• 공업화학
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• 제19권6호
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• pp.624-628
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• 2008

$N_2O$는 주요 온실가스 성분의 하나로서 광화학 스모그의 유발, 산성비의 전구체 등 온실효과에 상당한 기여를 하고 있는 물질이다. 이러한 $N_2O$ 및 질소산화물을 제거하기 위하여 환원제를 이용한 Selective Catalytic Reduction (SCR) 반응 공정이 널리 사용되고 있다. 본 연구에서는 Hydrotalcite 형태의 전구체로부터 Mixed Metal Oxide 촉매를 제조하고 그를 사용하여 $N_2O$ 분해를 위한 메탄 SCR 반응 및 CO의 생성효과를 비교 연구하였다. 실험결과 $CH_4$ 환원제의 첨가는 $N_2O$의 분해 반응에 긍정적인 영향을 미치며, 최적화된 $O_2/CH_4$ 비율의 조건에서 메탄의 부분산화에 의한 SCR 반응이 가장 높은 효율을 나타내는 것을 확인할 수 있었다.

• 한국안전학회지
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• 제17권4호
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• pp.133-139
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• 2002

Core-shell polymers of inorganic/organic pair, which are consisted of both core and shell component, were synthesized by sequential emulsion polymerization using ethyl methacrylate (EMA) as a shell monomer and ammonium persulfate as initiator. We found that $CaCO_3$ core should be prepared by adding 2.0wt% SDBS(sodium dodecyl benzene sulfonate), $CaCO_3$ core/PEMA shell polymerization was carried out on the surface of $CaCO_3$ particle during EMA shell polymerization in the core-shell polymer preparation. The structure of core-shell polymer were investigated by measuring the degree on decomposition of $CaCO_3$ by HCI solution, thermal decomposition of polymer composite on thermogravimetric analyzer, glass transition temperature on differential scanning calorimeter, and morphology using scanning electron microscope.

• Macromolecular Research
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• 제12권5호
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• pp.490-492
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• 2004

We report a new method using a heating medium for the thermal decomposition of epoxy resin (EP) at temperatures ranging from 50 to 200$^{\circ}C$. EP decomposition also occurred below 50$^{\circ}C$ during a 6-day period to generate bisphenol A (BPA) at concentrations as high as 5 ppm. When polyethylene glycol was used as a heating medium, we determined the kinetics of the EP decomposition at low temperature. We determined the apparent activation energy of the overall decomposition to be 40.8 kJ/mol and the frequency factor to be 2.3${\times}$10$^3$ by monitoring the rate of BPA formation. Thus, EP is clearly unstable upon the application of heat.

• Carbon letters
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• 제6권4호
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• pp.227-233
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• 2005

Carbonization products C1, C2, C3, C4 and C5 were prepared by the carbonization of date pit in limited air, at 500, 600, 700, 800 and $1000^{\circ}C$, respectively. C1-V-600, C3-V-600, C1-V-1000 and C3-V-1000 were prepared by thermal treatment of C1 and C3 under vacuum at 600 and $1000^{\circ}C$. The textural properties were determined from nitrogen adsorption at 77 K and from carbon dioxide adsorption at 298 K. The surface pH, the FTIR spectra and the acid and base neutralization capacities of some carbons were investigated. The amounts of surface oxygen were determined by out-gassing the carbon-oxygen groups on the surface as $CO_2$ and CO. The adsorption of water vapor at 308 K on C1, C2, C3 and C4 was measured and the decomposition of $H_2O_2$ at 308 K was also investigated on C1, C2, C3, C4 and C5. The surface area and the total pore volume decreased with the rise of the carbonization temperature from 500 to $1000^{\circ}C$. The adsorption of water vapor is independent on the textural properties, while it is related to the amount of acidic carbon-oxygen groups on the surface. The catalytic activity of $H_2O_2$ decomposition does not depend on the textural properties, but directly related to the amount of basic carbon-oxygen complexes out-gassed as CO, at high temperatures.

