• 한국철도학회논문집
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• 제18권5호
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• pp.466-470
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• 2015

본 연구에서는 선로상의 소규모 유류오염 도상자갈을 대상으로 펜톤산화를 적용하였다. 이를 위해 현장의 오염도상자갈을 채취하여 실험실에서 주요인자들에 대한 실험을 수행하였으며, 이 후 소규모로 오염된 역사 내 선로에서 원위치 펜톤산화의 적용가능성을 확인하였다. 그 결과, 실험실 조건에서는 0.1 mol Fe/L $H_2O_2$의 조건으로 도상자갈 잔류 TPH 농도를 약 1,000 mg/kg-ballast 수준으로 낮출 수 있었다. 그러나 원위치 현장적용에서는 자갈궤도의 배수특성으로 인해 $H_2O_2$의 상당량이 충분히 반응하지 못하고 하부로 배출되어 펜톤반응의 현장적용성 향상을 위한 추가적인 연구가 요구된다.

• 청정기술
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• 제23권2호
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• pp.158-162
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• 2017

철, 구리, 알루미늄, 니켈 등의 금속을 에칭하기 위한 에칭액으로 $FeCl_3$ 용액이 사용되며, 에칭 과정에서 $Fe^{3+}$가 $Fe^{2+}$로 환원되면서 에칭속도를 저하시키고, 에칭효율이 감소하게 된다. 또한 에칭 후 발생하는 염화철 에칭폐액은 환경적, 경제적으로 문제를 지니기 때문에 에칭액을 재생하여 재사용 할 필요가 있다. 본 연구에서는 $FeCl_2$ 용액에 HCl을 첨가한 후, 산화제로 $H_2O_2$, $NaClO_3$를 첨가하여 용액 내 $Fe^{2+}$를 산화시켰으며, 산화과정에서 산화-환원전위(ORP)와 산화율간의 관계를 조사하였다. ORP는 $H_2O_2$와 $NaClO_3$의 농도가 증가함에 따라 증가하였으며, 산화가 진행되면서 점차 감소하여 산화가 완료된 후에 일정한 ORP를 유지하였다. Nernst 식과 일치하는 결과를 보였다. 또한 충분한 양의 HCl 및 $H_2O_2$, $NaClO_3$를 첨가하였을 경우, 약 99% 이상 산화가 이루어짐을 알 수 있었다.

• 대한환경공학회지
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• 제33권10호
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• pp.723-730
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• 2011

본 연구는 토양이나 지하수 원위치 화학적 산화법(In-Situ Chemical Oxidation, ISCO)에서 사용할 수 있는 산화제 Persulfate를 상온에서 활용할 수 있도록 RDX를 처리대상물질로 연구하였다. Persulfate로 RDX를 처리한 결과, 반응은 유사1차반응으로 나타났으며 온도가 증가함에 따라 분해속도도 증가하였고, 이 때 활성화에너지(Activation energy)는 $1.14{\times}10^2kJ/mol$으로 산정되었다. Persulfate에 의한 RDX의 분해반응속도는 pH에 비례하여 증가하였으며, pH값이 4, 6, 8일 때 반응속도의 변화가 크지 않았다. 그러나 pH 10에서는 13배 이상 증가하였는데, persulfate에 의한 산화가 아니라 alkaline hydrolysis로 나타났다. Persulfate에 의한 RDX의 분해반응속도는 persulfate/RDX의 몰 비율에 따라 선형적으로 증가하였으며, $70^{\circ}C$에서 측정한 비례상수는 $4{\times}10^{-4}$ ($min^{-1}$/몰 비율)이었다. 용액 내 천연유기물(NOM) 농도가 증가함에 따라 persulfate에 의한 RDX 분해속도 선형 감소하였으며 $70^{\circ}C$, persulfate/RDX 몰비 10/1에서 측정한 비례상수는 $1.21{\times}10^{-4}$ ($min^{-1}{\cdot}L/mg-NOM$)이었다. 반응속도의 감소는 NOM 첨가량에 선형적으로 비례하였다. NOM 20 mg/L을 첨가한 반응의 Ea값은, 무첨가 반응에서 산정된 Ea값과 3.3% 오차에 불과하였는데, 이는 NOM의 첨가가 본래의 산화반응을 변화시키지는 않음을 의미한다.

