• Journal of Korean Society of Environmental Engineers
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• v.38 no.1
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• pp.8-13
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• 2016

This study investigated the removal of a radioactive cesium ($Cs^+$) in the water at the water treatment processes. Since cesium is mostly present as the $Cs^+$ ion state in water, it is not removed by sand filtration, and coagulation with polyaluminum chloride (PACl), powdered activated carbon (PAC) and mixture of PACl and PAC. However, it is known that the removal rate of cesium increases as the turbidity increases in raw water. As the turbidity was adjusted by 74 NTU and 103 NTU using the surrounding solids near G-water intake and yellow soils, removal rate of cesium was about 56% and 51%, respectively. In case of a GAC filtration with supernatants after jar-mixing/setting was conducted, 80% of cesium is approximately eliminated. The experimental results show that it is efficient to get rid of cesium when the turbidity of the raw water is more than 80 NTU. In case of a GAC filtration, about 60% of cesium is removed and it is considered by the effect of adsorption. Cesium is not eliminated by microfiltration membrane while about 75% of cesium is removed by reverse osmosis.

• Membrane Journal
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• v.16 no.4
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• pp.303-312
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• 2006

The asymmetric hybrid membranes of polyethersulfone (PES) and $ZrO_2$ nanoparticles were prepared via new one-step procedure combining simultaneously the phase-inversion method and the sol-gel technique. The optimum contents of $Zr(PrO)_4\;and\;HNO_3$ catalyst were determined by the adsorption experiments of phosphate anion onto the resulting hybrid membranes. The maximum adsorption of phosphate anion is obtained at the conditions of 0.15 mL $Zr(PrO)_4$ addition per 1 mL PES and 30 mL $HNO_3$ addition per 1 mL $Zr(PrO)_4$. Variation of morphology, performance and incorporated $ZrO_2$ amount of the resulting hybrid membranes were discussed and determined using SEM, pure water flux, TGA, ICP, XRD and contact angle measurements. Increasing $Zr(PrO)_4$ addition into casting solution, pure water flux is increased and $ZrO_2$ amount in the hybrid membrane is maximized at the conditions 0.15 mL $Zr(PrO)_4$ addition per 1 mL PES. The prephosphatation of PES-$ZrO_2$ hybrid membrane was studied to modify the surface characteristics of membrane. Ultrafiltration of bovine serum albumin (BSA) solution was performed in a dead-end cell using both a bare (non-phosphated) and a phosphated hybrid membrane. It is revealed that both the permeate flux and BSA rejection were increased as about 40% by prephosphatation of hybrid membrane. These results may be explained on the basis of the increase of membrane hydrophilicity, which was determined from contact angle measurements.

• Membrane Journal
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• v.28 no.6
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• pp.379-387
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• 2018

This study was conducted to improve the membrane characteristics and performance by increasing hydrophilicity by adding additives to the ultrafiltration polysulfone (PSf) hollow fiber membrane. The mixed matrix membranes (MMMs) were prepared by dispersing 15 nm of fumed silica (FS) in the spinning solution at 0.1, 0.3 and 0.5 wt%. SEM analysis was carried out to confirm the cross-section and surface condition. It was confirmed that mean pore radius of the hollow fiber increased by 4 nm as FS was added. In addition, contact angle measurement was carried out for the hydrophilicity analysis of hollow fiber membranes, and it was confirmed that the hydrophilicity of MMMs were increased by adding of FS. In the case of water permeability, the membrane including FS showed 91~96 LMH and showed 5~11% more increase than PSf membrane. In the antifouling performance test, relative flux reduction ratios of FS mixed hollow fiber membranes were lower than that of PSf membranes, and it was confirmed that increase of hydrophilicity hinders adsorption of hydrophobic BSA on the membrane surface.

• Membrane Journal
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• v.18 no.2
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• pp.157-167
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• 2008

Removal of organic substances and taste/odor control are ones of the main issues in water supply, resulting in introduction of advanced processes such as ozon/GAC, or PAC. However, raw water quality deteriorates, new pollutants advent, so water quality is not acceptable enough even with those existing advanced processes. In this paper, a new advanced water treatment process using PAC slurry blanket, where PAC particles stay in the basin as slurry blanket, coupled with submerged membranes is introduced. A pilot plant $(80m^3/day)$ was installed to assess the performance of this new process using actual raw water, and DOC was removed higher than 90% in the beginning and $70{\sim}80%$ afterwards, while 2-MIB and geosmin were removed completely. This new process still requires future study on process optimization and long-term assessment, however it seems highly possible to countermeasure as a new advanced process with high removal efficiency.

