• Clean Technology
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• v.18 no.4
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• pp.426-431
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• 2012

Carbon-rich coal can be utilized as a fuel for direct carbon fuel cell (DCFC). However, left-behind ash after the electrochemical oxidation may hinder the electrochemical reactions. In this study, we produced ash-free coal (AFC) by thermal extraction and then tested it as a fuel for DCFC. DCFC was built based on solid oxide electrolyte and the electrochemical performance of AFC mixed with $K_2CO_3$ was compared with AFC only. Significantly enhanced power density was found by catalytic steam gasification of AFC. However, an increase of the power density by catalytic pyrolysis was negligible. This result indicated that a catalyst activated the steam gasification reactions, producing much more $H_2$ and thus increasing the power density, compared to AFC only. Results of a quantitative analysis showed much improved kinetics in AFC with $K_2CO_3$ in agreement with DCFC results. A secondary phase of potassium on yttria-stabilized zirconia (YSZ) surface was observed after the cell operation. This probably caused poor long-term behavior of AFC with $K_2CO_3$. A thin YSZ (30 ${\mu}m$ thick) was found to be higher in the power density than 0.9 mm of YSZ.

• Applied Chemistry for Engineering
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• v.9 no.3
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• pp.355-360
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• 1998

Reduction activity of precious metal-loaded HZSM-5 for NO has been studied and was compared to that of Cu-HZSM-5 in the presence of excess oxygen. It was found that among the catalysts used in this study, Ru-HZSM-5 was the most active catalyst for the reduction of NO to $N_2$ in the absence of hydrocarbon reductant. The highest conversion obtained was 45%. No severe inhibition of water vapor to the reduction was observed. It is suggested that the higher catalytic activity of Ru-HZSM-5 may result from the better ability to oxidize NO to $NO_2$ in the presence of excess oxygen. A proposed reaction mechanism for the reduction of NO to $N_2$ in the presence of excess oxygen is that NO is oxidized to $NO_2$ on the surface of Ru-HZSM-5 catalyst and the adsorbed $NO_2$ on the surface is then decomposed to $N_2$. $NO_2$ is supposed to the reaction.

• Korean Chemical Engineering Research
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• v.45 no.4
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• pp.340-344
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• 2007

Catalytic upgrading of pyrolytic bio-oil produced from Japanes Larch was carried out over MCM-41 catalyst. Oil with enhanced stability was produced by the MCM-41 catalyst due to transform oxygen known as a main cause for the instability of bio-oil into $H_2O$, CO and $CO_2$. In addition, the MCM-41 catalyst produced the larger amount of phenolic compounds in the pyrolytic bio-oil product compared with that in the bio-oil produced without catalyst. Especially, the catalytic activity of Al-MCM-41 for the bio-oil upgrading was higher than that of Si-MCM-41 because Al-MCM-41 has the larger amount of acid sites. Also, the better reforming result was obtained when pyrolytic bio-oil vapor passed through catalytic layer rather than Japanese Larch was mixed with catalyst directly.

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2001.11a
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• pp.295-296
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• 2001

동물 축사, 폐수 및 하수처리장, 피혁공장, 생선처리시설 등에서 주로 발생하는 암모니아(NH$_3$) 및 트리메틸아민(($CH_3$)$_3$N)과 같은 악취 물질 제거에 대한 많은 연구가 진행되고 있다. 악취 물질에 대한 처리 기술에는 직접 산화법, 고온 연소법, 효소분해법, 흡착법, 촉매 산화법, 플라즈마 제거법 등과 같은 악취 물질을 분해 제거하는 방법과 단순히 악취를 은폐시키는 마스킹법이 있다. (중략)

• Journal of the Korean Chemical Society
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• v.21 no.2
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• pp.89-93
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• 1977

Faujasite type zeolite synthesized from kaolin minerals was cation-exchanged and the catalytic activities of $1-Butene{\rightarrow}2-butene$ took place readily even on zeolites having no strong acid sites. The order of activity for isobutene formation was La > H > Zn > Na-faujasite, La-faujasite showing much higher activity. The same trend was observed for propylene formation except that both La-and H-faujasite showed comparable activity. The results seem to indicate that the activities for 1-buten cracking and isomerization on zeolite are directly related to the strength and concentration of the acid sites on zeolites.