• 한국산업융합학회 논문집
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• 제6권4호
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• pp.269-275
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• 2003

A non-thermal plasma process combined with $Cr_2O_3/TiO_2$ catalyst was applied to the decomposition of trichloroethylene (TCE). A dielectric barrier discharge reactor operated with AC high voltage was used as the non-thermal plasma reactor. The effects of reaction temperature and input power on the decomposition of TCE and the formation of byproducts including HCl, $Cl_2$, CO, NO, $NO_2$ and $O_3$ were examined. At an identical input power, the increase in the reaction temperature from 373 K to 473 K decreased the decomposition of TCE in the plasma reactor. The presence of the catalyst downstream the plasma reactor not only enhanced the decomposition of TCE but also affected the distribution of byproducts, significantly. However, synergistic effect as a result of the combination of non-thermal plasma with catalyst was not observed, i.e., the TCE decomposition efficiency in this plasma-catalyst combination system was almost similar to the sum of those obtained with each process.

• 대한화학회지
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• 제33권6호
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• pp.662-668
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• 1989

Metal-4,4',4",4"'-tetraaminophthalocyanine [Mt-$PcNH_2$, Mt = Fe(III), Co(II), Ni(II), Cu(II)] 및 Mt-$PcNH_2$가 styrene-methacrylic acid 공중합체(STMA)에 고정화된 Mt-PcSTMA를 촉매로 사용한 불균일 수용액계에서 과산화수소의 분해반응에 대한 촉매활성에 대하여 실험하였다. 이 촉매들은 효소반응과 비슷한 촉매활성을 나타내었고, Fe(III)-$PcNH_2$이 공중합체에 결합되어 고정화된 Fe(III)-PcSTMA가 가장 촉매활성이 우수하였다. 분해반응율은 높은 pH 범위에서 증가하였으며, $CN^-,\;CNS^-,\;{C_2O_4}^{-2},\;I^-$ 등의 공존 음이온의 영향을 받았다. 또한, 반응속도론적인 고찰을 통하여 열역학적 특성값을 구한 결과로부터 촉매반응이 Michaelis-Menten형의 반응기구로 진행됨을 알 수 있었다.

• 펄프종이기술
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• 제38권3호
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• pp.79-84
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• 2006

Hydrogen peroxide has been a bleaching chemical for varied pulp, especially mechanical and deinking pulp. It is catalytically decomposed by some transition metals in pulp slurry. In this paper, some metals which can be contained in pulp such as manganese, copper, iron, magnesium and calcium were used to investigate their effect on the decomposition of hydrogen peroxide. From the result, hydrogen peroxide was more decomposed in the order of Mn, Cu, $Fe^{3+}\;and\;Fe^{2+}$, while Mg and Ca had little effect on the decomposition of hydrogen peroxide. The effect of Mg/Mn ratio on the decomposition of hydrogen peroxide was also investigated. At the specific ratio of them(Mg/Mn=10), hindering effect of peroxide decomposition by Mg was decreased.

• Korean Chemical Engineering Research
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• 제43권2호
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• pp.206-214
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• 2005

