• Journal of Korean Society of Environmental Engineers
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• v.35 no.3
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• pp.226-232
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• 2013

Several pretreatment processes such as softening, coagulation and precipitation, activated carbon adsorption, ion-exchange and neutralization processes were studied to remove organics and inorganics for selection of the RO based reusing system of metal industry wastewater. The effects of the hydrophobic/hydrophilic fractions of the organics on DOC removal were tested and used to optimize the combination process. Among various pretreatment processes, softening could reduce 93.4% of hardness and could remove all hydrophobic organics from the effluent of metal industry wastewater. Softening followed by coagulation process could reduce DOC (Dissolved Organic Carbon) from 5.1 mg/L to 1.6 mg/L. In addition, as a result of physiochemical pretreatment to raw wastewater of metal industry, neutralization with NaOH showed an efficient removal of iron and TDS (Total Dissolved Solids) without increase in the hardness.

• Journal of Korean Society of Forest Science
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• v.79 no.4
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• pp.367-375
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• 1990

In order to determine the effects of bedrock, organic matter, calcium and iron oxide on the soil aggregation, this research has performed with soils from bedrock regions of Limestone, Granite and Granite gneiss. This research was also to estimate how organic matter, calcium and iron oxide influence on soil aggregation under different forest conditions in various bedrock regions. And it also had a purpose to rate physical factors relevant to soil aggregation, their characteristics and aggregate diameter which closely relates to stabilities in the process of soil erosion. The following conclusions have been drawn in response to the overall research objectives. The rates of the soil aggregation on different bedrock regions were 21% in Limestone bedrock, 19.8% in Granite bedrock and 9.9% in Granite gneiss bedrock. A main factor in soil aggregation was the orgainc matter content in soils and the rate of soil aggregation increased in the constant proportion with the organic matter content. The relation could be formulated into Y=4.31X-4.37(Y : aggregation ratio X : organic matter content). The soil aggregation ratio under the deciduous forests eras higher than that under the coniferous forests. It was considered that this resulted from differences in organic matter content. Soil aggregates with larger diameter than 0.5mm were found more in Limestone bedrock than other smaller size soil aggregates of 0.25mm diameter were more distributed in Granite gneiss bedrock. Granite bedrock region had normal distribution in soil aggregate sizes with the highest frequency of 0.5mm diameter. Calcium and iron oxides had only partial influences on the soil aggregation in some specific conditions. But in Limestone bedrock region calcium influenced on the soil aggregation with the organic matter content.

• KSCE Journal of Civil and Environmental Engineering Research
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• v.29 no.5C
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• pp.229-237
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• 2009

A conventional way of backfilling has used sand or in-situ soil. It not only requires substantial amount of time and cost but also makes it particularly difficult to fill the bottom part and small cracks of a pipe. To address the problem with the conventional method of compaction, liquefied stabilized soil was proposed as an alternative because it reuses in-situ soil which can ensure sand supply while adjusting flowability and strength of the soil with design of mix proportion. With an aim to identify the mixing properties of liquefied stabilized soil depending on the organic content of in-situ soil, this study conducted indoor tests of material segregation, flowability, strength, and permeability by changing humic acid content of the soil. The results revealed that material segregation and flowability increased proportionally while strength decreased with the increased amount of humic acid. In the mean time, permeability of liquefied stabilized soil wasn't affected by organic content.

• Proceedings of the Korea Water Resources Association Conference
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• 2022.05a
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• pp.397-397
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• 2022

