• 한국가스학회:학술대회논문집
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• 2005.10a
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• pp.135-140
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• 2005

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2006.05a
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• pp.176-179
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• 2006

• 한국가스학회:학술대회논문집
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• 2005.05a
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• pp.214-214
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• 2005

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1999.11a
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• pp.237-240
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• 1999

철강, 석유화학공업 등 각종 산업에서 발생되는 부생가스, 현재 문제가 되고 있는 도시 폐기물, 폐플라스틱 뿐만 아니라 바이오매스 등 미활용에너지원이나 석탄을 열분해 또는 가스화 하거나 천연가스를 개질하여 만들어진 합성가스를 이용하여 기존의 간접법이 아닌 직접 합성으로 디메틸에테르(dimethyl ether, BME)를 생산하는 기술은 산업체의 생산원가 절감, 에너지절약 및 환경오염 감소 등 일석삼조의 효과를 기대할 수 있다.(중략)

• 한국가스학회:학술대회논문집
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• 2005.10a
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• pp.131-134
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• 2005

• Bulletin of the Korean Chemical Society
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• v.31 no.6
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• pp.1628-1632
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• 2010

Porous ${\eta}-Al_2O_3$ was synthesized by modified sol-gel method using ionic liquid as a templating material. The addition of ionic liquid assisted to increase the surface area of alumina. However, the acidity of aluminas prepared with ionic liquids was hardly affected regardless the change of its structural properties. Among the ionic liquids used in this study, 1-butyl-3-methylimidazolium hexafluorophosphate ([Bmim][$PF_6$]) was the most effective ionic liquid to produce porous ${\eta}-Al_2O_3$ particles. The catalytic performance of these aluminas has been investigated in dehydration of methanol to produce dimethyl ether. The alumina prepared with [Bmim][$PF_6$] outperformed the other aluminas except ${\eta}-Al_2O_3$ without modification in this reaction.

• Transactions of the Korean hydrogen and new energy society
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• v.26 no.5
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• pp.477-483
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• 2015

LFG (Land-Fill Gas) includes components of $CH_4$, $CO_2$, $O_2$, $N_2$, and water. The preparation of synthesis gas from LFG as a DME (Dimethyl Ether) feedstock was studied by methane reforming of $CO_2$, $O_2$ and steam over $NiO-MgO-CeO_2/Al_2O_3$ catalyst. Our experiments were performed to investigate the effects of methane conversion and syngas yield on the amount of LFG components over $NiO-MgO-CeO_2/Al_2O_3$ catalyst. Results were obtained through the methan reforming experiments at the temperature of $900^{\circ}C$ and GHSV of 8,800. The results were as following; it has generally shown that syngas yield increase with the increase of oxygen and steam amounts and then decrease. Highly methane conversion of above 98% and syngas yield of approximately 60% were obtained in the feed of gas composition flow-rate of 243ml/min of $CH_4$, 241ml/min of $CO_2$, 195ml/min of $O_2$, 48ml/min of $N_2$, and 450ml/min of steam, respectively, under reactor pressure of 1 bar for 200 hrs of reaction time. Also, it was shown that catalyst deactivation by coke formation was reduced by excessively adding oxygen and steam as an oxidizer of the methane reforming.

• 한국신재생에너지학회:학술대회논문집
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• 2005.11a
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• pp.689-692
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• 2005

