• 한국지하수토양환경학회지:지하수토양환경
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• 제27권1호
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• pp.60-70
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• 2022

We evaluated the performance of in-situ capping to prevent the release of phenol, one of hazardous chemicals of concern for their impact on sediment. Sediment near the estuary of Hyeongsan River, Korea, and commercially-available sand were collected to evaluate their physical properties and phenol sorption characteristics. Biodegradation kinetics of phenol spiked into the sediment was evaluated under freshwater and estuarine salinity conditions. These experimental measurements were parameterized and used as input parameters for executing CapSim, a software predicting the performance of in-situ capping. The CapSim simulation demonstrated that capping with 50-cm sand reduced the phenol release by several orders of magnitude over 0.25- and 1-year duration for almost all simulation scenarios. The variables tested, i.e., cap thickness, pore-water movement, and biodegradation rate, showed high correlation to each other to influence the extent of phenol release from sediment to the water column. The findings and the framework employed to evaluate the performance of in-situ capping in this study can be adopted to determine whether in-situ capping is appropriate remedial approach at sediment sites impacted by hazardous chemicals due to accidental spills.

• 청정기술
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• 제28권1호
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• pp.32-37
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• 2022

Food waste is produced from food factories, food services, and home kitchens. The generated mass reached 5.4 million tons/year in 2020. The basic management technology for such waste has been biological degradation under an anaerobic environment. However, the whole process is intrinsically slow and considerably affected by the inner physicochemical properties of the waste and other surrounding conditions, which makes optimization of the process difficult. The most promising options to counter this massive generation of waste are eco-friendly treatments or recycling. As a preliminary step for these options, attempts were made to evaluate the feasibility and usability of three simulative models based on reaction kinetics. Model (A) predicted relative changes over reaction time for reactant, intermediate, and product. Overall, an increased reaction rate produced less intermediate and more product, thereby leading to a shorter total reaction time. Particle diminishing model (B) predicted reduction of the total waste mass. The smaller particles diminished faster along with the dominant effect of microbial reaction. In Model (C), long-chain cellulose was predicted to transform into reducing sugar. At a standard condition, 48% of cellulose molecules having 10⁵ repeating units turned into reducing sugar after 100 h. Also it was found that the optimal enzyme concentration where the highest amount of remnant sugar was harvested was 1 mg L^-1.

• 한국지하수토양환경학회지:지하수토양환경
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• 제8권4호
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• pp.12-20
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• 2003

본 연구에서는 원위치 생물학적 처리 과정에서 공대사 기작에 의해 분해되는 유기오염물질의 성상과 거동을 모의하기 위한 수학적 모델을 제기하였다. 토양구조 내에서 부동유역의 존재가 처리 과정에 미치는 영향을 고려하기 위하여 이중공극 개념을 적용하였으며, 유기오염물질의 거동과 생물학적 처리에 미치는 미생물의 영향을 수학적으로 표현하기 위하여 수정된 Monod식과 토양상 미생물의 미소군집모형이 적용되었다. 가상의 원위치 생물학적 처리 과정에 대한 모델의 적용을 통하여 공극내 생체축적으로 인한 투수능의 감소가 지하수 흐름에 미치는 영향이 예시되었다. 가상의 생물학적 처리 과정에 대한 모델의 모의결과는 부동유역의 존재가 유기오염물질의 생물학적 가용성을 저감시키며, 생물벽체의 형성 및 처리과정에 있어 외부로부터의 미생물 및 영양물질 주입정의 위치가 효과적인 처리 계획의 수립을 위해 중요하다는 것을 보여 주었다.

• 유기물자원화
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• 제15권4호
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• pp.131-137
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• 2007

황산염 환원조건에서의 리그노셀룰로오스의 분해에 대하여 고찰하였다. 특히, 리그닌에 대한 셀룰로오스의 비(C/L 비)를 각각 42.15, 4.59, 2.51, 1.14, 0.7로 하여 리그닌과 셀룰로오스의 상호작용에 대하여 고찰하였다. 셀룰로오스의 분해율은 1차 반응식에 의해 계산되어져, C/L 비가 감소할수록 반응상수는 감소하여 셀룰로오스의 분해에 대한 리그닌의 저해작용을 보여 주였다. 1차 반응식에 의한 반응상수와 리그닌의 함량의 증가에 대한 셀룰로오스의 분해율은 0.97의 $R^2$ 값을 가지며 로그힘수에 의해 표현할 수 있었다. 리그노셀룰로오스의 분해율 또한 C/L 비와 로그함수의 관계를 가지며 리그닌의 함량이 많을수록 감소하였다. 리그닌의 분해율은 C/L 비가 2.51 및 1.14인 조건에서 4.59 및 0.7의 조건보다 높게 나타나, 공동기질로서의 과도한 탄소원은 리그닌분해에 장애가 됨을 보여 주였다.

