency was obtained more than 90 percentage at the surface loading rate and volumetric loading rate of the AFBR maintained less than 17 g $BOD/m^{2}{\cdot}$day and 1.7kg $BOD/m^{3}{\cdot}$day, respectively. The removal efficiency of TKN and $NH_{3}$-N at the loading rates below 5.60g $NH_{3}-N/m^{2}{\cdot}day$ and 0.56kg $NH_{3}-N/m^{3}{\cdot}$day were above 76 percentage and 82 percentage, respectively. In order to reduced sludge production rate and aggravation of water quality, endogenous respiration phase was accepted at first AFBR reactor. As a results of this operating condition, sludge production was minimized and removal efficiency was maintained stability.

• 한국지능시스템학회:학술대회논문집
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• 한국퍼지및지능시스템학회 2002년도 추계학술대회 및 정기총회
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• pp.447-450
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• 2002

본 논문에서는 통합 관리 시스템을 이용하여 현재 김해에 있는 플랜트의 공정상태를 모니터링하고, 퍼지와 신경망을 이용하여 플랜트로부터 얻을 수 있는 데이터를 모델링 함으로써 공정의 상태를 미리 예측이 가능하도록 구성하였다. 이러한 예측된 모델을 이용하여 제어 전략을 설계함으로써 최적화된 제어 파라미터를 찾을 수 있으며, 특히 비정상적으로 들어오는 데이터에 대해서는 플랜트의 공정상태를 진단할 수 있는 가능성을 보이고 있다. 또한 기존의 통합 관리 시스템을 관리자라면 누구나 장소에 구애받지 않고 플랜트의 공정상태를 모니터링 할 수 있도록 웹을 이용하여 개발함으로써 플랜트의 능률성과 효율성 향상 및 인건비 절약 등 플랜트의 효율을 개선시킬 수 있다 즉, 네트워크가 구축되어 있는 곳이면 어디서나 모니터링이 가능하도록 시스템을 설계하였다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 춘계학술발표대회
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• pp.125-128
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• 2000

본 연구에서는 순환식 돈분 폐수 처리 시스템에서의 미생물 분포에 따른 폐수 처리 효과를 모델링하기 위해 신경회로망과 PCA를 이용하는 새로운 방법을 제안하였다. PCA 분석 결과를 바탕으로 신경회로망의 최적 입력 조건을 찾고, 실측 데이터를 이용하여, 폐수 처리 시스템의 각 탱크를 별도로 학습함으로써 비교적 적은 수의 데이터에도 불구하고 정확한 모델링 결과를 얻었다. 제안한 시스템은 폐수 처리 시스템의 효과적인모니터링 시스템으로 사용할 수 있으며, 향후 실제 돈분 처리 시스템에서 원하는 기준의 방류수를 얻기 위한 최적의 입력조건 (미생물밀도 등)을 결정하는데 있어서 에뮬레이터로 사용될 수 있을 것으로 기대된다.

• 한국환경보건학회지
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• 제18권2호
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• pp.67-74
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• 1992

The lab-scale biological A$_{2}$O system was applied from treating piggery wastewater highly polluted organic material which nitrogen and phosphorous are much contained relatively in conversion with other wastewater. The objective of this study was to investigate the effect of variance parameters on the treatability of this system according to operation conditions. An obtained experimental data were analysed by using principal component analysis (PCA) method. The results are summarized as follows: 1. From Varimax rotated factor loading in raw wastewater, variance of factor 1 was 36.8% and cumulative percentage of variance from factor 1 to factor 4 was 81.5% and of these was related to BOD, TKN and BOD loading. 2. In anaerobic process, variance of factor 1 was 33.5% and cumulative percentage of variance from factor I to factor 4 was 81.8% and of these was related to PO$_{4}$-P, BOD, DO and Temperature. 3. In anoxic process, variance of factor 1 was 30.1% and cumulative percentage of variance from factor i to factor 4 was 84.3% and of these was related to pH, DO, TKN and temperature. 4. In aerobic process, variance of factor 1 was 43.8% and cumulative percentage of variance from factor 1 to factor 4 was 81.5% and of these was highly related to DO, PO$_{4}$-P and BOD. 5. It was better to be operated below 0.30 kg/kg$\cdot$day F/M ratio to keep over 90% of BOD and SS, 80% of TKN, and 60% of PO$_{4}$-P in treatment efficiencies. 6. Treatment efficiencies was over 93% of BOD and SS, 81% of TKN and 60% of PO$_{4}$-P at over 20$^{\circ}$C, respectively.

• 대한환경공학회지
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• 제28권1호
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• pp.61-66
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• 2006

슬러리 형태의 돈사폐수로부터 자원회수와 질소제거를 위하여 순차적으로 ADEPT(Anaerobic digestion elutriated phased treatment) 공정과 SHARON(Single reactor system High Ammonium Removal Over nitrite)-ANAMMOX(Anaerobic ammonium oxidation)공정을 결합하여 운전하였다. ADEPT 공정은 부하율 3.95 gSCOD/L-day에서 운전되었고, SCOD 생성율과 산생성율은 각각 5.3 gSCOD/L-day와 3.3 gVFAs/L-day(as COD)였다. 가수분해에 의한 VS감소와 SCOD생성율은 각각 13%와 0.19 $gSCOD_{prod}/gVS_{feeding}$였으며, 산생성율은 0.80 $gVFAs/gSCOD_{prod.}$였다. 메탄발효조에서 가스생성율과 메탄함량은 각각 2.8 L/day($0.3m^3CH_4/kgCOD_{removal}\;@STP$) 및 77%였다. 운전조건에서 $NH_4-N$ 94.1% (TKN으로서 86.5%) 및 T-P 87.3%가 제거되었다.

• 대한환경공학회지
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• 제30권6호
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• pp.628-636
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• 2008

축산폐수를 처리하기 위한 2상 혐기성소화(TPAD)공정을 생물학적 질소제거공정(BNR)과 결합하여 운전하였다. 질산화된 유출수를 TPAD 공정의 산생성 반응조로 반송할 경우 탈질반응이 산생성 반응에 미치는 영향과 효율을 관찰하였다. 질산화된 유출수의 반송은 유입된 COD의 VFA로의 전환율을 향상시켰다. 질산화된 유출수에 적응된 산생성 슬러지의 산생성 속도는 적응되지 않은 슬러지보다 6배 빠른 것으로 관찰되었다. 탈질반응은 생성된 VFA를 탄소기질로써 사용하였지만 산생성 활성도를 향상시킬 수 있었다. 탈질속도는 COD/N비에 영향을 받았지만, 질산성 질소에 대한 산생성 슬러지의 적응여부에 더욱 지배적인 영향을 받는 것으로 나타났다. 산생성 슬러지에 의한 탈질반응은 0차 반응을 보였으며 탈질속도는 1.31$\sim$1.90 mg/L$\cdot$h이었다. 반면, 질산화된 유출수에 적응된 산생성 슬러지의 탈질속도는 3.30 mg/L$\cdot$h로 거의 2배가 빠른 것으로 나타났다. COD/N비 10에서 1g의 질산성 질소를 탈질반응에 의해 제거하는데 소비된 COD의 양론비는 5.1$\sim$6.4 범위이었다.