• 한국지하수토양환경학회지:지하수토양환경
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• 제17권4호
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• pp.44-50
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• 2012

A new type of chemical oxidation technology utilizing micro bubble ozone oxidizer and a pneumatic fracturing equipment was developed to enhance field applicability of a traditional chemical oxidation technology using hydrogen peroxide as an oxidizer for in-situ soil remediation. To find an efficient way to dissolve gaseous ozone into hydrogen peroxide, ozone was injected into water as micro bubble form then dissolved ozone concentration and its duration time were measured compared to those of simple aeration of gaseous ozone. As a result, dissolved ozone concentration in water increased by 31% (1.6 ppm ${\rightarrow}$ 2.1 ppm) and elapsed time for which maximum ozone concentration decreased by half lengthened from 9 min to 33 min. When the developed pneumatic fracturing technology was applied in sandy loam, cracks were developed and grown in soil for 5~30 seconds so that the radius of influence got longer by 71% from 392 cm to 671 cm. The remediation system using the micro bubble ozone oxidizer and the pneumatic fracturing equipment for field application was made and demonstrated its remediation efficiency at petroleum contaminated site. The system showed enhanced remediation capacity than the traditional chemical oxidation technology using hydrogen peroxide with reduced remediation time by about 33%.

• 한국지하수토양환경학회지:지하수토양환경
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• 제15권2호
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• pp.34-39
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• 2010

In this study, the remediation of diesel contaminated soil was attempted with ozone treatment and Fenton reaction. About 10% of initial diesel concentration was removed by the ozone saturated solution. The pseudo-first order decomposition constant of diesel contaminated soil in the presence of 5% of hydrogen peroxide with 1.82, 2.82, 4.82, 6.82, and 11.82% of iron contents was 0.0228, 0.0308, 0.0482, 0.0471, and 0.0592 $min^{-1}$ respectively. The decomposition constant of the diesel was 0.0064 $min^{-1}$ with the addition of ozone saturated solution only. On the addition of ozone saturated solution in the presence of 5% hydrogen peroxide and 5% iron, the decomposition constant of the diesel was 0.0850 $min^{-1}$. These results indicated that the decomposition rate was 190% faster than without the addition of ozone saturated solution. Thus, the application of both ozone and the fenton reaction is promising for the remediation of the diesel contaminated soil.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2002년도 추계학술발표회
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• pp.86-88
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• 2002

The mathematical model was proposed to simulate ozone transport and remediation in unsaturated soils contaminated with phenanthrene. Soil column experiments were also carried out to calibrate the mathematical model. The experimental results successfully matched with the modeling results in various soil conditions. The model proposed nondimensional fraction factor to reveal reactivity between phenanthrene and gas phase ozone and liquid phase ozone. From sensitivity analysis, the fraction factor and stoichiometric coefficient decreased as water content increased. Simulation results showed increased SOM content retarded the ozone transport and the phenanthrene removal due to increased ozone consumption.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2001년도 총회 및 춘계학술발표회
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• pp.140-143
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• 2001

The packed column experiments were conducted with commercial Jumunjin sand(SOM content : 0.01 %) and a field soil(SOM content : 0.08 %) in order to understand the effects of water content and soil organic matter(SOM) on the transport of gaseous ozone in unsaturated soil contaminated with phenanthrene. Water content and SOM content were artificially controlled. As water content increased, earlier breakthrough was observed in the beginning of BTC of ozone, because direct contact of gaseous ozone with SOM and phenanthrene was prevented by water film formed between soil particles and gaseous ozone. The total removal of phenanthrene in Jumunjin sand was not affected by water content which was more than 99% at different water content(4.4, 8, 17.3%). However, the removal in field soil at water content 6.5 % and 20 % was 98% and 80 %.