오늘날 급격한 인구증가 및 도시화로 인해 음식물류 폐기물 발생량이 크게 증가하였으며, 음식물류 폐기물에서 발생되는 음폐수의 적절한 처리방안에 대한 관심이 증가하였다. 혐기성 소화(Anaerobic digestion; AD)는 음폐수의 바람직한 처리방법으로 알려졌지만, 긴 처리기간 및 공정 불안정 등의 문제로 개선이 필요하며, 그 중 기존 AD에 보조 반응조를 추가한 보조 미생물전기화학적 혐기성소화(Auxiliary bioelectrochemical anaerobic digestion; ABEAD)가 적절한 개선방안으로 제시되었다. 하지만 아직 20 L 이상 용량에서의 연구는 이뤄지지 않았으며, 따라서 본 연구에서는 100 L의 용량에서 ABEAD의 성능향상을 평가하고 규모증가에 따른 성능변화를 비교하였다. 반응조는 AD와 ABEAD로 구성되었다. 유효용량 100 L, 유기물부하율 4 kg/m³/d, HRT 20 days 및 중온소화(35℃) 조건으로 운전하였으며, AD는 기계적 교반, ABEAD는 기계적 교반 및 펌프를 통한 bulk 용액 순환이 이뤄졌다. ABEAD의 전극재질은 SUS304를 사용하였고, 0.4V의 전압을 공급하였다. 성능비교는 pH, 휘발성지방산(Volatile fatty acids; VFAs), 유기물제거율 및 메탄 생성량을 비교해 수행하였다. 실험결과 AD는 pH 및 VFAs가 각각 평균 7.37 및 3,880 mg/L, ABEAD는 각각 평균 7.5 및 2,870 mg/L로 VFAs의 빠른 처리를 통해 공정안전성 향상되었고, 유기물제거율 및 메탄생성량의 경우 AD는 각각 평균 65.8 % 및 85.1 L/d, ABEAD는 각각 평균 76.1 % 및 108.1 L/d로 유기물의 빠른 처리 및 메탄전환이 이루어져 비교적 큰 규모에서도 ABEAD의 성능향상이 나타남을 확인하였다. 또한 이전 소규모 연구들과 비교를 통해 규모에 따른 성능향상폭을 비교했을 때에도 큰 차이가 나지 않는 것으로 판단되며, 따라서 ABEAD는 BEAD 기술의 상용화 및 적용에 적합한 것으로 사료된다.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2002.05b
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• pp.275-276
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• 2002

CaO는 물과 반응하여 발열반응을 일으켜서 CaO에 코팅된 계면활성제를 용해시키며 그리고 규산소다에 흡착된 중금속과 유기물을 고정화 시키는 역할을 담당한다. 그리고 규산소다는 물과 가수분해하여 다공성이 되면서 중금속과 유기물 등을 흡착시키는 역할을 담당한다. 또 CaO에 코팅된 계면화성제는 기름과 반응성이 우수하므로 $80^{\circ}C$～$90^{\circ}C$에서 용해하여 기름과 반응하는 특성을 갖고 있다. 미분 슬래그는 보간 중에 암석화되는 과정을 도와 주므로 시간이 경과하면 pH가 점점 중성으로 변화하는 현상을 보여 주었다.

• Journal of Soil and Groundwater Environment
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• v.14 no.1
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• pp.44-50
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• 2009

The occurrence of endocrine disrupting compounds (EDCs), chemicals that interfere with human hormone system, are increasing in the freshwater, waste water and subsurface as well. In this study, we determined the reactivity of three EDCs in the presence of birnessite. In aqueous phase, bisphenol A, 2,4-dichlorophenol and 17${\beta}$-estradiol, which possesses phenoxy-OH, were very rapidly transformed by birnessite: up to 99% of initial concentrations (50 mg/L for bisphenol A, 100mg/L for 2,4-dichlorophenol, and 1.5mg/L for 17${\beta}$-estradiol) were destroyed within 60 minutes. Especially, bisphenol A was the most reactive chemical, disappearing by 99% in a few minutes. The reaction occurred on the surface of birnessite, showing a linear increase of first-order kinetic constants with the increase of the surface area of birnessite. In soil slurry phase, the reactivity of birnessiteto EDCs was faster than in aqueous phase probably due to the cross coupling reaction of phenoxy radicals with soil organic matter. Considering the rapid transformation of the EDCs in the both phases, this oxidative cross coupling reaction mediated by birnessite would be an effective solution for the remediation of EDCs in environmental media, especially in soil.