• 자원리싸이클링
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• 제26권2호
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• pp.18-24
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• 2017

$FeCl_3$ 용액은 금속의 에칭용액으로 사용되며, 사용 후 발생하는 $FeCl_3$ 에칭폐액은 환경적, 경제적으로 문제를 지니기 때문에 에칭액을 재사용할 필요가 있다. 본 연구에서는 $FeCl_2$ 용액에 HCl을 첨가 한 후, 산화제로 $H_2O_2$를 첨가하여 용액 내 $Fe^{2+}$를 산화시켰으며, 산화과정에서 산화-환원전위(ORP)와 산화율 간의 관계를 조사하였다. ORP는 HCl과 $H_2O_2$의 농도가 증가함에 따라 증가하였으며, 산화가 진행되면서 점차 감소하여 Nernst 식과 일치하는 결과를 보였다. 또한 충분한 양의 HCl과 $H_2O_2$를 첨가하였을 경우, 약 99% 이상 산화가 이루어짐을 알 수 있었다.

• 센서학회지
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• 제29권2호
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• pp.128-132
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• 2020

Total organic carbon (TOC) analysis equipment, which was previously used to prevent eutrophication in advance, is heavy, bulky, and expensive; therefore, so it is difficult to be carried and has been used as an experimental unit. In this study, a through-carbon analysis chip that integrates pretreatment through photocatalytic oxidation and carbon dioxide measurement using a pH indicator was investigated. Both the total carbon - inorganic carbon method and the nonpurgeable organic carbon (NPOC) measurement method require an acidification part for injecting an acid solution for inorganic carbon measurement and removal, an oxidation part for total carbon or NPOC oxidation and a measurement part for Carbon dioxide (CO₂) measurement. Among them, the measurement of oxidation and CO₂ requires physical technology. The proposed TOC analysis chip decomposed into CO₂ as a result of the oxidizing of organic carbon using a photocatalyst, and the pH indicator that was changed by the generated CO₂ was optically measured. Although the area of the sample of the oxidation part and the pH indicator of the measurement part were distinguished in an enclosed space, CO₂ was quantified by producing an oxidation part and a measurement part that shared the same air in one chip. The proposed TOC analysis chip is less expensive and smaller, cost and size are disadvantages of existing organic carbon analysis equipment, because it does not require a separate carrier gas to transport the CO₂ gas in the oxidation part to the measurement part.

• 한국물환경학회지
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• 제18권2호
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• pp.169-187
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• 2002

The effects of important parameters such as reaction time and pH on the Fenton's process were evaluated using a batch reactor. It was proven that organic materials and heavy metals in leachate could be successfully removed by Fenton's reagent. Favorable operation conditions were investigated. It was observed that the reaction between ferrous iron and hydrogen peroxide with the production of hydroxyl radical was almost complete in 10 minutes. That is, the oxidation of organic materials by Fenton's reagent was so fast that it was complete in 30 minutes with batch experiments. With the formation of carbonic acid, pH of the batch reactor decreased to favorable acidic conditions without acid addition. The oxidation of organic materials in the leachate showed a pH dependence and was most efficient in the pH range of 2-3.

• Corrosion Science and Technology
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• 제2권3호
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• pp.148-154
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• 2003

The addition of Ni leads to the formation of protective rust layer on steel and subsequently high corrosion resistance of steel in $Cl^-$-containing environment. $\alpha$-FeOOH, $\beta$-FeOOH, $\gamma$-FeOOH and $Fe_3O_4$ are formed mainly on steels exposed to $Cl^-$-containing environment. As the first work of this kind, this study reports the influence of Ni on the oxidation behavior of $Ni_xFe_{1-x}(OH)_2$ in $Cl^-$-containing solution at two different pH regions(condition I under which the solution pH is allowed to decrease and condition I under which solution pH is maintained at 8) where $\gamma$-FeOOH and $Fe_3O_4$ are predominantly formed, respectively, upon oxidation of $Fe(OH)_2$, In the presence of Ni(II) in the starting solution, the formation of $\beta$-FeOOH was facilitated and the formation of $\gamma$-FeOOH was suppressed with increasing Ni(II) content and with increasing oxidation rate of Fe(II). Ni(II) was found to have $Fe_3O_4$-suppressing effect under condition II.

