Transesterification reaction between dimethyl phthalate and ethylene glycol was kinetically investigated in the presense of various metal nitrate catalysts at 170℃. The reaction rates measured by the amount of distilled methanol from the reaction vessel. The transesterification reaction was carried out under the first order conditions respect to the concentration of dimethyl phthalate and catalyst, respectively. The over all order was 2nd. By Arrhenius plot, the activation energy was calculated as 17.4kcal/mole and 17.2kcal/mole on the transesterification reaction with zinc nitrate and lead nitrate, respectively. Apparent rate constant, k' was appeared linear about concentration of catalyst.

실리콘 산화막을 N2O 분위기에서 RTP로 제조하여 그 성장 기구를 고찰 했다. 산화막과 기판 실리콘 계면 사이에 질소성분이 포함된 oxynitride층이 존재한다. N2O 기체를 이용한 산화막 성장은 삼화제 확산에 의해 성장이 지배되는 포물선 성장론을 따르고 산화제 확산 억제작용은 실리콘 산화막과 실리콘 기판사이에 존재하는 oxynitride막에서 일어난다. 확산이 산화막 성장을 결정하는 구간에서 포물선 성장율 상수 B의 활성화 에너지는 약 1.5 eV이고 산화막 두께 증가에 따라 증가한다.

Single-Si 기판과 poly-Si 기판에 각각 Ti을 sputter한 후 RTA 처리하여 안정한 TiSi2를 형성하였다. 그 위에 Si이 1% 첨가된 Al-1% Si을 600nm sputter한 후 후속 열처리로서 400-600˚C 에서 30분간 N2분위기로 furnace어닐링을 실시하였다. 이렇게 준비된 각 시편에 대하여 면저항 측정, Auger분석, SEM 사진으로 Al-1% Si/TiSi2이중층 구조에서 Ti-silicide의 열적 안정성을 살펴 보았고, EDS 분석과 X-ray 회절 peak 분석을 통하여 Al-1% Si 층과 TiSi2층의 반응으로 생긴 석출물의 성분과 상을 조사하였다. 이로 부터 다음과 같은 결과를 얻었다 Single-Si 기관에서 형성한 TiSi2층은 Al-1% Si 층과 550˚C에서 완전히 반응하여 석출물을 형성하였고, poly-Si 기판에서 형성한 TiSi2층은 Al-1% Si 층과 500˚C에서 완전히 반응하여 석출물을 형성하였는데 전반적으로 기판이 poly-Si인 경우가 반응이 더 잘 일어났고, 석출물의 크기도 비교적 컸다. 이는 poly-Si에 존재하는 grain boundary로 인해 poly-Si에서 형성된 Ti-silicide 층이single-Si 기관에서 형성된 Ti-silicide 층보다 불안정하기 때문으로 생각된다. EDS 분석에 의하여 석출물은 Ti, Al, 그리고 Si로 이루어진 3상 화합물이라고 추정되었고, X-ray회절 분석에 의해 석출물은 Ti, Al, 그리고 Si간의 3상 화합물인 Ti7Al5Si12로 확인되었다.

Effects of caffeine, heparin and caffeine-heparin treatments for in vitro capacitation of Korean Native Cattle sperm on acrosorne reaction and viability were studied using the methods of Wells-Awa and Dual stain. The results were summerized as follows: 1. The acrosome reaction of sperm when treated with caffeine after 0 to 4 hrs of preincubation were 11.0~75.7% for Wells-Awa stain, and 14.3~75.55% for Dual stain. True acrosome reaction of sperm for Dual stain was 3.0~29.2%. The viability of sperm was 62. 2~27.2%. 2. The acrosome reaction of sperm when treated with heparin after 0 to 4 hrs of preincubation were 17.0~81.2% for Wells-Awa, and 14.3~75.5% for Dual Stain. True acrosome reaction of sperm for Dual stain was 1.5~26.6%. The viability of sperm was 58.6~35. 8%. 3. The acrosome reaction of sperm when treated with caffeine-heparin after 0 to 4 hrs of preincubation were 13.0~83.2% for Wells Awa, and 11.0~78.5% for Dual stain. True acrosome reaction of for Dual stain was 5.1~26.3%. The viability of sperm was 60.5~30.1%.

Transesterification reactions (methyl methacrylate with diethanolamine, ethylene glycol with dimethylphthalate) were kinetically investigated in the presence of zinc compound catalysts at 120~170℃ The amount of reactants was measured by gas chromatography. and the reaction rates also measured from the amount of reaction products and reactants upon each catalyst. The transesterification reactions were carried out under the first order conditions respect to the concentration of reactants, respectively, The overall reaction order was 2nd. The apparent rate constant (k') was found to obey first kinetics with respect to the concentration of catalyst. It shows that according to an increase in basicity of anionic species the rate constant increase, and that a linear relationship exists between ln k and pKa in transesterification reaction of methyl methacrylate with diethanolamine.

본 연구에서는 Cu-Cu2O의 공정반응에 의한 구리와 알루미나의 직접접합에 대하여 연구 하였다. 1.5×10-1torr, 1015˚C에서 산화시킨 후 10-3torr, 1075˚C에서 접합시킨 시편의 접합력과 계면특성을 인장시험, SEM, EDS 및 XRD를 통하여 분석하였다. 3분 산화시켜 접합하면 우수한 접합강도를 보이며 산화시간이 이보다 짧거나 길면 결합력은 저하하였다. 과단은 알루미나 공정조직 계면에서 발생하였으며 파단후 Al2O3표면에는 Cu쪽에서 빠져나간 Cu2O nodule의 존재하였는 바 접합력은 Cu2O-Al2O3계면보다는 Cu-Cu2O계면에 좌우됨을 보여주고 있다. 접합력은 접합시간에 따라 완만한 증가를 보였으며 CuAl2O4및 CuAlO2의 반응생성물이 접합중 형성되었다.