• 대한환경공학회지
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• 제31권10호
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• pp.927-932
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• 2009

난분해성 및 독성 폐수 처리는 고급산화 기술과 생물학적 처리가 친화결합(intimate coupling) 을 이룰 때 최적의 효과를 거둘 수 있다. 본 연구에서는 광촉매 산화와 생물학적 처리를 친화결합하도록 고안된 다공성 $TiO_2$ 코팅 담체를 제조하여 광촉매 반응에 관한 동력학 연구를 수행하였다. 저온 sol-gel 코팅법으로 제조된 PVA 재질의 다공성 $TiO_2$ 담체는 UV 조사하에서 methylene blue (MB)를 효율적으로 분해하였다. 시험 농도(최대 100 ${\mu}M$)에서 MB의 흡착속도는 1차반응 (first-order reaction)의 성질을 보였으며, 흡착과 산화를 포함한 총반응속도는 유사 Langmuir 모델로 예측 가능하였다. 이러한 원인은 담체 표면에 MB가 흡착됨에 따라 UV 조사에 의하여 광촉매 반응이 일어날 표면이 줄어들었기 때문인 것으로 판단된다. 다공성 $TiO_2$ 담체의 단위 $TiO_2$ 량당 최대 MB 제거속도는 슬러리 $TiO_2$ 반응기에서 얻은 MB 제거속도보다 4배 더 빨랐다. 본 연구로 인하여 저온 sol-gel 코팅법으로 제조한 PVA 재질 다공성 $TiO_2$ 담체가 성공적인 광분해 반응을 나타내는 것이 확인되었으며, 동 담체에 대한 광촉매 반응의 동력학적 성질이 구명되어, 향후 생물처리를 친화결합 시킬 수 있는 연구 바탕을 확보하였다.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2000년도 창립총회 및 춘계학술발표회
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• pp.92-95
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• 2000

A mixed bacterial culture capable of mineralizing methyl tort-butyl ether (MTBE), other fuel oxygenates ethers, tertiary carbon alcohols, benzene and toluene was used to inoculate batch reactor and sequence batch reactor (SBR) to treat gasoline contaminated ground water containing about 60 mg/L MTBE, 5 mg/L benzene, 5 mg/L toluene, and low concentrations of several other aromatic and aliphatic hydrocarbons. Respirometery studies showed that MTBE degrading mixed culture could treat MTBE contaminated ground water with addition of nitrogen and phosphate. SBR was operated to demonstrate the feasibility of using suspended growth activated system for the treatment of ground water and to confirm that the respirometry derived kinetics and stoichiometric coefficients were useful for predicting reactor performance. Theoretical performance of the reactor was predicted using mathematical models calibrated with biokinetic parameters derived from respirometry studies.

• Journal of Microbiology
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• 제35권3호
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• pp.193-199
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• 1997

From several industrial wastewaters, 14 bacterial strains which degrade benzene, toluene, o-xylene, m-xylene, or p-xylene (BTX) were obtained. These strains were characterized as to their species composition and the substrate range, kinetic parameters and the substrate interactions were investigated. Although BTX components have a similar chemical structure, isolated strains showed different substrate ranges and kinetic parameters. None of the strains could degrade all of BTX components and most of them showed an inhibition (Haldane) kinetics on BTX, BTX mixtures were removed under inhibitory substrate interactions with variation in the intensity of inhibition. For a complete degradation of BTX, a defined mixed culture containing three different types of patyways was constructed and all of the BTX components were simultaneously degraded with the totla removal rate of 225.69 mg/g biomass/h Judging from the results, the obtained mixed culture seems to be useful for the treatment of BTX-contaminated wastewater or groundwater as well as for the removal of BTX from the contaminated air stream.

