• 공업화학
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• 제18권4호
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• pp.391-395
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• 2007

본 연구는 electrokinetic process (EK process)를 이용하여 20000 mg/kg의 납(Pb)으로 오염된 토양을 처리하는 과정에서 중금속이 오염토양 내부에 수산화물 형태로 침전되는 현상을 억제할 수 있는 방법을 찾기 위하여 전극교환(EK-Exchange, EK-E)과 혼합용매(0.3 M acetic acid and 0.03 M EDTA, EK-Mixed Solution, EK-M)를 사용하는 방법을 적용하였다. 혼합용매를 사용하는 경우(EK-M)에는 EDTA 0.03 M을 단독으로 사용하는 경우(EK-Blank, EK-B)보다는 약 2% 정도 낮은 제거효율을 나타내었다. 그러나, 비싼 EDTA 약품 값을 절약할 수 있다는 측면에서 보면, 이 방법도 충분히 적용 가능한 방법이다. 전극교환을 하는 경우(EK-E)에는 EDTA 0.03 M을 사용하는 경우(EK-B)보다 2% 높은 제거효율을 나타내었다. 그러나 더욱 중요한 사항은 다른 운전조건(EK-B, EK-M)과는 달리 토양 내부의 pH가 7~8 사이로 중성 부근에서 유지되었다는 점이다. 특히, 중금속의 축적이 우려되는 EK-B와 EK-M과는 달리 중금속이 특정 부위(오염토양 중앙부 또는 음극부)에 축적되지 않는다는 장점을 나타내었다.

• 한국지하수토양환경학회지:지하수토양환경
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• 제7권1호
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• pp.15-24
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• 2002

현재 원위치 bioremediation을 목적으로 EK (electrokinetlc)기법에 의한 영양분과 TEAs (Terminal electron accepters) 공급이 연구되고 있으나, 아직까지 다양한 토질에서의 EK 주입특성 연구는 미비하다. 따라서 본 연구에서는 카올린과 모래시료에 대하여 영양분인 암모늄이온과 TEAs로서 황산염이온의 EK주입실험을 수행하였다. EK주입에 의한 암모늄이온의 경우 카올린에서는 주입부(양극)에서 높은 농도분포를 보이며, 특별히 모래의 경우는 음극에서 더욱 높은 농도분포를 보인다. 황산염이온의 주입분포는 두 시료에서 모두 균일한 주입분포를 보이지만 두 시료에서의 농도차는 크게 달랐다. 따라서 원위치 bioremediation에 EK 주입기법을 이용할 경우 토질에 따른 주입특성의 평가가 가장 중요하게 고려되어야 한다.

• 한국지반공학회:학술대회논문집
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• 한국지반공학회 2002년도 봄 학술발표회 논문집
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• pp.3-38
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• 2002

This paper presents a general review of the literature on electrokinetic (EK) remediation of contaminated soil. Lab-scale tests were investigated and contaminant transport mechanism were examined. And also major factors affecting to the EK process were discussed. Enhanced techniques as a method to solve the problems that frequently occurred during traditional EK process were examined. And last, field implemented case and commercially applied case were described.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2001년도 추계학술발표회
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• pp.127-130
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• 2001

This paper presented to phenanthrene removal of electrokinetic(EK) remediation and enhanced EK remediation with bench scale test. The experiments were carried out on mixture soil with phenanthrene as the test compound. The EK remediation experiments were conducted under controlled voltage. Surfactant solution was constantly supplied at the anode reservoir with constant concentration. Results showed that phenanthrene was removed little in EK remediation. Surfactant helped phenanthrene moving and cumulated in cathode region. Moving effect was increased with surfactant concentration.

• 한국지하수토양환경학회지:지하수토양환경
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• 제6권4호
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• pp.13-23
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• 2001

본 연구는 중금속 오염지반의 정화를 목적으로, Electrokinetic(EK) 기법을 적용 할 때 지반 내에서 pH와 오염물 분포특성을 알아보았다. 시료 내에서의 EK 처리로 인한 납 제거 효과를 살펴본 결과 1V/cm의 전압경사 하에서 납은 음극으로 이동하여, 전극 간 시료의 80%정도 영역에서 제거율은 대략 75% 정도에 이르렀다. 그러나 이동된 납은 대부분이 음극영역에 침전되어 궁극적으로 음극수로 배출되어 제거되는 납의 양은 미미하였다. 이때, EK 정화처리는 시료의 대부분인 80% 정도에서 토양환경보전법 상의 규준치를 만족할 수 있으나, 음극쪽 20%지역은 별도의 향상기법을 적용하여 처리하는 기법이 필요하다.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2003년도 추계학술발표회
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• pp.356-359
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• 2003

