• Proceedings of the Korea Technical Association of the Pulp and Paper Industry Conference
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• 2001.04a
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• pp.26-26
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• 2001

사무용 고지의 상당량을 차지하는 복사고지는 열과 압력으로 융착된 합성고분자 물질인 토너를 함유하고 있으며 이들 토너는 펄핑 후 크고 판상 형태의 잉크 입자를 형성하 여 기존의 부유부상법으로 제거가 곤란한 문제점을 지니고 있었다. 이러한 문제점을 극복하 는 방안으로 응집제를 이용하는 방법을 검토하였다. 복사기용 인쇄 잉크로 널리 사용되는 토너 업자는 낮은 표면에너지를 가지는 소수 성 물질이므로 같은 표면 특성을 가지는 소수성 물질과 서로 잘 결합한다. 따라서 소수성의 응집제를 이용하면 분리된 토너 잉크업자를 응집시킬 수 있으며, 응집된 토너 응집체는 스 크린 또는 클리닝 같은 정선 공정을 이용하여 제거가 가능할 것이다. 따라서 복사고지를 효 과적으로 재활용할 수 있는 탈묵방법으로 응집제를 이용하여 토너 입자를 조대한 웅집체로 형성시키고 이를 기존 탈묵방법인 스크린처리로 제거하는 방법을 검토하였다. 본 연구에서는 고급알코올의 하나언 1 -octadecanol을 이용하여 기존의 탈묵 방법 인 부유부상법으로는 제거가 곤란한 토너 잉크의 업자를 웅집시켜 구형의 조대한 응집체로 형성시켜 이를 제거하는 기술에 대하여 연구하였다. 펄핑 시의 온도를 70C의 고온으로 설 정한 경우 토너 입자가 유리전이온도에 이르게 되며 이들 토너 입자는 응집제에 의하여 웅 집되어 구형으로 성장하는 특정이 뚜렷하였으며, 토너 응집체의 크기는 최대 800 µm에 이 르기까지 조대하게 성장하였다. 또한 슬롯 폭 $250\mu\textrm{m}$의 진동 스크린 처리에 의한 토너 제 거 효율 측정 결과 역시 이들 토너 업자 웅집체의 형태가 구형임을 보여주었다. 해리 및 응 집 처 리 시 의 pH를 3으로 조정 하였을 때 토너 입 자가 웅집 제인 1 -octadecanol에 의 해 가장 효과적으로 구형의 조대한 웅집체를 이루는 것으로 나타났으며, 스크련을 통한 토너 웅집체 제거효율이 향상되었다. 복사고지 내에 포함되어 있는 전분 또는 사이즈제는 웅집 효과를 떨어뜨리는 주요 인으로 나타났다.

• Journal of Korean Society of Environmental Engineers
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• v.27 no.3
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• pp.323-329
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• 2005

In this paper, performance of a hybrid sequential aerobic-anaerobic natural system was investigated. Continuous aerobic and anoxic conditions were created by alternatively placing waste stabilization pond (WSP) and wale. hyacinth pond (WHP). Two pilot-scale treatment lines were built and operated; The first consists of WSP integrated with WHP and the second of WSP connected with Dark Pond(DP), namely control system ponds which were used to examine the effects of water hyacinth on nitrification and de-nitrification. The overall performance in nitrogen was 86% reduction in WSP-WHP and 36% in WSP-control pond system. Nitrogen was mostly removed by nitrification and de-nitrification which simultaneously occurred in the same water hyacinth ponds. For the de-nitrification, benthic layer was found out to be adequate support as a carbon source. In addition, WSP-WHP system was very effective in reducing phosphorus. Overall P removal efficiency in WSP-WHP is 81%, while it is only 16% in WSP-control. difference in phosphorus reduction between those two systems is thought to be caused by the plants and probably their roots producing extra-cellular materials, but these aspects need to be further studied.

• Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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• 2008.06a
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• pp.389-389
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• 2008