• Journal of Korean Society of Environmental Engineers
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• v.36 no.11
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• pp.747-752
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• 2014

Iodine-131, an artificial radionuclide, mostly exists as iodide ion ($^{131}I^-$) and iodate ion ($^{131}IO_3{^-}$) in the water, and When a short time contacted, it could not be removed by poly aluminum chloride (PACl) and powdered activated carbon (PAC). Although the removal rate of iodine-131 was not related with turbidity of raw water, it showed linear relationship with contact time with PAC. With the mixture of PACl (24 mg/L or more) and PAC (40 mg/L or more), about 40% of iodine-131 could be removed. Iodine-131 could be removed little by sand filtration, but approximately 100% by granular activated carbon (GAC), both virgin-GAC and spent-GAC. Microfiltration process could remove little iodine-131 while reverse osmosis process could remove about 92% of iodine-131.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2016.11a
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• pp.112-112
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• 2016

인체접촉시 니켈도금의 알러지 반응을 억제하기 위한 대체 도금기술인 비 시안계 Cu-Sn 합금도금을 개발함에 있어서, 황산구리5수화물과 황산제일주석을 금속염으로 하여 황산 및 계면활성제, 유화제 등을 포함한 각종 유기첨가제를 포함하였고 특히 은백색조의 외관 색상과 안정적인 Cu-Sn 합금전착을 위해 2종의 착화제인 EDTP($C_{14}H_{32}N_2O_4$)와 TEA(Triethanolamine)를 첨가한 비 시안계 Cu-Sn 합금 도금액을 도출하였다. Cu-Sn 합금도금 피막 조성의 균일화를 도모하기 위해서는 합금 도금액중의 Cu와 Sn 금속이온 농도를 일정하게 유지하는 것이 필요하다. 그러나 합금 도금액중 2가 주석이온($Sn^{2+}$)은 수용액중에서 4가 주석이온($Sn^{4+}$)으로 산화됨으로써 도금액 색상이 백탁이 되고 Stannic Hydroxide($Sn(OH)_4$, $SnO_2{\cdot}2H_2O$)이 생성되어 대량의 침전물이 침강하는 문제점이 발생되는 등 시간 경과에 따른 도금액의 경시 변화가 발생되었다. 상기 침전물은 연속여과에 의해 제거 가능하나 합금 도금액중 $Sn^{2+}$ 농도가 지속적으로 감소하게 된다. 이는 합금 도금액중 금속이온 비율이 변동함으로써 합금도금 피막의 조성비를 일정하게 유지하는 것이 곤란해진다. 이에 $Sn^{4+}$ 침전물 생성을 방지하기 위한 산화방지제를 개발하고 또한 산화방지제의 첨가에 따른 도금 피막 외관에 미치는 영향을 평가하여 외관 개선을 위한 광택제를 개발하고자 한다. 본 연구의 결과를 토대로 니켈도금과 동등 이상의 기능 특성을 갖는 비시안계 Cu-Sn 합금도금액을 개발하여 실용화하는 것을 목적으로 하였다.

• Proceedings of the Korea Water Resources Association Conference
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• 2005.05b
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• pp.1224-1228
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• 2005

본 연구는 강우시 주로 발생되는 강우유출수에 의해 하천으로 직유입 되는 다량의 오염물질을 사전에 저감시키기 위하여 하천의 제방사면부와 둔치부를 형상화한 Pilot 규모의 수처리시스템에 관한 것이다. 본 Pilot Plant는 경희대학교 내 하수처리장 부근에 설치하였으며, 유입부, 사면수처리부, 평면수처리부, 유출부로 구성되며, 수처리조 내부에 다공성여재와 상부에는 식생을 조성하여 연속적으로 운영되는 시스템으로 설계되었다. 사면수처리부는 하천의 제방사면부를 형상화 한 것으로 2:1의 구배를 가지며, 15개의 육각형 모듈을 5개씩 3계열로 배치하여 여재의 처리효율 및 현장 적용성 검토를 실시할 수 있도록 배열하였다. 평면수처리부는 장방형의 접촉산화조로서 하부에 슬러지 침전 및 저류를 위한 hopper를 설치하여 슬러지의 원활한 수집 및 인발이 가능하도록 설계하였다. 또한, 역세를 위한 배관을 설치하여 여재에 부착된 슬러지의 양 조절이 가능하도록 하였다. 또한, 수처리시설물의 자연 친화성 확보 및 식생에 의한 수질개선 효과를 위해 수처리부 상부에 식생을 조성하였다. 본 Pilot Plant의 주요 오염물질의 제거기작은 수처리부 내부에 충진된 다공성 여재와 강우유출수 사이에 발생되는 침전, 여과, 흡착과 여재에 부착된 미생물에 의한 유기물 분해, 식생에 의한 영양물질 섭취 등으로 대별된다. 본 연구는 하천의 제방사면부와 둔치부를 형성화한 Pilot Plant에서 다양한 factor, 즉 유입수량과 농도, 다공성여재 형상 및 충진밀도 등에 따른 수질개선 효과를 각각 비교, 검토하였다.

