• Journal of Ginseng Research
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• 제17권1호
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• pp.35-38
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• 1993

A new and rapid method for the hydrolysis of ginsenosides to panaxadiol or panaxatriol was developed. It is based on the microwave oven reaction, which is high temperature and high-pressure reaction. The optimal hydrolysis time using 5% $H_2SO_4$ solution was found at 10 min PTFE reaction vessel in microwave oven, which is more than 30 times faster than the conventional hydrolysis method.

• Archives of Pharmacal Research
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• 제17권5호
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• pp.389-391
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• 1994

• 한국세라믹학회지
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• 제32권2호
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• pp.227-233
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• 1995

By using homestyle microwave oven, Al-Al2O3 powder mixture could be oxidized and sintered into Al2O3 body. The differences in powder characteristics among the differently processed raw materials affect the oxidation and sintering behaviours, and these effects were more pronounced in case of microwave oven than of conventional furnace. Al-Al2O3 powder mixture was oxidized and sintered within 2hrs, which could save both processing time and energy.

• 한국결정학회지
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• 제9권1호
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• pp.44-47
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• 1998

가정용 2.45GHz 마이크로파 오븐을 사용하여 A1 금속분말과 SiO2 분말간에 SHS방법에 의하여 산화/환원 반응을 통한 Al2O3 분말과 Si분말간의 복합체를 얻을 수 있었다. 분말간의 반응을 일으키기 위한 온도까지 승온시키기 위하여는 SiC 분말을 susceptor로 이용한 마이크로파 복합가열(Microwave Hybrid Heating)방법을 사용하여 분당 100℃의 승온 속도로 가열하였으며 반응은 850℃ 근처에서 일어났으며 가열 속도는 반응이 시작되면서 분당 200℃ 이상의 온도상승이 일어나면서 원하는 반응을 얻을 수 있었다.

• 공업화학
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• 제18권4호
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• pp.344-349
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• 2007

마이크로파 가열(microwave heating)에 의하여 제올라이트 NaY를 합성하였으며, 그 결과를 기존의 가열 방법(conventional heating)에 의하여 합성한 결과와 비교하였다. 같은 승온 속도를 사용하였을 때는 마이크로파에 의하여 가열하였을 때가 기존의 가열 방법에 비하여 NaY 결정 생성의 유도 기간(induction period)이 감소하였으며 결정의 생성 속도가 증가하였다. 또한 마이크로파의 사용 여부와 관계없이 승온 속도가 빠를 때도 유도 기간이 감소하고 결정 생성 속도가 증가하였다. 빠른 승온 속도에서 합성하였을 때 최종 결정의 크기가 크며, 이는 마이크로파의 사용에 의하여 더욱 증가하였다. 빠른 승온 속도에서는 반응 시간이 짧아져서 NaY의 합성에 소모되는 에너지 소모량은 감소하였다. 본 연구의 조건에서는 에틸렌글리 콜조(ethylene glycol bath)를 사용한 기존 가열 방법에서의 에너지 소모량이 마이크로파 가열보다 적게 나타났는데, 이는 마이크로파 에너지를 사용하는 것이 항상 효율적인 것만은 아니라는 것을 말해준다. 그러나 승온 속도를 적절히 조절하면 마이크로파 가열에 의해서 에너지 면에서 보다 효율적으로 NaY를 합성할 수 있다는 것을 알 수 있었다

• 대한치과보철학회지
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• 제34권4호
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• pp.833-849
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• 1996

The material of choice for functional and esthetic reconstruction of maxillofacial defects is silicone. Silicone has appropriate physical properties for maxillofacial prosthesis but it has weak edge strength. Therefore, a proper combination of silicone and polyurethane sheet is recommended to improve this weakness. Various primers are also used to enhance the adhesive strength between silicone and polyurethane sheet. The purpose of this study was to determine the adhesive strength of silicone and polyurethane sheet. Silicone elastomer mixture was made by admixing MDX4-4210 elastomer (40%) and Silastic Medical Adhesive Type A(60%). This silicone elastomer mixture was attached to polyurethane sheet, using one of three different primers(1205, S-2260, or A-304), treated for 1, 2, 4, 6, and 8 hours. These were then polymerized in room temperature, dry-heat oven or microwave oven. Six specimens per each group, a total of 270 specimens were prepared for final test. The differences of T-peel bonding strengths were then determined by a test. The differences of T-peel bonding strengths were then determined by a test method that was recommended by American Society for Testing and Materials C794-80. The results were statistically analyzed using the ANOVA and Mutiple Range Tests(Tukey' HSD). The reults were as follow. 1. Type of primer, primer reaction time, and methods of polymerization showed significant correlation on the T-peel bonding strengths in adhesiveness between silicone and polyurethane sheet. 2. A-304 primer showed statistically higher in T-peel bonding strength than otehr type of primers except for the polymerization in microwave oven with reaction times of 2, 6 hours(p<0.05). 3. No significant differences in T-peel bonding strength were observed among the polymerization methods. 4. The effect of reaction time by the primer type and polymerization method showed statistically significant differences in bonding strength among different reaction times. And in most cases, reaction time of 1 or 2 hours showed higher T-peel bonding strength.