나노-스피어 리소그래피는 기존 리소그래피 방법에 비해 나노 크기의 패턴을 저비용에 공정이 간단하고, 대면적 패터닝이 가능하다는 장점이 있다. 본 논문에서는 나노-스피어 리소그래피 공정을 이용하여 실리콘 기판 위에 2차원 광자결정 구조를 제작하였다. 실리콘 기판 위에 직경이 500 nm 인 폴리스티렌 나노-스피어를 스핀 코팅 방법으로 단일막을 형성하였다. 스핀코팅 조건은 스핀속도와 시간을 조절하여 1단계는 400 rpm에서 10초, 2단계는 800 rpm에서 120초, 3 단계는 1400 rpm 에서 10초로 공정하였다. 그리고 산소 플라즈마를 이용한 반응성 이온 식각공정으로 폴리스티렌 나노-스피어의 크기를 조절할 수 있었으며, 이때 실리콘 기판 위에 형성된 다양한 크기의 폴리스티렌 나노-스피어 단일막은 금속막 증착시 마스크의 역할을 하게 된다. 금속막의 증착은 RF 마그네트론 스퍼터링 시스템을 이용하였으며, 공정 조건은 RF power를 100W, 공정 압력을 5 mTorr, Ar 유량을 10sccm으로 하였다. 스퍼터링 공정 후 폴리스티렌 나노-스피어를 제거함으로써 2 차원 광자결정 구조를 제작할 수 있었다. 실험 결과 단일막으로 형성된 폴리스티렌 나노-스피어의 크기를 조절함으로써 다양한 2차원 광자결정 구조 제작이 가능함을 확인할 수 있었다.

• Proceedings of the Korean Nuclear Society Conference
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• 1995.05b
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• pp.929-936
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• 1995

LOMI 제염제의 전기화학적 제조공정 중 전하운반체의 역할 및 V$^{3+}$ 이온의 침전현상을 방지하기 위하여 첨가되는 과량의 formic acid 는 제염제 제조시에는 중요한 역할을 하지만 제염 폐기물의 양을 증가시키는 요인이 되기도 한다. EPRI 공정에서는 formate : V 의 비율(FVR)이 10:1 인 조건에서 V$^{2+}$-formate 를 제조한 후 음이온 교환 수지를 이용하여 과량의 formate 를 제거하는 공정을 사용한다. 이러한 방법으로 줄일 수 있는 FVR의 한계가 약 2.5 : 1 이다. 본 연구에서는 제염제 중 formate 의 양을 더욱 줄일 수 있는 방법으로써 V$^{2+}$-formate 제조시 용액 중에 picolinic acid를 미리 첨가하는 영향을 조사하였다. V$^{2+}$ 이온의 농도가 0.1 M 일 때 FVR 를 1.5:1 까지도 줄일 수 있음을 확인하였다.

• Journal of Korean Society of Environmental Engineers
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• v.28 no.12
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• pp.1280-1286
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• 2006

Three different virgin activated carbons made of each coal(Calgon), coconut(Samchully) and wood(Picabiol) based activated carbon(AC) were tested for an adsorption performance of 1,4-dioxane in a continuous adsorption column. Breakthrough behavior was Investigated that the breakthrough points of coal, coconut and wood based AC were observed as 3600 bed volumn(BV), 1440 BV and 144 BV respectively. Adsorption capacity(X/M) of coal, coconut and wood based AC was observed. The reported results of adsorption capacity showed that coal based AC was highest(578.9 ${\mu}g/g$), coconut based AC was intermediate(142.3 ${\mu}g/g$) and wood based AC was lowest(7.4 ${\mu}g/g$) due to increasing specific surface area. Moreover, carbon usage rates(CURs) for coal, coconut and wood based AC had been shown as 0.48 g/day, 1.41 g/day and 6.9 g/day respectively. The constant characteristic of the system, k of coal based AC was found to be 91.5 and k of coconut based AC was found to be 17.9. Removal efficiencies of 1,4-dioxane with different ozonation dosages(2 and 5 mg/L) for 20 min ozonation had been shown 38% and 87% respectively. There was no observation for biological removal of 1.4-dioxane by attached micro-organisms when used(3.1 years and over 5 years) biological activated carbon(BAC) without pretreatment of oxidation were employed. When a combination of ozonation(2 mg/L and 5 mg/L) and BAC process for $10{\sim}30$ min was applied, removal efficiency for 1,4-dioxine increased only $2{\sim}6%$ compared to only applying ozonation. Therefore removal efficiency of BAC process prior to using oxidation was proven to negligible. Consequently, the results presented in this paper provide a better insight into the adsorption performance of 1,4-dioxane. This observation suggests that using virgin activated carbon made of coal is the best selection for removal of 1,4-dioxane in the water treatment for an advanced treatment. It is clear from this research that longer EBCT for ozonation or higher ozone concentration are more effective operation methods for removal of 1,4-dioxane than longer EBCT in the BAC process.

