• 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.

• 한국지하수토양환경학회지:지하수토양환경
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• 제22권2호
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• pp.17-25
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• 2017

The efficiency and mechanism of electrochemical phenol oxidation using persulfate (PS) and nanosized zero-valent iron (NZVI) were investigated. The pseudo-first-order rate constant for phenol removal by the electrochemical/PS/NZVI ($1mA^*cm^{-2}/12$ mM/6 mM) process was $0.81h^{-1}$, which was higher than those of the electrochemical/PS and PS/NZVI processes. The electrochemical/PS/NZVI system removed 1.5 mM phenol while consuming 6.6 mM PS, giving the highest stoichiometric efficiency (0.23) among the tested systems. The enhanced phenol removal rates and efficiencies observed for the electrochemical/PS/NZVI process were attributed to the interactions involving the three components, in which the electric current stimulated PS activation, NZVI depassivation, phenol oxidation, and PS regeneration by anodic or cathodic reactions. The electrochemical/PS/NZVI process effectively removed phenol oxidation products such as hydroquinone and 1,4-benzoquinone. Since the electric current enhances the reactivities of PS and NZVI, process performance can be optimized by effectively manipulating the current.

• 자원환경지질
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• 제34권1호
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• pp.147-156
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• 2001

티탄자철석(titanomagnetite)은 해양지각을 이루는 현무암에 존재하는 중요한 자성광물로서 일반적으로 저온산화에 의해 양이온이 결핍된(cation-deficient) 티탄맥히마이트(titanomaghemite)로 변한다. 실험실에서 철성분 제거방식(removal of iron mechanism)을 통해 자연에서 일어나는 티탄자철석의 수성 저온산화(low-temperature aqueous oxidation)를 재현하였으며, 산화정도에 따라 티탄맥히마이트의 자기적 특성이 민감하게 변화하는 것을 관찰하였다. 본 실험 결과 산화정도에 따라 티탄자철석의 큐리온도(Tc)는 166$^{\circ}C$에서 40$0^{\circ}C$로 증가하였고, 상온에서의 포화자화 강도(Ms)는 126.30 kA/m(25.26 emu/g)에서 16.55 kA/m(3.31 emu/g)로 감소하였으며, 항자기력(Hc)은 6.13 kA/m(77 Oe)에서 38.83 kA/m (488 Oe)로 잔류항자기력(Hcr)은 23.24 kA/m(292 Oe)에서 47.03 kA/m(591 Oe)로 증가함을 관찰하였다. 또한 대자율($\chi$)은 $2023{\times}10^{-6}SI$에서 $84{\times}10^{-6}SI$로 감소함을 나타내었다. 이와 같은 결과를 근거로 현재에서 30 Ma까지의 해양지각의 자화 강도의 변화는 티탄자철석의 저온산화에 의한 결과로 해석하였으며 30~120 Ma에 이르는 해양지각의 자화 강도의 변화는 해양지각에 포함된 티탄자철석의 산화와 산화에 순반되는 광물전에 의한 결과로 추정하였으며 보다 구체적인 원인은 해양지각에서 채취한 시료에 대한 체계적인 연구를 통해서 밝혀질 것으로 기대된다.

• 한국지하수토양환경학회지:지하수토양환경
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• 제20권5호
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• pp.1-10
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• 2015

FeS, as a natural reduced iron mineral, has been recognized to be a viable reactive material for As(III) sequestration in natural and engineered systems. In this study, FeS-coated sand packed columns were tested to evaluate the As(III) removal capacities under anaerobic conditions at pH 5, 7 and 9. The column obtained As(III) removal capacity was then compared with the capacity result obtained from batch reactors. In the comparison, two different approaches were used. The first approach was used the total As(III) removal capacity which method was proved to be useful for interpreting pH 5 system. The second approach was used to consider sorption non-linearity and proved to be useful for interpreting the pH 9. The results demonstrated that a mechanistic understanding of the different removal processes at different pH conditions is important to interpret the column experimental results. At pH 5, where the precipitation of arsenic sulfide plays the major role in the removal of arsenic, the column shows a greater removal efficiency than the batch system due to the continuous dissolution of sulfide and precipitation of arsenic sulfide. At pH 9, where adsorption mainly governs the arsenic removal, the sorption nonlinearity should be considered in the estimation of the column capacity. This study highlighted the importance of understanding reaction mechanism to predict column performance using batch-obtained experimental results.

