• Environmental Engineering Research
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• 제24권3호
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• pp.363-375
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• 2019

Micellar-enhanced ultrafiltration (MEUF) is a surfactant-based separation technique and has been investigated for the removal of heavy metals from wastewater. The performance of heavy metals removal from wastewater through MEUF relies on membrane characteristics, surfactant properties, various operational parameters including operating pressure, surfactant and heavy metal concentration, pH of the solution, temperature, and presence of dissolved solutes and salts. This study presents an overview of literature related to MEUF with respect to the all significant parameters including membranes, surfactants, operating conditions and MEUF hybrid processes. Moreover, this study illustrates that MEUF is an adaptable technique in various applications. Nowadays water contamination caused by heavy metals has become a serious concern around the globe. MEUF is a significant separation technique in wastewater treatment that should be acknowledged, for the reason that removal of heavy metals contamination even at lower concentrations becomes achievable, which is evidently made known in the presented review. Hybrid processes presented the better results as compared to MEUF. Future studies are required to continue the experimental work with various combinations of surfactant and heavy metals, and to investigate for the treatment of concentrated solutions, as well as for real industrial wastewater.

• 대한환경공학회지
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• 제35권5호
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• pp.301-306
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• 2013

본 연구는 퍼클로레이트($ClO_4{^-}$)와 질산염($NO_3{^-}$)의 직접적인 처리방법으로 무산소/호기생물막반응조와 MF막에 의한 연속처리의 적용 가능성을 조사하였다. 생물막 처리공정은 첫 번째 단계로 퍼클로레이트와 질산염의 제거를 위해 무산소생물막반응조를 이용하였고 두 번째 단계로 이화적 퍼클로레이트와 질산염 환원을 위해 사용된 잔류탄소원의 제거를 위해 호기생물막반응조가 도입되었다. 그리고 마지막 단계로 탁도제거를 위해 중공사형 MF막을 적용하였다. 본 연구에서 102 ${\mu}g/L$ $ClO_4{^-}$와 61.8 mg/L $NO_3{^-}$ (14 mg/L $NO_3$-N)가 유입수로 주입되어 퍼클로레이트는 IC 검출농도 이하(5 ${\mu}g/L$ $ClO_4{^-}$)로 제거되었으며 질산염은 최종 처리수의 농도가 4.4 mg/L $NO_3{^-}$ (1 mg/L $NO_3$-N)로 제거되었다. 탄소원으로 사용된 과잉의 179 mg/L 유입 $CH_3COO^-$는 무산소생물막반응조의 유출수에서 117 mg/L, 호기생물막반응조의 유출수에서 11 mg/L로 감소하였다. 3 NTU의 유입 탁도는 무산소/호기생물막반응조의 유출수에서 1.5와 0.3 NTU였으며 최종 MF막의 유출수에서 0.2 NTU였다. 이 결과는 지표수와 지하수에 포함된 저농도 퍼클로레이트와 질산염 오염의 직접적인 처리방법으로 무산소/호기생물막반응조와 MF막의 연속처리가 적용될 수 있음을 의미하는 것으로 사료된다.

• Composites Research
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• 제29권5호
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• pp.243-248
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• 2016

열경화성 탄소 섬유 복합재료 분리판은 높은 기계적 특성뿐만 아니라 높은 내산성을 갖으나, 높은 제조단가 및 낮은 자체저항이 극복해야 할 가장 큰 장애물이다. 따라서 본 연구에서는, 열가소성 폴리머를 복합재료 분리판의 기지로 적용하여 분리판 생산성과 자체저항이 모두 증가된 열가소성 탄소 복합재료 분리판을 개발하였다. 전기 전도도 및 기계 강도를 증가시기키 위하여 평직 형태의 탄소 섬유 직물을 사용하였으며, 분리판의 자체 저항을 감소시키기 위하여 전도성 나노입자를 열가소성 기지에 혼합하였다. 개발된 분리판의 면적 비저항 및 기계물성을 고온 연료전지 작동 온도 및 스택의 체결압에 따라 측정하였다.