Fe2O3, Al2O3, TiO2 및 Si분말을 사용하여 고상반응법으로 써어미스터 소결체를 합성하였다. 합성된 소결체의 조식특성을 SEM으로 조사하고, 액체항온조에서 -50~+50˚C 온도영역에서의 측정 결과 β상수가 972~4005K의 값을 갖는 써어미스터 소결체를 얻었다. 이 소결체는 고공기온측정을 위한 라디오존데용 온도센서로 사용될 수 있다.

Transesterification reactions (methyl methacrylate with monoethanolamine, methyl methacrylate with n-butyl alcohol, dimethylphthalate with ethylene glycol, dimethyl phthalate with monoethanolamine) were kinetically investigated in the presense of various metal acetate catalysts at 110℃. The amount of reactants was measured by gas and liquid chromatography, and the reaction rates also measured from the amount of reaction products and reactants upon each catalyst. The transesterification reactions were carried out under the first order conditions respect to the concentration of reactants, respectively. The overall reaction order was 2nd, Maximum reaction rates were appeared at the range of 1.4 to 1.6 in electronegativity of metal ions and maximum catalytic activities were obserbed at the range of 1.5 to 1,8 in instability constant of metal acetates.

수도 주요 품종들의 재배방식에 따른 도복 양상과 형질의 차이를 구명하기 위해 내도복성품종 IR8과 IR64중간정도의 내도복성을 나타내는 IR36 그리고 도복성품종인 IR 21820-154-3-2-2-3를 공시하여 각 품종간에 도복을 유발시키는 형질간의 비교와 식물체의 구성성분을 조사하였던 바, 결과를 요약하면 다음과 같다. IR8을 제외하고는 공시된 모든 품종은 손이양재배가 산파재배한 것보다 도복저항상이 크게 나타났으며 수량에 있어서도 대체로 손이양재배에서 높게 나타났다. 산파재배에 있어서 도복에 의한 수량손실은 손이앙에 비하여 0.6톤에서 1.5톤으로 품종에 따라 각각 수량이 감소되었다. 그러나 재배방식에 따른 수도의 생육변이와 수량구성요소는 차이를 보이지 않았으며 줄기내의 칼륨함량은 손이앙재배가 산파재배 보다는 높게 나타났는데 이것이 도복의 저항성을 증대 시킨 것으로 사료된다. 한편 인산이나 규산의 함량은 줄기의 강도를 증대시키는데 아무런 영향도 미치지 못하였다.

Aliphatic aldehyde polyoxyethylene glycol acetals were synthesised through the reaction of aliphatic aldehydes such as caproic aldehyde, capryl aldehyde, capric aldehyde and lauric aldehyde with excess diethylene glycol, triethylene glycol and tetraethylene glycol, respectively. The acetal formation, in which water was azeotropically distilled by adding benzene to the reaction system, was gained a good yield of acetal type compounds. This reaction is found pseudo first order reaction at various temperatures such 70, 80, 90 and 97℃. Also these activation energies of reaction of acetal type products such as caproic aldehyde diethylene glycol acetal, capryl aldehyde diethylene glycol acetal, capric aldehyde diethylene glycol acetal, lauric aldehyde diethylene glycol acetal, caproic aldehyde triethylene glycol acetal and caproic aldehyde tetraethylene acetal were 17.3, 19.6, 21.2, 21.6, 15.5 and 14.7 Kcal/mole.

The transesterification reaction between diethanolamine and methyl methacrylate was kinetically investigated in the presence of various metal acetate catalysts at 120℃. The amount of reacted methyl methacrylate was measured by gas chromatography and liquid chromatography, and the reaction rate also measured from the amount of reaction products and reactants under each catalyst. The transesterification reaction was carried out in the first order with respect to the concentration of diethanolamine and methyl methacrylate, respectively. The over-all order is 2nd. The apparent rate constant was found to obey first-order kinetics with respect to the concentration of catalyst. The maximum reaction rate was appeared at the range of 1.4 to 1.6 of electronegativity of metal ions and instability constant of metal acetates.

The transesterification reaction between diethanolamine and methyl-methacrylate was kinetically investigated in the presence of various metal acetate catalysts at 120℃. The quantity of methylmethacrylate reacted in the reaction flask was measured by gas chromatography and liquid chromatography, and the reaction rate was investigated by measuring of the quantity of products and reactnts under various catalysts. The transesterification reaction was carried out in the first order reaction kinetics with respect to the concentration of diethanolamine and methylmethacrylate, respectively. The apparent rate constant was found to obey first-order kinetics with respect to the concentration of catalyst. The linear relationship was shown between apparent rate constant and reciprocal absolute temperature, and by the Arrhenius plot, the activation energy has been calculated as 11.08 Kcal with zinc acetate catalyst, 17.99 Kcal without catalyst. The maximum reaction rate was appeared at the range of 1.4 to 1.6 of electronegativity of metal ions and instability constant of metal acetates.