• 한국물환경학회지
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• 제32권1호
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• pp.23-29
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• 2016

Ozonation was investigated for its ability to remove pyruvic acid in a laboratory-scale batch reactor under various experimental conditions, including UV irradiation, TiO₂ addition, and variations in temperature. An ozone flow rate of 1.0 L min^-1 and a concentration of 75±5 mg L^-1 were maintained throughout the experiment, and pH, COD, and TOC were measured at 10 min intervals during a 60 min reaction. Our results confirmed that the combination of UV irradiation and photocatalytic TiO₂ in the ozonation reaction improved the removal efficiency of both COD and TOC in aqueous solution at 20℃. Pseudo first-order rate constants and activation energies were quantified based on the COD and TOC measurements. We observed that the O₃/UV, O₃/UV/TiO₂ system increased mineralization and reduced the activation energy (E_a) necessary for pyruvic acid decomposition.

• Advances in environmental research
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• 제3권1호
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• pp.29-43
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• 2014

Pharmaceutical wastewater effluents are well known for their difficult elimination by traditional biotreatment methods and their important contribution to environmental pollution due to its fluctuating and recalcitrant nature. OTC is one of the nonbiodegradable antibiotics that makes antibiotic-resistant, so it can make be high risk for environment. NZVI can be a good choice for removal of OTC in aqueous solution. Response surface methodology (RSM) was used to optimize the amounts of NZVI and OTC to be used at pH 3 and under 200 W, UV-A irradiation. The responses were removal percent of absorption at 290 and 348 nm, TOC and COD of OTC. In the optimum condition, Linear model was performed 155 ppm of OTC were removed by 1000 ppm NZVI after 6.5 hours and the removal efficiency of absorption at 290 and 348 nm, TOC and COD were 87, 95, 85 and 89 percent, respectively. In the similar process, there is no organic compound after 14 hours. The parameters ORP, DO and pH were investigated for 6:30 hours to study the type of NZVI reaction in process. In the beginning of reaction, oxidation was the dominant reaction after 3 hours, photocatalytic reaction was remarkable. The mechanism of OTC degradation is proposed by HPLC/ESI-MS and four by products were found. Also the rate constants (first order kinetic chain reaction model) were 0.0099, 0.0021, 0.0010, 0.0049 and $0.0074min^{-1}$, respectively.

• 생명과학회지
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• 제30권2호
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• pp.129-136
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• 2020

암모니아성 질소(NH₄-N) 함유폐수의 효과적인 처리를 위하여 암모니아성 질소가 함유되어있는 식품폐수처리장의 폭기조 활성오니에 우점적으로 존재하는 미생물 중 TOC (total organic carbon) 제거율이 높은 AT2, AT9, AT12 균주와 암모니아성 질소 제거능이 우수한 FN47을 분리, 동정하였다. 이들 분리균주의 균체를 탈지강을 담체로하여 산업폐수처리용 미생물제제 FIW-1 을 제조하였다. 폭기조 분리균주들의 대상으로 폐수자체를 배양기질로 하여 배양학적 특성을 조사하였을 때 분리균주들의 기질친화성이 매우 높은 것으로 나타났으며, 분리균주 중 AT12 균주(Alcaligenes sp. AT12)가 가장 높은 기질친화성을 나타내었다. 식품폐수 중의 암모니아성 질소 제거효율은 분리균주 FN47 (Microbacterium sp. FN47)의 처리구에서 71%의 제거율을 나타내었다. 실험실규모의 반응조에서 식품폐수를 이용한 연속배양 실험에서 활성슬러지만을 첨가한 경우 63% TOC제거효율을 나타내었으며, 폐수처리용 미생물제제 FIW-1을 첨가 시에는 92%의 제거효율을 나타내었다. 또한 폐수처리용 미생물제제 FIW-1의 폐수처리장 현장실험에서는 미생물제제 FIW-1을 투입한 초기 3일간의 유출수COD (chemical oxygen demand) 값은 43% 내외의 처리율을 나타내었으나, 5일이 경과하였을 때 유출수의 COD값은 62%의 처리효율을 나타내었다.