• KSBB Journal
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• v.22 no.4
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• pp.191-196
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• 2007

This study used biofilm process, which needs simple operation, maintenance and smaller facility area than conventional activated sludge process with the small plant operation, in the treatment of increasing sewage with the rapid industrial growth. The reactor used in this study consists of one anaerobic and one aerobic chamber filled with waste ceramic and waste vinyl as media and the treated sewage was from restaurant source. The experiment was scaled up from lab. to pilot scale and lasted for about 100 days. We focused on the removal efficiency of organics, nitrogen and phosphorus with constant HRT and continuous aeration. The removal efficiency of $BOD_5$ and SS were 94.33% and 87.77% respectively, which was a satisfaction level. However the removal efficiency of $COD_{Cr}$ was 81.46% somewhat below the desired level of 90%, and that of T-N and T-P showed 71.92% and 21.10% respectively, that was below the expected value. The removal efficiency of $COD_{Cr}$ and T-N in the pilot scale was about 10% low compared with the lab.-scale.

• Journal of the Korea Organic Resources Recycling Association
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• v.29 no.1
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• pp.5-17
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• 2021

This study is a literature review on the recovering phosphorus from Incinerated Sewage Sludge Ash(ISSA), which has relatively high content of phosphorus. Experimental conditions and influencing factors related to the recovery of P and removal of heavy metals by wet and thermochemical methods were discussed. For the practical application of the recovery of P from ISSA, an integrated process linked to incineration facilities is required in terms of economy from the perspective of the entire system including disposal of wastewater and residues generated during the recovery process, and minimizing added chemicals and energy consumption.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.5
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• pp.895-905
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• 2000

This study was performed to investigate the removal efficiencies of pollutants at various filtration rates and the quality of the filtered water along the depth of filter media during treatment of a BNR process effluent by a dual-media gravitational rapid filtration. The results of the experiments at filtration rates of 200, 300 and 400 m/day using the effluent of a pilot scale 4-stage BNR plant showed that turbidity of the filtered water was below 2.6 NTU, satisfying the Korean standard for water for reuse. Even though the SS removal efficiency deteriorated as the filtration rate increased, the average SS concentration of the filtered water was 1.3 mg/L at all filtration rates. Simultaneous biological nitrification and denitrification was observed with nitrification efficiencies of 17.4, 18.8 and 14.3%, and denitrification efficiencies of 32.3, 27.7 and 21.4% respectively at filtration rates of 200, 300 and 400 m/day. At the latter period of each filtration cycle, the effluent T-P concentration was higher than influent T-P concentration by 6.1 to 21.4% due to phosphorous release under DO-deficient condition.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.3
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• pp.587-595
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• 2000

The most problems of domestic sewage for BNR(Biological Nutrients Removal) process are deficiency of carbon source and low C/N ratio. Primary sludge fermentation is seemed to be one of the best solutions producing biodegradable organic substrates. Soluble organic materials from sludge fermentation are mainly SCFAs(Short-Chain Fatty Acids) with 2~5 carbon atoms. In this research, it was attempted to apply $A_2/O$ process with the side-stream acid fermenter to improve the nutrients removal efficiency. The result showed that proper SCFAs production is about 3.000mg/L with SRT of 4~5 days. SCFAs yield of approximately 0.10~0.16 mg SCFAs(as COD) per mg of primary sludge(as COD) were achieved. The ratio of acetic. propionic. butyric and valerie acid were 1, 0.7, 0.5 and 0.6. Significant improvements of nutrients removal over 70% in BNR process were observed. thus will reduce the demand for chemical dosing to increase nutrients removal efficiency. When the fermentate was entered $A_2/O$ process, the ratio of phosphate release to substrate uptake amounts to $0.34gPO_4-Pg^{-1}COD$.

• Journal of Korean Society of Environmental Engineers
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• v.27 no.11
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• pp.1168-1173
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• 2005

Pilot scale vertical-type membrane bioreactor was operated to examine the effect of $FeCl_3$ injection on the removal of organics, nitrogen and phosphorous, and additionally trans-membrane pressure (TMP) was observed. The membrane type was hollow fiber membrane with pore size of $0.25\;{\mu}m$, and the material was polytetrafluoroethylene (PTFE). The membrane permeate was continuously removed by a pump under a constant flux ($25\;L/m^2/h$). Air back-flushing technique were adopted to reduce fouling. As a result, TMP was increased more slowly than that of the operation without air back-flushing, During long-term operation, approximately 310 days, the injection of $FeCl_3$ was effective not only in removing phosphorous chemically but also in reducing TMP increase. Furthermore, while the average COD and T-N concentration of the effluent without $FeCl_3$ injection was 14.3 mg/L and 6.0 mg/L respectively, that of effluent with $FeCl_3$ was 11.3 mg/L and 6.0 mg/L respectively, which confirmed the effects of $FeCl_3$.