$TiO_2$에 담지된 불균일 촉매상에서 ppm 수준으로 존재하는 수중 유기오염물질들을 제거하기 위한 모델반응으로 액상 trichloroethylene(TCE) 분해반응을 선정하였으며, 여러 반응변수의 동시제어가 가능하도록 디자인된 연속 흐름식 고정층 반응기 내에서 incipient wetness 기법으로 제조된 여러 전이금속 산화물 촉매들의 TCE 분해활성을 조사하였다. 선택된 반응조건에서 모델반응의 내부확산저항은 없었으며, $36^{\circ}C$의 반응온도에서 촉매표면에 흡착에 의한 액상 TCE 제거된 정도는 무시할 만하였고 촉매반응에 의해서만 제거될 수 있었다. TCE 제거반응에 대한 촉매들의 활성 및 반응시간에 따른 분해효율의 의존성은 사용된 금속 산화물 및 담지체의 종류에 따라 달라지는 것으로 나타났다. 5 wt.% $CoO_x$/$TiO_2$ 촉매는 본 대상반응에 대하여 가장 우수한 활성을 갖는 것으로 나타났으며, 반응시간의 경과 정도에 따라 TCE 분해효율이 점진적으로 증가하여 안정되는 전이구간의 존재를 확인할 수 있었다. 이와 같은 촉매활성의 반응시간 의존성은 반응 초기와 일정시간 경과 후의 $TiO_2$ 표면에 존재하는 $CoO_x$의 표면구조가 상이할 뿐만 아니라 반응시간 경과와 함께 활성이 더욱 높은 Co species의 표면노출을 암시하고 있다. $NiO_x$, $CrO_x$와 같은 금속 산화물 촉매들의 반응활성은 매우 낮은 수준이었다. $TiO_2$와 MFI를 담지체로 하여 각각 incipient wetness법과 이온교환법으로 제조된 $CuO_x/TiO_2$, Cu-MFI, $FeO_x/TiO_2$ 및 Fe-MFI의 TCE 제거효율을 반응시간의 함수로 살펴본 결과, Cu 촉매들에서 관찰되는 반응시간-분해효율 거동과는 다른 현상이 $FeO_x/TiO_2$와 Fe-MFI 촉매상에서 관찰되었다. $36^{\circ}C$의 반응온도에서 전반응시간 동안에 5 wt.% $FeO_x/TiO_2$ 촉매상에서 TCE 제거반응은 일어나지 않았으나, 1.2 wt.% Fe-MFI의 경우 반응 초기에 높은 제거율을 일정시간 동안 유지하다가 서서히 감소하는 비활성화 현상이 발생하였다. 이는 동일한 활성성분이 사용된다 할지라도 그 제조방법에 따라 촉매활성이 달라질 수 있음을 보여주고 있으며, 액상반응 중에 일어나는 활성성분의 redox cycle이 중요한 역할을 할 수 있음을 암시하고 있다. 가장 우수한 $CoO_x/TiO_2$ 촉매의 TCE 분해활성에 미치는 $CoO_x$ 담지량, 반응온도 등의 영향을 조사한 결과, 최적의 $CoO_x$ 담지량이 존재하였고 반응온도가 높을수록 TCE 제거효율은 높게 나타났다. 반응 중에 $CoO_x$ leaching에 의한 $CoO_x$의 손실이 확인되었으나 TCE 전환율에 영향을 미칠 정도는 아닌 것으로 판단되었다.

• 한국표면공학회지
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• 제32권6호
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• pp.686-694
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• 1999

Insoluble anodes of the Ta/Ir mixed metal oxide for electrodeposition of Ni-W alloy in ammoniacal citrate bath were prepared by thermal decomposition method. Ti plate was etched in boiling oxalic acid solution and coated with ethanol solution of $TaCl_{5}$ and $IrCl_4$ mixed in a fixed ratio, followed by drying and treating at various temperatures. The coating layer of these insoluble anode was characterized by SEM, EDX, XRD and DSC. The decomposition rate of citric acid in plating bath was determined by measuring the $CO_2$ gas evolved at the anodes with Gas Chromatography. Evolution of $CO_2$ gas from Ta/Ir oxide anodes decreased about 5% compared with that of Pt. The $CO_2$ gas evolution was increased with the amount of Ir-oxide in the coatings. The coatings which have more than 40% ratio of Ta content and heat-treated at the temperature higher than $400^{\circ}C$ showed better efficiency

• Bulletin of the Korean Chemical Society
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• 제33권8호
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• pp.2483-2488
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• 2012

The X-ray line broadening technique was used to calculate the grain size of MgO at 1023, 1123, 1223 K respectively either in $CO_2$ or during the thermal decomposition of magnesites in air as well as in vacuum. By referring to the conventional grain growth equation, $D^n=kt$, the activation energy and pre-exponential factor for the process in air are gained as 125.8 kJ/mol and $1.56{\times}10^8\;nm^4/s$, respectively. Ranman spectroscopy was employed to study the surface structure of MgO obtained during calcination of magnesite, by which the mechanism of grain growth was analyzed and discussed. It is suggested that a kind of highly reactive MgO is produced during the thermal decomposition of magnesites, which is exactly the reason why the activation energy of the grain growth during the thermal decomposition of magnesite is lower than that of bulk diffusion or surface diffusion.