• 상하수도학회지
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• 제13권1호
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• pp.81-94
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• 1999

This study aims at a proposal of the plan that can improve raw water quality by an experimental study using influent water of Nak-dong river, which has been used as raw water for drinking in U-city, through the establishment of the submerged biofilter process PILOT PLANT of media packing channel method. From the analysis of removal efficiency for each water quality item of the collected sample, following results are obtained. First of all, the removal rate of suspended material, BOD, COD, T-N, TOC, turbidity, and $NH_3$ -N appear 82%, 78%, 42%, 15%, 57%, 43%, 54%, and 55% respectively and it is known that the submerged biofilter process of media packing channel method takes effects on water quality improvement from the above analysis results of water treatment efficiency. And the analyzed results for water temperature, residence time, and activities of microorganism, which can be the factors affect on water quality improvement, are as follows. 1) The removal rate variation of SS, BOD, and COD attendant on water temperature change is examined and it is known that the removal rate increases at $13^{\circ}C$ or above. 2) The removal rate of SS, BOD, and COD attendant on residence time is most active in the range of 0~18hr, 0~1.8hr, 0~2.7hr respectively, so it is found that the removal rate becomes smaller after 2.7hr. 3) From the examination of microorganism activity with the abundance of normal bacteria, it is found that the floating bacteria decrease as the flow distance from raw water inflow point of PILOT PLANT increases, and the adhesive bacteria have no concern with the flow distance. And it its known that the biomass of fine algae decreases as the flow distance from the raw water inflow point of PILOT PLANT increases from the examination with Chl-a.

• Environmental Engineering Research
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• 제19권1호
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• pp.9-14
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• 2014

Fenton reaction with zerovalent iron (ZVI) and $Fe^{2+}$ ions was studied to treat pharmaceutical wastewaters (PhWW) including antibiotics and non-biodegradable organics. Incremental biodegradability was assessed by monitoring biochemical oxygen demand (BOD) changes during Fenton reaction. Original undiluted wastewater samples were used as collected from the pharmaceutical factory. Experiments were carried out to obtain optimal conditions for Fenton reaction under different $H_2O_2$ and ion salts (ZVI and $Fe^{2+}$) concentrations. The optimal ratio and dosage of $H_2O_2$/ZVI were 5 and 25/5 g/L (mass basis), respectively. Also, the optimal ratio and dosage of $H_2O_2/Fe^{2+}$ ions were 5 and 35/7 g/L (mass basis), respectively. Under optimized conditions, the chemical oxygen demand (COD) removal efficiency by ZVI was 23% better than the treatment with $Fe^{2+}$ ion. The reaction time was 45 min for ZVI and shorter than 60 min for $Fe^{2+}$ ion. The COD and total organic carbon (TOC) were decreased, but BOD was increased under the optimal conditions of $H_2O_2$/ZVI = 25/5 g/L, because organic compounds were converted into biodegradable intermediates in the early steps of the reaction. The BOD/TOC ratio was increased, but reverse-wise, the COD/TOC was decreased because of generated intermediates. The biodegradability was increased about 9.8 times (BOD/TOC basis), after treatment with ZVI. The combination of chemical and biological processes seems an interesting combination for treating PhWW.

• 한국지반환경공학회 논문집
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• 제11권8호
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• pp.41-47
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• 2010

본 연구에서는 휴믹산 농도, 초기 pH 그리고 공기주입유량과 같은 실험인자가 오존/페록시라디칼 반응시스템의 처리효율에 미치는 영향과 연속 처리을 통한 시스템의 처리 특성을 실험적으로 검토하였다. 오존과 페록시라디칼을 조합한 시스템의 처리효율은 각각의 단독공정에 비해 더 높은 색도 제거효율을 나타내었다. 초기 휴믹산 농도가 증가할수록 처리효율이 증가했지만 초기 휴믹산 농도 30mg/L 이상에서는 오히려 처리효율이 감소한 결과를 나타냈고 초기 pH의 경우 산성영역에서 보다는 중성과 알카리성 영역에서 휴믹산 제거효율이 더 높았으며 공기주입유량이 증가할수록 시스템의 처리효율이 증가하였다. Pilot-scale 시스템을 실제 정수장 유입수에 적용시킨 결과, TOC와 $COD_{Cr}$에 대한 각각의 평균 제거율은 약 70%와 60%로 나타나 수중 난분해성 유기물 제거를 위한 적용가능성을 확인할 수 있었다.

• 산업기술연구
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• 제29권A호
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• pp.89-94
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• 2009

The efficiency of heterogeneous catalysts has been investigated in ozonation process for organic removal. Heterogeneous catalytic ozonation was conducted for the degradation of humic acid in the presence of Granular Activated Carbon or Zeolite as a solid catalyst. And the results were compared to those of ozonation alone and adsorption alone without ozonation. The degradation characteristics of humic acid in each process were examined with the values of pH, TOC, $UV_{254}$ and $COD_{Cr}$.