• 대한환경공학회지
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• 제22권10호
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• pp.1825-1832
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• 2000

유류화합물(디젤)로 오염된 불포화층 토양에 대한 현장오존복원공정의 기초연구로, 토양조건에 따른 오존의 이동과 분해, 디젤과의 반응경향을 조사하였다. 건조상태에서 유기물을 제거한 모래와 glass beads 충진컬럼에서 기상 오존의 분해를 조사한 결과 일차반응으로 가정시 반응 속도상수값(k)이 각각 $9.9{\times}10^{-3}s{^{-1}}$와 $4.3{\times}10^{-4}s{^{-1}}$로 나타나 모래의 경우 철 (Fe), 망간(Mn) 성분 등의 촉매작용으로 25배 가량 반감기가 짧은 것을 확인할 수 있었다. 디젤로 오염시킨 현장 토양과 모래를 컬럼에 충진하여 동일조건하에서 오존주입시 토양입자의 크기와 유 무기물의 함량 차에 의한 오존이동상에 지체효과 및 소모량의 차이를 관찰하였고, 50mL/min의 유속에서 공기만을 주입시 DRO(diesel range organic) 기준 초기 디젤총량($800{\pm}50mg/kg$)의 30%가 제거된데 비해 오존을 6mg/min으로 16시간 주입한 결과 각각 80% 이상이 제거되었다. 오존주입시간에 따라 컬럼의 유출 입부에 잔류하는 TPH(total petroleum hydrocarbon)와 DRO 중 aliphatic계열 8개 물질들의 농도를 비교/분석한 결과, 낮은 탄소수 물질들로의 전환과정을 거쳐 유체의 흐름에 따라 컬럼 밖으로 이동됨을 확인하였고, 토양내 수분함량은 오염 토양복원에 오존을 적용시 중요한 인자임을 확인하였다.

• 대한환경공학회지
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• 제27권10호
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• pp.1052-1057
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• 2005

본 연구에서는 오존분해 된 슬러지를 인 방출을 위한 외부 탄소원으로 사용하기 적절한지 평가하기 위하여 오존 주입량 변화에 따라 오존분해된 슬러지의 성상변화와 함께 인 방출 실험 및 VFA(Volatile Fatty Acid) 생성량을 살펴보았다. 슬러지를 오존 주입량 0.5 g $O_3/g$ SS로 분해했을 경우 TCOD(Total Chemical Oxygen Demand)와 TSS(Total Suspended Solid)는 오존분해 전 7050, 4900 mg/L에서 5850, 2867 mg/L로 각각 17, 41% 감소하였다. 또한, pH는 6.6에서 3.8로 감소하였고, SCOD(Soluble Chemical Oxygen Demand)는 38.7 mg/L에서 2760 mg/L로 약 70배 증가함을 보였다. 오존 분해에 의해 acetic acid와 같은 VFA도 새로이 생성됨을 확인하였다. Acetic acid의 경우 0.05 g $O_3/g$ SS로 분해된 슬러지에서 50.24 mg/L가 생성되었으며, 0.5 g $O_3/g$ SS로 분해된 슬러지의 경우는 123.56 mg/L로 증가되었다. 그러나 혐기성 소화에 의한 VFA의 증가량은 0.05 g $O_3/g$ SS로 분해된 슬러지에서 Acetic acid가 50.24 mg/L에서 219.28 mg/L로 가장 많이 증가되었다. 또한 낮은 오존 주입량(0.05, 01 g $O_3/g$ SS)으로 분해된 슬러지에서 관찰되지 않았던 Propionic acid는 46 mg/L가 새로이 증가하였다. 그 외 혐기성 소화로 인해 n-Butyric Acid, Propionic Acid, n-Butyric Acid, Isovaleric Acid, Valleric Acid의 농도도 증가하였다. 오존 주입량에 따라 SCOD, VFA의 농도는 증가하지만 인 방출 속도 및 경제성을 고려하여 적정 오존 주입 농도는 0.05-0.1 g $O_3/g$ SS로 조사되었다.

