• Journal of Climate Change Research
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• v.7 no.3
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• pp.249-256
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• 2016

Porous $Al_2O_3$ hollow fiber membranes were successfully prepared by dry-wet spinning/sintering method. The SEM image shows that the $Al_2O_3$ hollow fiber membrane consists mostly of sponge pore structure. The contact angle and the breakthrough pressure were $126^{\circ}$ and 1.91 bar, respectively. This results indicate that the $Al_2O_3$ hollow fiber membranes were successfully modified to hydrophobic surface. The hydrophobic modified $Al_2O_3$ hollow fiber membranes were assembled into a membrane contactor system to separate $CO_2$ from a model gas mixture of the flue gas at elevated gas velocity. The $CO_2$ absorption flux was enhanced when the gas velocity increased from $1{\times}10^{-3}$ to $6{\times}10^{-3}$ m/s. Whereas the $CO_2$ absorption flux was decreased with the number of hollow fiber membrane of a module because of the concentration polarization. Furthermore, we developed an lab-scale $Al_2O_3$ hollow fiber membrane contactor modules and their system (i.e., $CO_2$ absorption using the $Al_2O_3$ membrane and monoethanolamine (MEA)) that could dispose of over $0.02Nm^3/h$ mixture gas (15% $CO_2$) with the removal efficiency higher than 95%. The results can be useful in a field of the membrane contactor for $CO_2$ separation, helping to design and extend a equipment.

• Membrane Journal
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• v.33 no.6
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• pp.369-376
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• 2023

In this study, the alternative to the energy-intensive conventional vacuum distillation process, an eco-friendly and energy-efficient pervaporation separation was employed in 1,2 hexane diol/water (HDO/water) mixture. The crosslinked PVA-glutaraldehyde was coated inside the alumina hollow fiber membrane (Al-HF). In the HDO/IPA pervaporation separation, optimization of the membrane concerning PVA/GA ratio, curing temperature, and pervaporation operating condition were performed. In the long-term stability test, the sustainable pervaporation separation performance giving flux in the range of 1.90~2.16 kg/m²h, and water content in permeate was higher than 99.5% (separation factor = 68) was obtained from the PVA/GA (molar ratio = 0.08, curing temperature = 80℃) coated Al-HF membrane from HDO/water (25/75, w/w, %) mixture at 40℃. Therefore, this work provides potential and inspiration for PVA-based membranes to mitigate excessive energy requirements in HDO/water separation by pervaporation.

• Proceedings of the Korea Concrete Institute Conference
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• 2009.05a
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• pp.143-144
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• 2009

This study is a development of new PSC girder overcomes weakness of the existing PSC girder and has advantage of construction mark, economical efficiency and maintenance. The gole of this study is reducing dead-load and long-span as HWPC girder has same section through hole and multi-prestressing.

• Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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• 2003.05b
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• pp.115-118
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• 2003

본 고에서는 현재 중국에서 추진되고 있는 고등교육 부문에 대한 진흥시책을 "211공정(工程)"을 중심으로 조망해보았다. 등소평의 중점대학 육성 구상에 따라 중국 국내의 제반 여건을 고려하여 "구오(九五)"기간 중에 개시된 "211공정(工程)"의 주요내용은 국가중점대학(國家重點大學)과 국가중점학과(國家重點學科) 건설 사업이다. 강역민(江澤民) 집권 후에는 "과교흥국(科敎興國)"을 기본국책으로 설정하여 교육부(敎育部)내의 과학기술사(科學技術司)에서 기지건설과 인재양성을 중점적으로 담당하면서 과학기술교육을 고등교육 발전의 기본축으로 삼아 적극적으로 추진하고 있다. 중국의 경우 이와 같은 국가 주도적인 진흥책을 중국공산당중앙위원회(중공중앙(中共中央))와 국무원의 방침 결정에 따라 집중육성(중점(中点)) 항목 결정 및 관리를 국무원 산하 유관부문이 상호 협조 하에 분담하여 지원하고 있다.

• 기계와재료
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• v.10 no.2 s.36
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• pp.129-137
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• 1998

원자력발전소 기기의 구조, 건전성 확보를 위해 기기가 적절한 기술기준에 따라 제작, 설치 및 운전되고 있는지 여부를 정부가 인정한 제3자에 의해 시행되는 검사를 원자력공인검사라하며 세부적으로 기기의 제작 및 시공단계에서 수행되는 공인검사를 제작/시공공인검사, 시운전 및 운전단계에서 수행되는 공인검사를 가동전/중공인검사로 분류하여 검사를 수행하고 있다. 현재 우리 연구원에서는 월성원자력 2,3,4호기를 비록하여 울진원자력3,4호기를 비롯하여 울진원자력3,4호기, 영광원자력5.6호기에 대한 시공공인검사를 수행하고 있으며 울진원자력5,6호기와 KEDO에서 시행하는 북한원전에 대한 시공공인검사를 준비하고 있는 실정이다. 여기에서는 현재 검사가 진행중인 월성원자력 2,3,4호기 시공공인검사를 중심으로 원자력발전소 시공에 적용하고 있는 공인검사에 대해 소개하고자 한다.