• 대한화학회지
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• 제47권6호
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• pp.591-596
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• 2003

아미노싸이에노피리다진(1a, b)과 아미노싸이에노쿠마린(2)은 DMFDMA와 축합반응을 하여 아미딘(3a, b)을 형성한다. 이 화합물들을 N-페닐말레이마이드와 반응시키면 화합물 9와 10이 얻어진다. 반면에 3a, b, 4, 18, 19, 20을 말레산 무수물과 반응시키면 포밀 유도체인 5a, b, 6, 21, 22, 23 들이 얻어진다. 아미딘 화합물 3a, b 를 다이에틸 퓨마레이트와 반응시키면 가수분해산물인 아미딘 14를 거쳐 11이 얻어진다. N-페닐말레이마이드를 마이크로웨이브 오븐에서 반응시키면 [2+2]와 [2+2+2] 고리첨가반응 산물이 얻어진다.

• Korean Chemical Engineering Research
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• 제56권2호
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• pp.275-280
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• 2018

Methyl ester derived from coconut oil is very interesting to study since it contains free-fatty acid with chemical structure of medium carbon chain ($C_{12}-C_{14}$), so the methyl ester obtained from its part can be a biodiesel and another partially into biokerosene. The use of heterogeneous catalysts in the production of methyl ester requires severe conditions (high pressure and high temperature), while at low temperature and atmospheric conditions, yield of methyl ester is relatively very low. By using microwave irradiation trans-esterification reaction with heterogeneous catalysts, it is expected to be much faster and can give higher yields. Therefore, we studied the production of methyl ester from coconut oil using CaO catalyst assisted by microwave. Our aim was to find a kinetic model of methyl ester production through a transesterification process from coconut oil assisted by microwave using heterogeneous CaO catalyst. The experimental apparatus consisted of a batch reactor placed in a microwave oven equipped with a condenser, stirrer and temperature controllers. Batch process was conducted at atmospheric pressure with a variation of CaO catalyst concentration (0.5; 1.0; 1.5; 2.0, 2.5%) and microwave power (100, 264 and 400 W). In general, the production process of methyl esters by heterogeneous catalyst will obtain three layers, wherein the first layer is the product of methyl ester, the second layer is glycerol and the third layer is the catalyst. The experimental results show that the yield of methyl ester increases along with the increase of microwave power, catalyst concentration and reaction time. Kinetic model of methyl ester production can be represented by the following equation: $-r_{TG}=1.7{\cdot}10^6{_e}{\frac{-43.86}{RT}}C_{TG}$.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2009년도 춘계학술대회 논문집
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• pp.889-892
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• 2009

A microwave plasma torch at the atmospheric pressure by making use of magnetrons operated at the 2.45 GHz and used in a home microwave oven has been developed. This electrodeless torch can be used to various areas, including industrial, environmental and military applications. Although the microwave plasma torch has many applications, we in the present work focused on the microwave plasma torch operated in pure steam and several applications, which may be used in future and right now. For example, a high-temperature steam microwave plasma torch may have a potential application of the hydrocarbon fuel reforming at one atmospheric pressure. Moreover, the radicals including hydrogen, oxygen and hydroxide molecules are abundantly available in the steam torch, dramatically enhancing the reaction speed. Also, the microwave plasma torch can be used as a high-temperature, large-volume plasma burner by injecting hydrocarbon fuels in gas, liquid, and solid into the plasma flame. Lastly, we briefly report an underway research, which is remediation of soils contaminated with oils, volatile organic compounds, heavy metals, etc.

• 한국표면공학회지
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• 제42권3호
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• pp.139-144
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• 2009

A microwave plasma torch at the atmospheric pressure by making use of magnetrons operated at the 2.45 GHz and used in a home microwave oven has been developed. This electrodeless torch can be used to various areas, including industrial, environmental and military applications. Although the microwave plasma torch has many applications, we in the present work focused on the microwave plasma torch operated in pure steam and several applications, which may be used in future and right now. For example, a high-temperature steam microwave plasma torch may have a potential application of the hydrocarbon fuel reforming at one atmospheric pressure. Moreover, the radicals including hydrogen, oxygen and hydroxide molecules are abundantly available in the steam torch, dramatically enhancing the reaction speed. Also, the microwave plasma torch can be used as a high-temperature, large-volume plasma burner by injecting hydrocarbon fuels in gas, liquid, and solid into the plasma flame. Finally, we briefly report treatment of soils contaminated with oils, volatile organic compounds, heavy metals, etc., which is an underway research in our group.