• 한국토양환경학회지
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• 제4권3호
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• pp.3-15
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• 1999

기존의 SVE 공정에 공기 대신 오존을 주입하여 유류물질의 지중분해를 유도하고 추출가스의 처리부담을 최소화할 수 있는 복원 신공정 개발을 위한 기초연구를 수행하였다. 이를 위하여 비휘발성 유류물질인 디젤유를 처리대상물질로 하여 토양칼럼실험을 통해 오존주입에 의한 지중분해 가능성을 검토하였다. 수분함량 8.39%의 실토양에 디젤유를 혼합하여(초기농도 1,485mg-DRO/kg-soil)칼럼에 충진시킨 후 119.0$\pm$6.1mg/L의 농도를 가지는 오존가스를 50mL/min의 유량으로 연속 주입하였을 때 14시간 반응후 칼럼 상 하부의 디젤유 제거율은 각각 87.9%, 100.0%를 나타내어 비교적 빠른 시간내에 효과적으로 처리되는 것으로 나타났다. 한편 동일한 조건에서 오존가스 대신 공기를 주입하였을 때 공기 유입 및 유출부 모두 총 14시간 동안의 접촉시간 동안 30%이내의 제거율을 나타냄에 따라 디젤오염토양에 대한 기존 SVE공정의 적용한계를 확인하였다.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2002년도 총회 및 춘계학술발표회
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• pp.22-25
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• 2002

The effect of in-situ chemical oxidation on the indigenous soil microorganisms (total microbes and PAH-degrading microbes) and contaminant removal were investigated. Field soil contaminated with diesel in gas station was collected and the soil was treated from 0 to 900 minutes by in-situ ozonation as chemical remediation. The treated soil samples were incubated with supplying oxygen during the 9 weeks to understand the characteristics of microbes regrowth, damaged by ozone. The sharp decrease of aromatic fraction and TPH was observed within 60 minutes of ozone application and aromatic fraction and TPH then slowly decreased. The phenanthren-degrading bacteria were the most sensitive to ozonation, because 1 hour of ozonation reduced the microbes from 10$^{6}$ CFU/g-soil to below detection limits.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2003년도 추계학술발표회
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• pp.172-175
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• 2003

Field scale application of in-situ ozonation were carried out for remediation of variably saturated soils contaminated with diesel fuel with 3 dimensional test cell (3m$\times$2m$\times$2m). After 20 days of ozone injection, more than 90% of removal rate was observed through the 3-D test cell. This result might be caused by uniform distribution, relatively low oxidant demand, and low water content of soils, as well as high oxidation potential of ozone. However, less than 50 % of injected ozone was monitored through the 3-D test cell even after 20 days of injection.

• 한국지하수토양환경학회지:지하수토양환경
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• 제15권6호
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• pp.37-45
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• 2010

Surfactant-enhanced ozone sparging (SEOS), an advanced version of SEAS (surfactant-enhance air sparging) was introduced in this study for the first time for removal of non-volatile contaminant from aquifer. The advantages of implementing SEAS, enhanced air saturation and expanded zone of sparging influence, are combined with the oxidative potential of ozone gas. Experiments conducted in this study were tow fold; 1-dimensional column experiments for the changes in the gas saturation and contaminant removal during sparging, and 2-dimensional box model experiment for the changes in the size of zone of influence and contaminant removal. An anionic surfactant (SDBS, sodium dodecylbenzene sulfonate) was used to control surface tension of water. Fluorescein sodium salt was used as a representative of watersoluble contaminants, for its fluorescence which is easy to detect when it disappears due to oxidative degradation. Three different gases (air, high-concentration ozone gas, and low-concentration ozone gas) were used for the sparging of 1-D column experiment, while two gases (air and low-concentration ozone gas) were used for 2-D box model experiment. When SEOS was performed for the column and box model, the air saturation and the zone of influence were improved significantly compared to air sparging without surface tension suppression, resulted in effective removal of the contaminant. Based on the experiments observations conducted in this study, SEOS was found to maintain the advantages of SEAS with further capability of oxidative degradation of non-volatile contaminants.