• 한국환경과학회지
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• 제15권3호
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• pp.193-201
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• 2006

Advanced oxidation processes involving $O_3/H_2O_2$ and $O_3/catalyst$ were used to compare the degradability and the effect of pH on the oxidation of 1,4-dioxane, Oxidation processes were carried out in a bubble column reactor under different pH. Initial hydrogen peroxide concentration was 3.52 mM in $O_3/H_2O_2$ process and 115 g/L (0.65 wt.%) of activated carbon impregnated with palladium was packed in $O_3/catalyst$ column. 1,4-dioxane concentration was reduced steadily with reaction time in $O_3/H_2O_2$ oxidation process, however, in case of $O_3/catalyst$ process, about $50{\sim}75%$ of 1,4-dioxane was degraded only in 5 minutes after reaction. Overall reaction efficiency of $O_3/catalyst$ was also higher than that of $O_3/H_2O_2$ process. TOC and $COD_{cr}$ were analyzed in order to examine the oxidation characteristics with $O_3/H_2O_2\;and\;O_3/catalyst$ process. The results of $COD_{cr}$ removal efficiency and ${\Delta}TOC/{\Delta}ThOC$ ratio in $O_3/catalyst$ process gave that this process could more proceed the oxidation reaction than $O_3/H_2O_2$ oxidation process. Therefore, it was considered that $O_3/catalyst$ advanced oxidation process could be used as a effective oxidation process for removing non-degradable toxic organic materials.

• 대한환경공학회지
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• 제31권9호
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• pp.755-764
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• 2009

시화호 인공습지내 표층퇴적토에 의한 오염물질 제거효율을 평가하기 위하여 표층퇴적물내 물질함량과 퇴적토에 의한 오염물질의 용출여부를 조사하였다. 조사기간 동안 표층퇴적물의 COD, TOC, IL, TN, TP 함량은 각각 4.1~47.7 mg/g, 0.29~2.81%, 1.88~8.15%, 0.03~0.35%, 362~1,150 ${\mu}g$/g의 범위로 조사지점과 시기에 따라 차이를 보였다. 유기물과 TN 함량은 봄에 높고 시간이 지날수록 감소하는 경향을 보인 반면 TP 함량은 유의적인 차이를 보이지 않았다(3월${\geq}$5월${\geq}$7월${\geq}$9월, p=0.003 for COD, p=0.001 for TOC, p=0.017 for IL, p=0.015 for TN). 표층퇴적토의 중금속 함량은 As 3.5~13.9 ${\mu}g$/g, Cd 0.08~0.38 ${\mu}g$/g, Cr 51.8~107.0 ${\mu}g$/g, Cu 16.4~81.8 ${\mu}g$/g, Pb 26.8~81.8 ${\mu}g$/g, Zn 85~559 ${\mu}g$/g의 범위로 항목에 따라 상이한 시공간적인 분포를 보였다. 퇴적물환경기준으로 볼 때 유기물 함량은 대부분 기준 이하의 수준을 보인 반면 TN과 TP는 "중간오염" 또는 "심한 오염" 수준을 보였다. 그리고 중금속 함량은 Cd과 Pb을 제외한 모든 항목에서 퇴적물 환경기준으로 초과하는 것으로 나타났다. 퇴적토의 용출실험 결과로부터 TN, Pb, Zn은 퇴적토에 의해 제거되는 반면 TP, Cd, Cu는 퇴적토로부터 용출되는 경향을 보였다. 그러므로 시화호 인공습지에서 표층퇴적토의 수질정화기능을 향상시킬 수 있는 방안수립이 필요하다.

• 접착 및 계면
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• 제19권3호
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• pp.101-105
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• 2018

도시의 산업화와 인구의 빠른 증가로 인해, 지구상에서 여전히 7억 8천만명이 물자원 사용에 어려움을 격고 있으며, 이에 따라 깨끗하고 저렴한 물자원 확보 방안에 대한 관심이 집중되고 있다. 그러나, 현존하는 폐수처리 시스템은 낮은 공정효율, 높은 운영비용, 그리고 넓은 부지 요구 등의 다양한 이슈에 직면하여 있는 실정이다. 따라서, 저렴하고 효율적인 폐수 처리 시스템의 개발이 시급히 요구된다. 이러한 노력의 일환으로 rutile type $RuO_2$를 기반으로 한 DSA전극을 이용한 전기 화학적 방법에 기초한 폐수 처리 시스템을 제안하였고, 이를 성공적으로 시연하였다. 우리의 폐수 처리 시스템은 생활폐수의 경우, 생화학적 산소 요구량 (BOD), 화학적 산소 요구량 (COD) 및 총 유기탄소 (TOC) 제거 효율이 52.0 %, 77.8 % 및 65.6 % 로 우수한 특성을 보였다. 또한 축산 폐수의 경우, BOD, COD, 총 질소 (TN), 총 인 (TP)의 제거 효율이 각각 92.9 %, 75.6 %, 35.1 %, 100 %로 획기적인 감축 효과를 거두었습니다. 이 장치의 탁월한 제거 효율과 작은 크기를 고려할 때, rutile $RuO_2$로 코팅된 DSA를 사용한 전기화학적 폐수 처리는 생활 및 축산 폐수의 처리를 위한 유망한 방안이 될 수 있음을 제안하고자 합니다.