• Journal of the Korean Society of Marine Environment & Safety
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• v.4 no.1
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• pp.49-56
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• 1998

The Microfiltration and Ultrafiltration were used to treat effluent of secondary municipal wastewater treatment system(Sequencing Batch Reactor). The cross-flow hollow fiber, UF 500,000(NMWC) and MF 0.65$\mu$ membrane were selected as suitable membrane. Short term and long term fouling effect were measured as a factor of flux decrease and the fouling removal effect of mixing air bubble in the penetrant was studied. The removal of anionic sulfactants before and after formation of micelle with several kinds of oil were checked. The test results show that removal of TOC was 70~80%, TN 28% and TP 16%. The decrease of flux due to fouling were 85%(UF) and 90%(MF) after running of 100hrs. The removal of anionic sulfactants were 60~70% notwithstanding micelle or not.

• Proceedings of the Korean Society for Noise and Vibration Engineering Conference
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• 1996.10a
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• pp.27-31
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• 1996

연사기는 장섬유가 천연섬유와 유사한 섬유의 성질을 갖도록 하거나 면사, 모사 등의 단섬유사의 인장강도를 높여주기 위해서 실을 꼬아주는 기계를 가리키며 여러 가지의 연사기 가운데 생산성이 높은 2-for-1 연사기가 널리 사용되고 있다. 2-for-1 연사기는 고정된 급사 보빈과 이것을 관통하는 중공스핀들, 실이 통과하는 구멍(yarn guide)을 가진 디스크와 실을 감는 장치등으로 구성되어 있다. 고정된 보빈에서 풀려 나온 실이 스핀들을 거쳐 회전하는 yarn guide를 통과하면서 실이 한 번 꼬이고 yarn guide를 빠져나온 실이 감기면서 다시 꼬이므로 1회전당 2회 꼬이게 되어 2-for-1이라는 이름이 붙여졌다[1]. 2-for-1연사기의 스핀들은 대개 10,000-15,000rpm으로 회전하며 고속으로 올라갈수록 생산성이 증대되기 때문에 고속화를 위한 노력이 계속되고 있으나 고속화를 가로막는 중요한 애로기술의 하나가 소음, 진동저감기술이다. 본 연구에서는 스핀들 32개짜리로 특별제작된 2-for-1 연사기에서 가장 중요한 소음으로 인식되고 있는 스핀들 소음의 소음원인을 규명하고자 하였다. 소음원인의 분석에는 다중입력/단일출력(MISO)모형을 이용한 신호 해석법을 사용하였다.

• Membrane Journal
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• v.24 no.2
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• pp.107-112
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• 2014

The composite membranes were prepared on the surface of hydrophobic porous poly (vinylidene fluoride) (PVDF) hollow fiber membranes through the interfacial polymerization. The preparation variables were the concentrations of piperazine (PIP), trimesoyl chloride (TMC) and the contents of polyethylene glyco l (PEG). The separation characterization of the resulting membranes were carried out for aqueous 100 ppm solution of NaCl, $CaSO_4$, and $MgCl_2$ and also mixed 300 ppm solution of NaCl and $CaSO_4$ in terms of the flux and rejection. Both the flux and rejection were the highest when the interfacial polymerization was conducted using TMC. When TMC concentration was 0.1 wt%, the flux and rejection were shown 48.3 LMH ($L/m^2{\cdot}hr$) and 59%, respectively. To improve the flux, the annealing post-treatment and the addition of PEG into piperazine were done. As expected, the overall flux was enhanced while the rejection was reduced.

• Journal of Korean Society of Environmental Engineers
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• v.35 no.5
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• pp.371-380
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• 2013

Though MBR process has many advantages, the greatest risk factors in operating MBR process are occurrence of membrane fouling and decrease of flux. It is very difficult to find exact mechanism due to complex influence by many effects, although there have been recently many studies of membrane fouling. The purposes of this study are firstly evaluating bioreactor of lab-scale and micro-filtration hollow fiber membrane, secondly investigating correlation between foulants affecting membrane performance and membrane fouling, and lastly evaluating various parameters affecting fouling and applicability of membrane fouling reducer. This study found that TMP was increasing rapidly and showed 0.32 bar and the average of flux was 88 LMH. EPS concentration tends not to change much above MLSS concentration (6,000 mg/L). However, EPS concentration variation is wide below MLSS concentration (6,000 mg/L). Also, from results of membrane surface condition and element analysis using SEM/EDX, carbon and fluorine were founded to be the highest percentage in membrane because of characteristics of membrane material. In operating continuously, inorganic fouling was generated by increase of these inorganic substances such as $Al^{3+}$ and $Mg^{2+}$. Lastly, the best filtration performance was obtained for 0.03 mg MFR/mg MLSS by results of particle size, zeta potential, $SCOD_{cr}$, EPS and MLSS concentration.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.4 no.2
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• pp.114-119
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• 2003

This study is to remove several organic pollutants from wastewater by non-dispersive membrane solvent extraction technique. The distribution coefficients of several solvents were determined and the experimental system was operated counter-currently and cocurrently with respect to the aqueous phase and solvent. In these experiments, as the flow rate of aqueous solution inclosed, due to being shortened contact time to solvent, the rate of removal of organic pollutants decreased and as the flow rate of solvent increased, the rate of removal increased. Meanwhile, the rate of removal of organic pollutants for the countercurrent flow system was higher than that for the occurrent flow system.