• Journal of Advanced Marine Engineering and Technology
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• 제38권10호
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• pp.1347-1353
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• 2014

It's possible for a human to breathe under water, if dissolved oxygen is effectively used. Fish can stay under water using the gill which extracts dissolved oxygen from water. Water includes small amounts of oxygen, so a human needs larger amounts of water to acquire oxygen enough for underwater breathing. The exhalation gas from a human is another method to get higher amounts of oxygen under water. It mainly composes of oxygen, nitrogen and carbon dioxide. So, if only carbon dioxide is decreased, the exhalation gas has good characteristics for breathing of a human under water. In this paper, composition of the exhalation gas from a human was analyzed using GC. Based on these results, the synthesized gas was prepared and mixed into water which was used for experimental devices to analyze separation characteristics of dissolved gases from water. Experimental devices included a water pump, a hollow fiber membrane module and a vacuum pump. The effects of pressure and water flow on separation characteristics of synthesized gas were investigated. The compositions of gases separated from water using synthesized gas were investigated using GC. These results expect to be applied to the development of underwater breathing technology for a human.

• 상하수도학회지
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• 제26권5호
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• pp.619-627
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• 2012

In order to determine reduction of greenhouse gas emissions (GHGs) when the submerged membrane bioreactor with granular sulfur (MBR-GS) is used in wastewater treatment plant (WTP), the amount of GHGs was compared and analyzed in the advanced treatment process of P wastewater treatment plant (WTP). The amount of GHGs was estimated by classifying as construction and operation phase in WTP. The amount of GHGs in construction phase was evaluated from multiplying raw materials by using carbon emission factors. Also the amount of GHGs in operating phase was calculated by using total electricity consumption and carbon emission factor. The construction of anoxic tank and secondary settling tank is unnecessary, because the MBR-GS conducts simultaneously the nitrification and denitrification in aeration tank and filtration by hollow fiber membrane. The amount of $CO_2$, $CH_4$, and $N_2O$ emitted by constructing the MBR-GS was 6.44E+06 kg, 8.16E+03 kg and 1.38E+01 kg, respectively. The result shows that the GHGs was reduced about 47 % as compared with the construction in the MLE process. In operating the MBR-GS, the electricity is not required in the biological reactor and secondary setting tank. Thus, the amount of $CO_2$, $CH_4$, and $N_2O$ emitted by operating in the MBR-GS was 7.39E+05 kg/yr, 5.80E+02 kg/yr and 2.44E+00 kg/yr, respectively. The result shows that the GHGs were reduced about 37 % as compared with the operation in the MLE process. Also, $LCCO_2$(Life Cycle $CO_2$) was compared and analyzed between MLE process and MBR-GS. The amount of $LCCO_2 $emitted from the MLE process and MBR-GS was 3.56E+04 ton $CO_2$ and 2.12E+04 ton $CO_2$, respectively. The result shows that the GHGs in MBR-GS were reduced to about 40 % as compared in the MLE process during life cycle. As a result, sulfur-utilizing autotrophic denitrification process (SADP) is expected to be utilized as the cost-effective advanced treatment process, owing to not only high nitrogen removal efficiency but also the GHGs reduction in construction and operation stage.

• Korean Chemical Engineering Research
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• 제49권2호
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• pp.250-255
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• 2011

본 연구는 막 분리 공정을 이용한 것으로 수소의 에너지원을 이용가능한 메탄을 정제하기 위해 바이오가스 중 이산화탄소와 메탄의 분리 및 황화수소의 제거하고자 한다. 막은 건/습식 상전이 법을 이용하여 중공사공 형태로 제조하고 표면 실리콘 코팅 후 모듈을 제조하였다. 제조된 중공사 막의 구조특성을 확인하기 위해 전자주사 현미경 관찰을 통하여 치밀한 표면과 망상구조의 비대칭 구조를 확인하였다. 압력과 온도가 증가함에 따라 이산화탄소의 투과도는 증가하였고, 이산화탄소와 메탄의 선택도 역시 증가하는 것으로 나타났다. 혼합가스의 경우 압력 및 온도가 증가함에 따라 메탄 농도는 100%에 가까웠으며 이산화탄소와 황화수소의 제거효율도 증가하였다. Retentate 유량증가와 압력 온도감소에 따라 메탄 농도 감소 및 회수율이 증가하는 경향을 나타내었다.