• Proceedings of the Korean Society of Applied Pharmacology
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• 1995.04a
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• pp.130-130
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• 1995

AM, SM 및 ASA는 수용액중에서 겉보기 1차반응에 따라 분해되었으며 보존온도가 높을수록 분해가 촉진되는 온도 의존성을 나타내었다. AM의 분해경로는 pH 1.22 및 pH 7.0 이상에서는 AM$\longrightarrow$ SM $\longrightarrow$ SA의 경로로 주로 분해되었으며 pH 2.01 - 6.08의 범위에서는 AM $\longrightarrow$ASA$\longrightarrow$SA의 경로로 분해되는 양상을 보였다. 또 pH가 분해에 미치는 영향을 pH-rate profile로 나타낸 결과 AM, SM 및 ASA의 최대안정 pH는 각각 4.0, 3.0, 2.0 부근이 있고 이 조건에서의 분해 반감기는 114, 168, 113 hr로 나타났다. 전체적으로 보면 pH 2.0 이하에서는 ASA가 AM 보다 약간 안정한 편이나 pH 2.0-8.0 사이에서는 AM의 분해속도가 ASA보다 현저히 낮았다. 또 AM은 pH 7.0 이상에서, SM은 pH 6.0 이상에서, ASA는 9.0 이상에서 특수염기촉매반응에 따라 분해가 이루어지는 것을 알 수 있었다. 이온강도($\mu$)의 영향으로는 pH 7.0에서 이온강도가 0.115에서 1.0으로 증가할수록 $\mu$$^{1}$2/에 대해 AM의 분해속도정수가 직선적으로 완만하게 감소되었다. 또 완충수용액 중 AM의 가수분해 억제효과를 검토하기 위해 시클로덱스트린류를 첨가하였을 때, $\beta$-시클로덱스트린과 히드록시프로필기-$\beta$-시클로덱스트린은 AM의 분해를 각각 1.6배 및 1.1배 촉진시켜 촉매적으로 작용하였으며 디메칠-$\beta$-시클로덱스트린은 약 3.2배 분해속도를 억제시켜 안정화제로 작용하였다.Zn^{2+}$, soybean trypsin inhibtor에 의해 25～50% 정도, serine proteinase inhibitor인 phenylmethylsulfonyl floride에 의해 80%정도 활성이 억제되는 특성이 있음을 규명하였다.면역환성 (immunoreactivity)이 나타났고 pyramidal cell layer (PCL)와 glia에 SOD-1이 강하게 염색되었다. APT 병용 투여로 상당수의 경련이 일어나지 않은 흰쥐는 해마의 DG에 FRA가 경미하게 염색되었고, PCL에 SOD-1도 경미하게 나타났으나, 경련이 나타난 쥐에서는 KA만을 투여한 흰쥐와 구별되지 않았다. 이상의 APT의 항산화 효과는 KA로 인한 뇌세포 변성 개선에 중요한 인자로 작용할 것으로 사료되나, 보다 명확한 APT의 기전을 검색하고 직접 임상에 응응하기 위하여는 보다 다양한 실험 조건이 보완되어야 찰 것으로 생각된다. 항우울약들의 항혈소판작용은 PKC-기질인 41-43 kD와 20 kD의 인산화를 억제함에 기인되는 것으로 사료된다.다. 것으로 사료된다.다.바와 같이 MCl에서 작은 Dv 값을 갖는데, 이것은 CdCl$_{4}$$^{2-}$ 착이온을 형성하거나 ZnCl$_{4}$$^{2-}$ , ZnCl$_{3}$$^{-}$같은 이온과 MgCl$^{+}$, MgCl$_{2}$같은 이온종을 형성하기 때문인것 같다. 한편 어떠한 용리액에서던지 NH$_{4}$$^{+}$의 경우 Dv값이 제일 작았다. 바. 본 연구의 목적중의 하나인 인체유해 중금속이온인 Hg(II), Cd(II)등이 NaCl같은 염화물이 함유된 시료용액에 공해이온으로 존재할 경우 흡착에 의한 제거가 가능하다. 한편 이같

• Applied Chemistry for Engineering
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• v.28 no.6
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• pp.619-625
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• 2017