• Membrane Journal
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• v.26 no.6
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• pp.463-469
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• 2016

In this research, a new expectation in enhancing the PES (polyethersulfone) polymer phase inversion membrane performances with nanoparticles is proposed by using ZnO. This paper investigated the synthesis of PES phase inversion membranes including ZnO nanoparticles and evaluates the performance of these mixed matrix membranes. The PES-ZnO mixed matrix membranes were fabricated by phase inversion method using the PES-ZnO-NMP(N-methyl-1-pyrrolidone) casting solutions with low ZnO nanoparticles content of 0.375 wt%. The influence of ZnO nanoparticles on the characteristics of PES-ZnO mixed matrix membranes was investigated with scanning electron microscope observations of membrane cross-sections, contact angle measurements, tensile strength measurements, pure water flux measurements and ultrafiltration experiments of BSA solution. Those results showed that the performance advancements in comparison with the pure PES membrane without ZnO in terms of increasing hydrophilicity as well as reducing membrane fouling by adding ZnO nanoparticles even in low concentration.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2017.05a
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• pp.68.2-68.2
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• 2017

인체접촉시 니켈도금의 알러지 반응을 억제하기 위한 대체 도금기술인 비 시안계 Cu-Sn 합금도금을 개발함에 있어서, 황산구리5수화물과 황산제일주석을 금속염으로 하여 황산 및 계면활성제, 유화제 등을 포함한 각종 유기첨가제를 포함하였고 특히 은백색조의 외관 색상과 안정적인 Cu-Sn 합금전착을 위해 2종의 착화제인 EDTP (Ethylenediaminetetrapropanol, $C_{14}H_{32}N_2O_4$)와 TEA (Triethanolamine)를 첨가한 비 시안계 Cu-Sn 합금 도금액을 도출하였다. Cu-Sn 합금도금 피막 조성의 균일화를 도모하기 위해서는 합금 도금액중의 Cu와 Sn 금속이온 농도를 일정하게 유지하는 것이 필요하다. 그러나 합금 도금액 중 2가 주석이온($Sn^{2+}$)은 수용액 중에서 4가 주석이온($Sn^{4+}$)으로 산화됨으로써 도금액 색상이 백탁이 되고 Stannic Hydroxide($Sn(OH)_4$, $SnO_2{\cdot}2H_2O$)이 생성되어 대량의 침전물이 침강하는 문제점이 발생되는 등시간 경과에 따른 도금액의 경시 변화가 발생되었다. 상기 침전물은 연속여과에 의해 제거 가능하나 합금 도금액 중 $Sn^{2+}$ 농도가 지속적으로 감소하게 된다. 이는 합금 도금액 중 금속이온 비율이 변동함으로써 합금도금 피막의 조성비를 일정하게 유지하는 것이 곤란해진다. 이에 $Sn^{4+}$ 침전물 생성을 방지하기 위한 산화방지제를 개발하고 또한 산화방지제의 첨가에 따른 도금 피막 외관에 미치는 영향을 평가하여 외관 개선을 위한 광택제를 개발하고자 한다. 본 연구의 결과를 토대로 니켈도금과 동등 이상의 기능 특성을 갖는 비 시안계 Cu-Sn 합금도금액을 개발하여 실용화하는 것을 목적으로 하였다.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.1
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• pp.73-81
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• 2000

The removal of ferrous iron (Fe(II)) in groundwater is generally achieved by simple aeration or the addition of oxidizing agent. Aeration followed by solid-liquid separation is the most commonly used as physico-chemical treatment method for iron removal. In general aeration has been shown to be very efficient in insolubilizing ferrous iron at the pH level greater than 6.5. In this study pH was maintained over 6.5 using limestone granules under constant aeration to oxidize ferrous iron. In batch experiments, oxidation rate of ferrous iron was investigated under different conditions including limestone granule size. initial concentration of the ferrous iron, pH, temperature and ionic strength in groundwater. The pH in groundwater was presumed as the most important factor determining oxidation rate of ferrous iron. According as the size of the limestone granules decreased, the pH of the iron contaminated water increased quickly and oxidation of the ferrous iron was achieved immediately too. The oxidation rate of the ferrous iron was found to be proportion to initial concentration of the iron contaminated water, temperature and ionic strength, respectively.