• Journal of the Korean Applied Science and Technology
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• v.37 no.2
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• pp.250-259
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• 2020

The solubilization constant (K_s) was determined by the UV-Vis method to investigate the interaction between organic matter (solubilized substance) and surfactant in solubilization. Solubilization constants and thermodynamic functions, according to the hydrophobic interaction between organic mater (4-alkylanilines with different alkyl substituent length) and cationic surfactants (DTAB, TTAB, and CTAB, having different hydrophobic lengths), were measured and calculated at various temperatures and compared with each other. As a result, the hydrophobic interactions between organic matters and cationic micelles increased with increasing the chain length of solute's substituent as well as surfactant's hydrophobe. However, the hydrophobic effect by the alkyl substituent of organic matter was greater than the hydrophobic effect by the surfactant. In addition, the results of the calculated thermodynamic functions showed that 4-alkylaniline was solubilized at the deep place in the micelle and its solubilization was greatly dependent on both the hydrophobic effects of organic matter and surfactant. At the calculated iso-structural temperature, the difference between the maximum and minimum values was less than 1K within the experimental conditions.

• Journal of Korean Society of Environmental Engineers
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• v.28 no.10
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• pp.1024-1030
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• 2006

Genus Nitrospira and Nitrobacter species are the key nitrite-oxidizing bacteria(NOB) in nitrifying wastewater treatment plants. It has been hypothesized that genus Nitrospira are K-strategists(low $K_6$ value) that can exploit low amounts of nitrite more efficiently than Nitrobacter. In contrast, Nitrobacter species are r-strategists(high $V_{max}$) that can grow faster than Nitrospira. It has also been known that the availability of organic compounds and dissolved oxygen as well as nitrite affects the distribution of NOB. In this study, we determined the distribution and competition of NOB in wastewater nitrification systems where nitrite, organic compounds, and dissolved oxygen concentrations were compositively varied. For the purpose, several compounds of the laboratory-scale nitrificaiion bioreactor and full-scale $A_2O$ wastewater treatment plant and their distribution of NOB were analyzed and compared. The analysis showed that Nitrobacter was the dominant NOB in nitrification bioreactor where average nitrite was maintained at 5 mg-N/L with very low organic concentration in aerobic condition, whereas Nitrospira was the dominant NOB in full-scale $A_2O$ plant where nitrite was maintained very low and organic compounds were maintained relatively high in alternating aerobic-anoxic condition. The result indicates that nitrite concentration is more critical factor than organics and dissolved oxygen which determines the dominant NOB in nitrification system and it is confirmed that Nitrospira and Nitrobacter showed the characteristics of r-strategist and K-strategist, respectively.

• Journal of the Korea Organic Resources Recycling Association
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• v.11 no.1
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• pp.127-128
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• 2003