• 한국항공우주학회지
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• 제43권8호
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• pp.699-705
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• 2015

항공기가 적은 동력으로 장시간 체공을 하기 위해서는 높은 양항비(Lift Drag Ratio)와 구조경량화가 요구된다. 일반적으로 고고도 장기체공 비행기에는 가로세로비가 큰 날개가 적용된다. 또한 기체의 주요 구조물에 고강도, 고강성 탄소섬유복합재료를 사용하고, 날개의 표피(Skin)에 박막(Membrane) 소재인 얇은 마일러(Mylar)를 사용된다. 그 결과 날개 구조물이 다른 구조물에 비하여 유연해진다. 그리고 박막 소재인 얇은 마일러의 강성이 동적 안정성에 영향을 미치게 된다. 본 연구에서는 비선형 갭(Gap) 요소를 사용하여 마일러의 박막 특성을 모사하였다. 그리고 비선형해석 결과를 이용하여 등가강성을 갖는 선형 쉘(Shell) 요소로 등가모델링 하는 방법을 제시하였다. 선형 등가 쉘 모델은 멤브레인 요소법를 이용한 비선형해석 결과와 비교하여 결과의 타당성을 검증하였다. 제안된 선형등가 쉘 모델은 모드 해석에 적용하여 마일러의 기계적 물성이 고유진동수에 미치는 영향을 평가하였다.

• Membrane and Water Treatment
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• 제11권4호
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• pp.313-321
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• 2020

ACF preparation from different materials and its application in constructed wetlands for wastewater treatment has been focused in environmental field. Different materials have been used to prepare ACF around the world. This study aims to prepare, characterize and use of ACF from loofah for removal of Tetracycline from water through composite vertical flow constructed wetlands. ACF was prepared and it was tested for characterization, later it was used for removal of Tetracycline from water through composite vertical flow constructed wetlands. In composite vertical flow constructed wetlands, three HRTs were set according to the experiment, 1D, 2D, and 3D is individually. Samples were transported immediately from collection point to laboratory for analyzing. Samples were measured for Tetracycline (TC), Total Phosphorus (TP), and Total nitrogen and COD. Tetracycline absorbance with respective 356nm was obtained good and HRT is important factor. Results show that composite vertical flow constructed wetlands with ACF from luffa is best option and it is recommended to study further deep analysis.

• Membrane and Water Treatment
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• 제10권3호
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• pp.213-221
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• 2019

Anaerobic digestion (AD) has been widely used to valorize food waste (FW) because of its ability to convert organic carbon into $CH_4$ and $CO_2$. Korean FW has a high content of fruits and vegetables, and efficient hydrolysis of less biodegradable fibers is critical for its complete stabilization by AD. This study examined the digestates from different anaerobic digesters, namely Rs, Rr, and Rm, as the inocula for the AD of vegetable waste (VW) and cellulose (CL): Rs inoculated with anaerobic sludge from an AD plant, Rr inoculated with rumen fluid, and Rm inoculated with anaerobic sludge and augmented with rumen fluid. A total of six conditions ($3\;inocula{\times}2\;substrates$) were tested in serial subcultures. Biogas yield was higher in the runs inoculated with Rm than in the other runs for both VW (up to 1.10 L/g VS added) and CL (up to 1.05 L/g VS added), and so was biogas production rate. The inocula had different microbial community structures, and both substrate type and inoculum source had a significant effect on the formation and development of microbial community structures in the subcultures. The overall results suggest that the bioaugmentation with rumen microbial consortium has good potential to enhance the anaerobic biodegradability of VW, and thereby can help more efficiently digest high fiber-content Korean FW.

• 한국환경과학회지
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• 제24권12호
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• pp.1629-1637
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• 2015

To develop various usable water from coal seam gas (CSG) water that needs to be pumped out from coal seams for methane gas production, a feasibility study was carried out, evaluating and analysing a recent report (Coal Seam Gas Water Management Policy 2012) from Queensland State Government in Australia to suggest potential CSG water treatment options for fit-for-purpose usable water production. As CSG water contains intrinsically high salinity-driven total dissolved solid (TDS), bicarbonate, aliphatic carbon, $Ca^{+2}$, $Mg^{+2}$ and so on, it was found that appropriate treatment technologies are required to reduce the hardness below 60 mg/L as $CaCO_3$ by setting the reduction rates of $Ca^{+2}$, $Mg^{+2}$ and Na+ concentrations, as well as TDS reduction. Also, Along with fiber filtration and membrane separation, an oxidation degradation process was found to be required. Along with salinity reduction, as CSG water contains organic compounds (TOC: 248 mg/L, $C_6-C_9$: <20 mg/L and $C_{10}-C_{36}$: <60 mg/L), compounds with relatively high molecular weights ($C_{10}-C_{36}$) need to be treated first. Therefore, this study suggests a combined system design with filtration (Reverse osmosis) and oxidation reduction (electrolysis) technologies, offering proper operating conditions to produce fit-for-purpose usable water from CSG water.