In this study, the formation of hydroxyl radical and decomposition characteristics of bisphenol A (BPA) was investigated by quantifying hydrogen peroxide formed as a reaction by-product during the formation stage of hydroperoxyl radical. The direct oxidation reaction by ozone only decomposed BPA just like the Criegee mechanism under the condition where radical chain reactions did not occur. Non-selective oxidation reactions occurred under the conditions of pH 6.5 and 9.5 where radical chain reactions do occur, confirming indirectly the formation of hydroxyl radical. The decomposition efficiency of BPA by the added catalysts appeared in the order of $O_3$/PAC ${\geq}$ $O_3/H_2O_2$ > $O_3$/high pH > $O_3$ alone. 0.03~0.08 mM of hydrogen peroxide were continuously measured during the oxidation reactions of ozone/catalyst processes. In the case of $O_3$/high pH process, BPA was completely decomposed in 50 min of the oxidation reaction, but reaction intermediates formed by oxidation reaction were not oxidized sufficiently with 29% of the removal ratio for total organic carbon (TOC, selective oxidation reaction). In the case of $O_3/H_2O_2$ and $O_3$/PAC processes, BPA was completely decomposed in 40 min of the oxidation reaction, and reaction intermediates formed by the oxidation reaction were oxidized with 57% and 66% of removal ratios for TOC, respectively (non-selective oxidation reactions).

• Proceedings of the Korean Vacuum Society Conference
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• 2013.08a
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• pp.71.1-71.1
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• 2013

메탄가스와 이산화탄소는 지구온난화 가스이기 때문에 배출규제가 점차 강화될 것으로 전망되고 있다. 또한 이들 가스는 매립지 또는 바이오 공정을 통해 발생되는 가스이기 때문에 단순히 배출을 억제하는 데 그치지 않고 보다 적극적으로 활용해야할 필요성이 있다. 현재 메탄과 이산화탄소를 동시에 활용하는 기술로는 촉매공정을 통해 메탄과 이산화탄소를 수소와 일산화탄소로 전환하는 방법이 대표적이나, 본 공정은 $800{\sim}900^{\circ}C$의 고온조건을 필요로 하고 고압조건에서 다량으로 생성되는 탄소에 의한 촉매 활성도의 저하문제로 인해 해당 기술의 실제 보급에 어려움이 있는 것으로 알려져 있다. 한편, 플라즈마를 활용한 메탄가스 개질(reforming) 기술은 고온 플라즈마인 경우 60~70년 전부터 상용화 사례가 있으며, 저온 플라즈마의 경우는 약 10여 년 전부터 개질반응의 공정온도를 낮추려는 연구를 중심으로 기초연구가 수행되어왔다. 이들 플라즈마를 활용한 메탄개질 기술은 메탄의 직접분해, 부분산화, 수증기 개질 및 건식개질 등으로 분류되는 데, 최근 지구온난화가스인 이산화탄소의 처리에 대한 관심이 높아지면서 이산화탄소를 활용하는 건식개질 기술에 대한 관심이 높아지고 있는 상황이다. 현재 플라즈마 건식개질기술에서 주된 이슈는 높은 전력비용이고, 이를 낮추기 위해 촉매를 활용하거나 플라즈마 발생을 최적화하려는 연구가 진행되고 있다. 본 발표에서는 플라즈마를 활용한 건식개질 기술의 장단점, 실용화 가능성 및 향후의 과제를 다루고 있으며, 이를 위해 기계연구원에서의 연구결과 및 국내외 연구실의 결과를 살펴보았다.

• Applied Chemistry for Engineering
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• v.22 no.6
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• pp.627-630
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• 2011

We focus on a catalytic process based on direct injection method that can produce high-quality oils of gasoline and kerosene with various carbon-number feed oils. The reaction characteristics of a commercial catalyst were analyzed using a spouted bed reactor. Decane and pentadecane were used to compare the characteristics of the fixed bed and the spouted bed reactor. The yield of gasoline plus kerosene was highest at the reaction temperature of $550^{\circ}C$. For the spouted bed reactor, the at-a-pulse injection was more effective for catalytic cracking of feed oils than multiple consecutive injections. The reaction activity became higher as the carbon number of feed oil is larger.

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 2008.05a
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• pp.111-114
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• 2008

The performance evaluation of a micro monopropellant thruster is described in this paper. The platinum which has stable physical and chemical properties is used as a catalyst. The ceramic form, named Isolite is chosen as a catalyst bed. Hydrogen peroxide whose concentration is up to 90wt% is supplied into thruster by direct pressurization with nitrogen gas. The $c^*$ efficient is calculated to evaluate the performance of a thruster. The pressure rise time, pressure decent time and reaction delay are synthetically considered.