Polycyclic aromatic hydrocarbons (PAHs) are representative hydrophobic organic carbons (HOCs). Surfactant-enhanced electrokinetic (EK) remediation is an innovative in-situ technology that can effectively remove HOCs from low-permeability soils. In this study, the electrokinetic remediation using Tergitol 15-S-12, a nonionic surfactant, was conducted for the removal of phenanthrene from kaolinite. Tergitol 15-S-12 was used at concentrations of 1.5, 2.0, 2.5 and 7.5 g/L to enhance the solubility of phenanthrene. When the surfactant solution was applied to EK system, high electrical potential gradient was maintained and the amount of electroosmotic flow decreased. Removal efficiency of phenanthrene was proportional to the concentration of Tergitol 15-S-12 because the solubility and mobility of phenanthrene was enhanced by surfactant micelle. Therefore, the suitable concentration of nonionic surfactant Tergitol 15-S-12 is expected to improve the removal efficiency of PAHs in EK remediation.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2003년도 총회 및 춘계학술발표회
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• pp.306-309
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• 2003

Surfactant-enhanced electrokinetic (EK) remediation is an emerging technology that can effectively remove hydrocarbons from low-permeability soils. In this study, the electrokinetic remediation using Calfax 16L-35 was conducted for the removal of phenanthrene from kaolinite. An anionic surfactant Calfax 16L-35 was used at concentrations of 5, 15, and 30g/L to enhance the solubility of phenanthrene. When the surfactant solution was applied to EK system, low electrical potential gradient was maintained because of its ions. Even when the surfactant concentration was high, the removal efficiency of phenanthrene was low After the operation, most of surfactants were remained in soil and there were few in effluent. This phenomena was observed because the migration of Calfax 16L-35 from cathode to anode was predominant over electroosmotic flow which moved in opposite direction. Therefore, the anionic surfactant Calfax 16L-35 is considered to be improper in surfactant - enhanced electrokinetic remediation.

• 한국지하수토양환경학회지:지하수토양환경
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• 제17권4호
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• pp.91-97
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• 2012

In this study, cost analysis of electrokinetic (EK) restoration process for desalination of saline agricultural land was performed for field application based on a pilot scale field application. For reasonable cost analysis, EK process was classified into three major parts: system design, installation and operation. Cost of system installation consists of materials and installation for electrode/electric wire, power supply and data monitoring, drainage system, etc. Operation cost was calculated based on electrical consumption and water charges for EK process. Total cost for EK process was 2,943,013 won for $1000m^2$ in greenhouse area. Cost for system installation was 2,553,786 won, that is, 87% of total cost, while cost for system operation was 389,229 won, that is, 13% of total cost.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2004년도 임시총회 및 추계학술발표회
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• pp.76-79
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• 2004

This research was carried out to evaluate role of supplementary reagents, such as phosphate and SDS, to remove hydrophobic organic contaminant from soils during the EK-Fenton process. The $H_2O$$_2$ stability improved due to the role as stabilizer of phosphate and SDS during the EK-Fenton process. Furthermore, although pH in region near cathode was 8.2 after test, $H_2O$$_2$ stability improved due to transportation of SDS in the region near cathode. Therefore, in tests using phosphate and SDS as supplementary reagent, the efficiency of phenanthrene treatment improved through the EK-Fenton process using longer reaction time.

• 한국지반공학회:학술대회논문집
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• 한국지반공학회 2004년도 춘계학술발표회
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• pp.211-218
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• 2004

The objective of this study is to enhance the ultimate bearing capacity of piles embedded in marine clay by electrokinetic(EK). The focus of improvement is at interlace between soil and pile. A series laboratory test was performed in EK cell. In each of test, the pile in the centre as anode is surrounded by cathode and it was installed in the vicinity of pile with triangular layout. The pile was made by stainless and embedded with 30cm of depth. Afterward, the DC voltage was applied to electrode over period of time. It caused flowing water from anode to cathode, thus the soil in the center of box has higher bearing capacity value than in the side of box has. It is shown by increasing of un-drained shear strength(Cu) near the pile and also ultimate bearing capacity of pile increase after EK treatment. In the future work, the continuous of this study is finding the effective DC voltage and makes EK treatment more applicable in the field.