• 한국대기환경학회지
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• 제13권1호
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• pp.91-98
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• 1997

Y-zeolite and ${\gamma}$-Al$_2$O$_3$ were used as supports on CO and $C_3$H$_{6}$ oxidation for diesel emission control. The catalysts composed of Pd and Pt as active components were wash coated on honeycomb type ceramic substrate. The oxidation of CO and $C_3$H$_{6}$ was carried out over prepared honeycomb in a fixed bed continuous reactor in the temperature range of 20$0^{\circ}C$~50$0^{\circ}C$ and 20,000 GHSV (h$^{-1}$ ). Surface area of Y-zeolite was larger than that of ${\gamma}$-Al$_2$O$_3$ due to channel structure of Y-zeolite. Therefore, high conversion of CO and $C_3$H$_{6}$ could be obtained because of good dispersion of active metals over Y-zeolite. The honeycomb used Y-zeolite as a support showed higher $C_3$H$_{6}$ conversion than that of ${\gamma}$-Al$_2$O$_3$ due to better cracking and isomerization activity of Y-zeolite. PdPt catalyst showed high conversion of CO and $C_3$H$_{6}$ at low temperature region, 20$0^{\circ}C$~30$0^{\circ}C$, for their synergy effects. PdPt/Y-Zeolite catalyst could achieve more than 80％ conversion of $C_3$H$_{6}$ at 30$0^{\circ}C$. The use of Y-zeolite as a support increased CO and $C_3$H$_{6}$ conversion, and decreased SO$_2$ conversion very effectively. Y-zeolite found to have a good adaptability as a support for the diesel emission after treatment system.

• 한국물환경학회지
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• 제21권3호
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• pp.267-273
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• 2005

Dye wastewater generally contains strong color and non-biodegradable materials. Therefore, the conventional wastewater treatment plant can hardly meet the regulation of wastewater effluent water. In this study, a pilot plant of the conventional process followed by advanced oxidation process (AOP), was set up to treat the dying wastewater. The treatment efficiencies on the various candidate processes, such as ozone alone, UV alone, ozone/UV, $ozone/H_2O_2$, $H_2O_2/UV$ and $ozone/UV/H_2O_2$, were investigated in the various ozone and $H_2O_2$ doses. As the results, the $ozone/H_2O_2$ process, among the tested processes, showed the highest efficiency for removing color and $COD_{Cr}$. For color removal, the ozone alone process was enough without combining UV or $H_2O_2$. No significantly enhanced efficiency for removing color and $COD_{Cr}$ by UV irradiation was observed because of the very low transmittance of UV light in dye wastewater.

• 한국표면공학회:학술대회논문집
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• 한국표면공학회 1999년도 춘계학술발표회 초록집
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• pp.5-5
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• 1999

A novel process is proposed to improve oxidation resistance of Ti-Al intermetallic compounds at elevated temperatures by both Cr addition and pre-sulfidation, where TiAl alloys withlor without Cr addition were sulfidized at 1173K for 86.4ks at a 1.3 Pa sulfur partial pressure in a $H_2-H_2S$ gas mixture. The pre-sulfidation treatment formed a thin Cr-Al alloy layer as well as 7~10 micrometer $TiAl_3$ and $TiAl_2$ layer, due to selective sulfidation of Ti. Oxidation resistance of the pre-sulfidation processed TiAl 4Cr alloy was examined under isothermal and heat cycle conditions between room temperature and 1173K in air. Changes in $TiAl_3$ into $TiAl_2$ and then TiAl phases as well as their effect on oxidation behavior were investigated and compared with the oxidation behavior of the TiAl-4Cr alloy as TiAl and pre-sulfidation processed TiAl aHoys. After oxidation for up to 2.7Ms a protective $Al_2O_3$ scale was formed, and the pre-formed $TiAl_3$ changed into $TiAl_2$ and the $Al_2Cr$ phase changed into a CrAlTi phase between the $Al_2O_3$ scale and $TiAl_2$ layer. The pre-sulfidation processed TiAl-4Cr alloy had very good oxidation resistance for longer times, up to 2.7 Ms, in contrast to those observed for the pre-sulfidation processed TiAl alloy where localized oxidation occurred after 81 Oks and both the TiAl and TiAl-4Cr alloys themselves corroded rapidly from the initial stage of oxidation