• Advances in environmental research
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• 제2권3호
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• pp.229-243
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• 2013

Coagulation-flocculation (CF) was tested coupled with an aerobic biofilter to reduce total petroleum hydrocarbon (TPHs) concentration and toxicity from petrochemical wastewater. The efficiency of the process was followed using turbidity and chemical oxygen demand (COD). The biofilter was packed with a basaltic waste (tezontle) and inoculated with a bacterial consortium. Toxicity test were carried out using Lactuca sativa var. capitata seeds. Best results for turbidity removal were obtained using alum. Considerable turbidity removal was obtained when using Opuntia spp. COD removal with alum was 25%, for Opuntia powder it was 36%. The application of the biofilter allowed the removal of 70% of the remaining TPHs after 30 days with a biodegradation rate (BDR) value 47 $mgL^{-1}d^{-1}$. COD removal was slightly higher with BDR value 63 $mgL^{-1}d^{-1}$. TPH kinetics allowed a degradation rate constant equal to $4.05{\times}10^{-2}d^{-1}$. COD removal showed similar trend with $k=4.23{\times}10^{-2}d^{-1}$. Toxicity reduction was also successfully achieved by the combined treatment process.

• 한국환경과학회지
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• 제15권6호
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• pp.513-525
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• 2006

In recent decades, biofiltration has been widely accepted for the treatment of contaminated air stream containing low concentration of odorous compounds or volatile organic compounds (VOCs). In this study, conventional biofilters packed with flexible synthetic polyurethane (PU) foam carriers were operated to remove toluene from a contaminated air stream. PU foams containing various amounts of pulverized activated carbon (PAC) were synthesized for the biofilter media and tested for toluene removal. Four biofilter columns were operated for 60 days to remove gaseous toluene from a contaminated air stream. During the biofiltration experiment, inlet toluene concentration was in the range of 0-150 ppm and EBRT (i.e., empty bed residence time) was kept at 26-42 seconds. Pressure drop of the biofilter bed was less than 3 mm $H_2O/m$ filter bed. The maximum removal capacity of toluene in the biofilters packed with PU-PAC foam was in the order of column II (PAC=7.08%) > column III (PAC=8.97%) > column I (PAC=4.95%) > column IV (PAC=13.52%), while the complete removal capacity was in the order of column II > column I > column III > column IV. The better biofiltration performance in column II was attributed to higher porosity providing favorable conditions for microbial growth. The results of biodegradation kinetic analysis showed that PU-PAC foam with 7.08% of PAC content had higher maximum removal rate ($V_m$=14.99 g toluene/kg dry material/day) than the other PU-PAC foams. In overall, the performance of biofiltration might be affected by the structure and physicochemical properties of PU foam induced by PAC content.

• Environmental Engineering Research
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• 제11권1호
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• pp.1-13
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• 2006

In this study, conventional biofilters packed with flexible synthetic polyurethane (PU) foam carriers were operated to remove toluene from a contaminated air stream. PU foams containing various adsorbents (e.g., zeolite, sepiolite, dolomite and barite) were synthesized for the biofilter media and their adsorption characteristics of toluene were determined. Adsorption capacity of PU-adsorbent foam was in the order of PU-dolomite ${\approx}$ PU-zeolite > PU-sepiolite > PU-barite. During the biofiltration experiment, influent toluene concentration was in the range of 0-160 ppm and EBRT (i.e., empty bed residence time) was 45 seconds. Pressure drop of the biofilter bed was 4-5 mm $H_2O/m$ column height. The maximum removal capacity was in the order of PU-dolomite > PU-zeolite > PU-sepiolite > PU-barite, while the complete removal capacity was in the order of PU-dolomite > PU-sepiolite > PU-zeolite > PU-barite. The better biofiltration performance in PU-dolomite foam was because PU-dolomite foam had lower density and higher porosity than the others providing favorable conditions for microbial growth. The results of biodegradation kinetic analysis showed that PU-dolomite foam had higher maximum removal rate ($V_m\;=\;11.04\;g$ toluene/kg dry material/day) and saturation constant ($K_s\;=\;26.57\;ppm$) than the other PU foams. This supports that PU-dolomite foam was better than the others for biofilteration of toluene.