본 연구는 퇴비화 과정 중 난용성 인산의 가용화와 무기태 인산의 변화를 알아보기 위하여 수행하였다. 비료와 퇴비중의 인산형태는 다른 성분들보다 토양에 흡착 또는 고정되거나 불용화 되는 양이 많아 작물의 흡수량이 적다. 시비된 인산의 흡수율은 낮고, 그 대부분은 난용화되기 때문에 토양에 축적되거나 세탈과 용탈에 의해 수질을 오염화시키는 주원인이 되고 있다. 퇴비화 과정중의 인산형태별 함량변화를 분석조사하여 작물에 시비되는 인산비료와 퇴비의 시용량을 적절하게 조절하여 인산의 과잉 시비량을 저감시키기 위한 연구이다. 돈분을 원료로 한 퇴비화 과정에서 단계별로 퇴비시료를 채취하여 총인산(T-P), 유효인산(Avail. -P)과 무기태인산분획별(Ca-P, Al-P, Fe-P)로 분석한 결과는 다음과 같다. 퇴적더미의 초기부피는 570L였으며, 약 2개월간의 퇴비화를 통해서 시료채취와 미생물등의 분해작용으로 최종부피는 430L정도로 감소하였다. 이는 초기의 부피보다 25% 감소하였다. 퇴적더미의 분해로 인한 용적밀도의 변화를 고려하면, 총인산 함량은 초기 약 17,500mg/kg에서 최종시료는 22,500mg/kg로 증가되었다. 또한 퇴비화가 진행됨에 따라 인산의 가용태가 증가하는 결과를 보였으며, 초기의 유효인산이 4,500mg/kg에서 최종시료에서는 8,900mg/kg으로 증가되었다. 그리고 무기태 인산분획별 인산의 형태별 변화를 조사한 결과, 퇴비화 과정 중 Ca-P의 경우 pH와의 중요한 상관관계를 갖고 있었다. 유기물분해를 통해 유리된 인산과 Ca은 난용태로 전환되는데, 초기의 약 10일 동안 Ca-P의 감소원인은 pH의 감소로 인한 Ca이 유리되는 정도가 낮기 때문인 것으로 해석된다. 초기 Ca-P형태의 인산함량은 11,900mg/kg으로 Fe-P와 Al-P보다 많았다. 또한 퇴비화가 안정화되어 부숙된 최종시료의 무기태 인산분획물 중 Ca-P는 18,000mg/kg로 증가하였으며, Ca-P>Al-P>Fe-P의 순 이었다. 그러나 Al-P와 Fe-P 형태의 무기태인산은 초기의 함량비율보다 다소 감소한 결과를 보였다. 결론적으로, 퇴비화과정 중 단계별 인산함량의 형태전환을 분석한 결과 총인산의 함량은 퇴비화가 안정화될수록 부피감소로 인한 인산함량이 증가하는 경향을 보였지만, 유기물질의 분해로 인한 원료내 인산의 형태가 불용태와 난용태에서 가용태 인산으로 전환되는 것을 도출하였다. 또한 무기태 인산분획물에서는 Ca-P 인산형태가 퇴비화가 진행될수록 증가한다는 결과를 얻었으며, Fe-P와 Al-P는 분해된 유기물의 킬레이트작용으로 감소되었다고 판단되며, 그 존재형태가 경쟁적임을 알 수 있었다. 따라서 화학비료와 퇴비의 시용이 병행될 경우에는 퇴비의 가용태 인산함량뿐만 아니라 무기태 인산의 함량을 분석한 후 인산질비료의 시비량을 조절해야할 것으로 판단된다.

• Journal of the Korean Society for Marine Environment & Energy
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• v.9 no.2
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• pp.72-78
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• 2006

Effect of organic loading rate on digester performance was evaluated under the conditions of same surface area/reactor volume ratio and different reactor diameter. At the low loading rate of $0.4\;kg\;COD/m^3{\cdot}d$, high rate of organic removal could be obtained regardless of reactor diameter. It can be estimated that reactor configuration can not affect reactor performance at the low loading rate. However, different performance depending on reactor diameter was observed at the organic loading rate of $6\;kg\;COD/m^3{\cdot}d$. That is, volatile acid accumulation and low COD removal efficiency was observed in reactor having 6.4 cm diameter, while volatile acid was not accumulated at all and high COD removal efficiency was observed in reactor having 3 cm diameter. Such a difference of reactor performance depending on reactor diameter can be explained that sludge bed can be fluidized by evolved gas bubble in narrow reactor while sludge bed can not be fluidized by evolved gas bubble only in wide reactor. At a high organic loading rate of $20\;kg\;COD/m^3{\cdot}d$, it can be judged that there is no relation between reactor configuration and reactor performance because all reactors showed very low COD removal efficiencies regardless of reactor diameter. Sludge bed fluidization is one of the most important factors in achieving efficient start-up of anaerobic digester. Narrow and tall type reactor is favorable condition for making sludge bed fluidization at a constant surface area/reactor volume ratio. Thus, it can be judged that reactor configuration and sludge bed fluidization have great influence to reactor performance.