2020년까지 전 세계 수송에너지의 수요가 현재의 2배까지 증가할 것으로 예상되면서 석유 자원의 안정적 공급이 어려워지기 이전에 이를 대체할 수 있는 에너지원 개발이 시급하다. 이러한 노력의 일환으로 최근 들어 대두되고 있는 가스화용융 기술은 석탄 폐기물 등으로부터 합성가스를 생산하는 고청정 고효율 기술이다. 여기에서 생산되는 합성가스는 천연가스를 대체하여 전기 및 화학원료를 생산하기 위한 원료로 이용 가능하다. 폐기물로부터 가스화용융기술을 통하여 생산되는 합성가스로부터 DME(dimethyl ether)를 생산할 수 있다. 가스화용융기술로부터 생산되는 합성가스는 자체의 일산화탄소와 수소의 조성비가 DME를 합성하는데 적당하다고 알려져 있다. DME는 에너지원의 다원화와 대기오염 물질의 저감, 지구온난화 대응 등과 아울러 제 4세대 수송 연료로 부각되고 있다. DME를 합성하는 방법은 합성가스로부터 메탄올의 합성 단계를 거친 후 DME를 합성하는 간접법과 단일단계의 반응에서 합성가스로부터 직접적으로 DME를 합성하는 직접법이 있다. 현재는 화학 평형적 측면 경제적 측면에서 이점을 가지고 있는 직접법에 관한 연구가 활발히 이루어지고 있다. DME 직접합성법에서는 메탄올 합성 촉매와 메탄올 탈수촉매의 물리적 혼합에 의한 혼성촉매가 주로 이용되고 있는 것으로 알려져 있다 본 연구에서는 일산화탄소와 수소로 이루어진 합성 가스로부터 직접 DME를 생산할 수 있는 직접 합성 공정에 적용 가능한 고효율 촉매 기술을 개발하기 위해 상용촉매의 스크린 테스트를 수행하였다. 상용촉매로는 sud-chemi사에서 메탄을 합성 촉매와 탈수촉매를 각각 구입하였으며, 이들 촉매를 원하는 조성비로 물리적으로 혼합한 다음 반응온도 ($250-290^{\circ}C$) 압력 (30-50 atm), $H_2$/CO 몰비 (0.5-2.0) 등의 다양한 반응조건 하에서 스크린 테스트를 수행하였다.대장조영영상을 얻을 수 있어 대장암의 위치에 관한 정보를 삼차원적으로 제공하므로 대장암의 성상을 정확히 알 수 있는데 도움을 주었다.요인은 없는 것으로 사료된다. 이 중 2예의 CT에서 선상 혹은망상형의 음영을 보였다. 결론: 유방암 환자의 방사선 치료 후 CT 소견은 방사선 치료의 방법에 따라 폐첨부 혹은 폐의전면 흉막하 부위에 선상 혹은 망상형의 음영으로서 방사선 폐렴 혹은 섬유화 소견이다. CT는 단순 흉부 촬영보다 이상 소견의 발견이 쉽다.이러한 소견은 후에 합병될 수 있는 다른 폐질환의 감별 진단에 도움이 될 것으로 보인다.moembolization via the radial artery approach were involved in this study. All underwent Allen’s test to check ulnar arterial patency. In all cases, we used the radial approach hepatic artery (RHA) catheter designed by ourselves, evaluating t\ulcorner selec\ulcorneron ability of the hepatic artery using an RHA cathter, the number of punctures, the procedure time, and compression time at the puncture site as well as complications occurring during and after the procedure. Results: Except for three in which puncture failure, brachial artery variation or hepatic artery variation occurred, all procedures were successful. The mean number of punctures was 3.5, and the

• Korean Chemical Engineering Research
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• v.45 no.6
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• pp.566-572
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• 2007

Two hybrid catalysts for the direct synthesis of DME were prepared and the catalytic activity of these catalysts were investigated. The hybrid catalyst for the direct synthesis of DME was composed as the catalytic active components of methanol synthesis and dehydration. The methanol synthesis catalyst was formed from the precursor contained Cu and Zn, the methanol dehydration catalyst was used ${\gamma}-Al_2O_3$. As PM-CZ+D and CP-CZA/D, Two hybrid catalysts were prepared by physical mixing method (PM-CZ+D) and precipitation method (CP-CZA/D), respectively. PM-CZ+D was prepared by physically mixing methanol synthesis catalyst and methanol dehydration catalyst, CP-CZA/D was prepared by depositing Cu-Zn or Cu-Zn-Al components on ${\gamma}-Al_2O_3$. The crystallinity and the surface morphology of synthesized catalyst were analyzed by X-ray diffraction (XRD) and scanning electron microscope (SEM) to investigate the physical property of prepared catalyst. And BET surface area by $N_2$ adsorption and the surface area of Cu by $N_2O$ chemisorption were investigated about the hybrid catalysts. In addition, catalytic activity of these hybrid catalysts was examined with varying reaction conditions. At that time, the reaction temperature of $250{\sim}290^{\circ}C$, the reaction pressure of 50~70 atm, the $[H_2]/[CO]$ mole ratio of 0.5~2.0 and the space velocity of $1,500{\sim}6,000h^{-1}$ were investigated the catalytic activity. From these results, it was confirmed that the reactivity of CP-CZA/D was higher than that of PM-CZ+D. When the conditions of reaction temperature, pressure, $[H_2]/[CO]$ ratio and space velocity were $260^{\circ}C$, 50 atm and 1.0, $3,000h^{-1}$ respectively, CO conversion using CP-CZA/D hybrid catalyst was 72% and the CO conversion of CP-CZA/D was more than 20% compared with the CO conversion of PM-CZ+D. It was known that Cu surface area of CP-CZA/D hybrid catalyst was higher than that of hybrid PM-CZ+D catalyst using $N_2O$ chemisorption. It was assumed that the catalytic activity was improved because Cu particle of hybrid catalyst prepared by precipitation method was well dispersed.

• Korean Chemical Engineering Research
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• v.47 no.5
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• pp.519-530
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• 2009

Reducing the emission of carbon dioxide, which is the main contributor to the green house effect, is becoming a global hot issue. Great attention has been thus given to utilization of carbon dioxide rather than just capturing and isolating it because it could convert carbon dioxide to high-value chemicals. In this paper, recent research trends are investigated on the catalytic conversion of carbon dioxide to syngas in the context of $CH_4$, dry-reforming, trireforming, and the electro-catalytic conversion of carbon dioxide through SOFC(Solid Oxide Fuel Cell) system. Research trends for utilizing syngas to high-value-added useful products, mainly fuel such as DME(Dimethyl Ether) are also discussed.