• 한국수산과학회지
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• 제35권2호
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• pp.146-154
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• 2002

황토살포에 따른 해수중 영양염 제거효율 및 제거기구를 파악하기 위하여 황토의 입자 크기와 살포농도에 따른 경과시간별 해수중 영양염 농도변화를 실내 실험을 통하여 측정하였다 53$\mu$m 이하에서 500$\mu$m 크기범위의 황토입자를 해수중에 첨가하여 24시간이 경과 후, 인산인의 제거효율은 황토 살포농도에 따라 59$\~$$99\%$까지 변하였으며, 살포농도가 증가할수록 제거효율은 높게 나타났다. 그러나, 황토 입자크기에 따른 인산인의 제거효율의 차는 그다지 크지 않았다 규산규소의 제거효율은 황토입자 크기 및 살포 양의 차이에 관계없이 평균 약 $26\%$가 일정하게 감소하였다. 해수중 황토 살포 후, 인산인의 제거기구를 파악하기 위한 인의 존재형태별 분석결과는 $99\%$ 이상의 인산인이 철성분에 의한 화학적인 결합에 의해 제거된다는 것을 나타내었고, 규산규소는 해수와 황토 내에 들어있는 양이온과의 이온교환에 의하여 제거되는 것을 시사해 주었다

• 한국지하수토양환경학회지:지하수토양환경
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• 제12권6호
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• pp.29-37
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• 2007

먹는물 수질기준(0.3 mg/L)을 자주 초과하는 고농도의 용존 철(Fe)은 특히 국내 충적층 지역 천부 지하수의 개발 이용(특히, 강변여과 적용)을 제한하는 중요한 원인이 되고 있다. 이에 본 연구에서는 반응성용질이동모델링을 이용하여 지하수 내 용존 철을 효과적으로 저감하기 위한 하나의 방법으로서 '산소가 풍부한 물을 대수층에 주입한 후 양수하는 기법의 효용성에 대하여 모사해 보았다. 모사 결과, 산소가 풍부한 물을 주입함으로써 양수된 지하수의 철 농도를 뚜렷이 저감할 수 있으며, 양수량이 주입량에 비해 4배가 되더라도 용존 철의 농도는 먹는물 수질기준 이하로 매우 낮게 유지됨을 보여주었다. 또한, 대수층 내에서의 철수산화물 침전에 의해 야기될 수 있는 크로깅 및 투수율 저하도 미미한 수준인 것으로 평가되었다. 본 논문에서는 주입-양수 기법에 의한 대수층 내에서의 철 저감의 기작과 공간적 규모에 대해서도 토의하였다.

• Bulletin of the Korean Chemical Society
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• 제26권2호
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• pp.281-284
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• 2005

The Fe/MgO catalysts with different Fe loadings (1, 4, 6, 15 and 30 wt% Fe) were prepared by a wet impregnation with iron nitrate as precursor. All of the catalysts were characterized by BET surface analyzer, X-ray diffraction (XRD), temperature-programmed reduction (TPR), and X-ray photoelectron spectroscopy (XPS). The maximum removal capacity of $H_2S$ was obtained with 15 wt% Fe/MgO catalyst which had the highest BET surface area among the measured catalysts. XRD of Fe/MgO catalysts showed that well dispersed Fe particles could be present on Fe/MgO with Fe loadings below 15 wt%. The crystallites of bulk $\alpha$-$Fe_2O_3$ became evident on 30 wt% Fe/MgO, which were confirmed by XRD. TPR profiles showed that the reducibility of Fe/MgO was strongly related to the loaded amounts of Fe on MgO support. Therefore, the highest removal efficiency of $H_2S$ in wet oxidation could be ascribed to a good dispersion and high reducibility of Fe/MgO catalyst. XPS studies indicated that the $H_2S$ oxidation with Fe/MgO could proceed via the redox mechanism ($Fe^{3+}\;{\leftrightarrow}\;Fe^{2+}$).

• 한국정밀공학회지
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• 제16권3호통권96호
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• pp.84-90
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• 1999

The finishing process for dies and molds is directly related to finished surface quality, but many parts of process depend on human labor which needs much time and value. So automatic finishing machine has been produced for dies and molds, and applied widely for finishing process. Conventionally finishing machine has applied resin bonded finishing pad as a tool, but the removal ability of pad decreases greatly as finishing process goes on. In the finishing mechanism for dies and molds, finishing process is affected severely by cutting process, so can be divided into removing cusp and smoothing surface process. So, this study investigated the application of cast iron bonded diamond pellet for press dies, which is considered to have better characteristics than the other metal bonded pellets. The finishing characteristics were compared the between finishing pellet and pad. And finishing performance was appraised as the several cutting surfaces.

• 청정기술
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• 제12권2호
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• pp.87-94
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• 2006

철과 니오븀의 몰비가 1/0, 10/1, 5/1, 1/1, 1/5, 1/10 및 0/1 인 철-니오븀 촉매상에서 일산화탄소에 의한 아황산가스의 원소 황으로의 환원이 고정층 흐름반응기에서 연구되었다. 촉매 활성 및 선택도 면에서 우수한 상승효과를 철-니오븀 촉매에서 관찰할 수 있었으며, 가장 우수한 촉매 현상은 철과 니오븀의 몰비 1/1 촉매에서 관찰되었다. 활성화된 철-니오븀 촉매의 활성상은 XRD와 XPS 의 분석결과 $FeS_2$ 로 확인되었다. 일산화탄소에 의한 아황산가스의 선택적 환원은 카르보닐 황화물 반응중간체 메커니즘을 따르는 것으로 나타났다.

• 한국수처리학회지
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• 제26권6호
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• pp.13-26
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• 2018

This research was conducted to elucidate the removal mechanism of heavy metals and sulfate ion from acid mine drainage(AMD) by porous zeolite-slag ceramics (ZS ceramics) packed in a column reactor system. The average removal efficiencies of heavy metals and sulfate ion from AMD by the 1:3(Z:S) porous ZS ceramics in the column reactor under the HRT condition of 24 hours were Al 97.5%, As 98.8%, Cd 86.1%, Cu 96.2%, Fe 99.7%, Mn 64.1%, Pb 97.2%, Zn 66.7%, and $SO_4{^{2-}}$ 76.0% during 121 days of operation time. The XRD analysis showed that the ferric iron from AMD could be removed by adsorption and/or ion-exchange on the porous ZS ceramics. In addition it was known that Al, As, Cu, Mn, and Zn could adsorb or coprecipitate on the surface of Fe precipitates such as schwertmannite, ferrihydrite, or goethite. The EDS analysis revealed that Al, Fe, and Mn, which were of relatively high concentration in the AMD, would be adsorbed and/or ion-exchanged on the porous ZS ceramics and also exhibited that Al, Cu, Fe, Mn, and Zn could be precipitated as the form of metal hydroxide or sulfate and adsorbed or coprecipitated on the surface of Fe precipitates. The microscopic results on the porous ZS ceramics and precipitated sludge in a column reactor system suggested that the heavy metals and sulfate ion from AMD would be eliminated by the multiple mechanisms of coprecipitation, adsorption, ion-exchange as well as precipitation.