• Proceedings of the Korean Society of Computer Information Conference
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• 2019.01a
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• pp.315-318
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• 2019

본 논문은 화학에서 사용되는 2가지 산, 염기 모델에 대한 이해를 높이고자 각 모델의 핵심 알고리즘가 반영된 단계별 교육용 콘텐츠를 개발하는데 목적이 있다. 이를 위해 먼저 Arrhenius와 Brønsted-Lowry 모델이 갖는 핵심 알고리즘을 탐색하였으며, 이러한 핵심 알고리즘을 반영된 단계별 교육용 콘텐츠를 JAVA를 이용하여 개발하였다. 개발된 교육용 콘텐츠는 총 5단계로 구성되어 있다. 1단계는 화학에서 다루어지는 입자들이 개별적으로 무작위하게 운동함으로 표현하였으며, 2단계는 화학반응이란 이러한 무작위적 운동 중 입자 간 충돌에 의해 반응이 개시됨을 보여주었다. 3단계에서는 단일입자에 대해 정반응과 역반응을 동시에 고려한 진행되는 상황을, 4단계는 여러 입자가 동시다발적으로 정반응과 역반응에 참여한 상황을 구현하였다. 마지막 5단계는 정반응과 역반응의 공존의 비율이 다른 상황을 통해 평형상수의 의미를 고찰하도록 하였다. 창발적 사고의 핵심은 여러 입자를 생각하는 확률적 사고와 이러한 여러 입자가 개별적으로 움직인다는 사고가 반영되어야 한다. 이 연구에서 개발한 교육콘텐츠를 활용한다면 학생들이 보다 창발적 사고를 하는데 도움을 줄 것으로 기대된다.

• The Microorganisms and Industry
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• v.20 no.1
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• pp.23-27
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• 1994

본고에서는 화학적수법으로 다양한 특이한 기질을 제조하여 여기에 입체특이적 성질(stereospecificity)과 입체선택적 성질(steroselectivity)이 높은 생물학적 방법들 중에서 주로 lipase를 이용한 부제가수분해반응(asymmetric hydrolysis)과 그 역반응인 에스테르화반응(esterification)등을 도입한 chiral building block의 제조와 이를 이용한 곤충 생리활성물질인 pheromone의 합성에 대한 최근의 많은 예들중 상품화를 시도하고 있는 매미나방의 pheromne인 (+)-disparlure에 대하여 간단히 소개하고자 한다.

• Journal of Sericultural and Entomological Science
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• v.39 no.1
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• pp.73-78
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• 1997

The crystalline fraction of silk fibroin (Fcp) was obtained from the aqueous solution of silk fibroin hydrolyzed by $\alpha$-chymotrypsin. The molecular weight of Fcp was found approximately 7000 by using high speed GPC. On the other hand, a high molecular weight of PIFcp product could be obtained by the reverse reaction of enzymatic proteolysis of Fcp precipitates. Some parts of this PIFcp have the molecular weights of approximately 17000 and 24000. As a result of x-ray diffraction analysis, the crystal structure of Fcp and PIFcp was turned out silk-II type and silk-I type, respectively. Upon the reverse reaction of enzymatic protelysis, the structural transition occured from silk-II type to silk-I type crystal for the most of Fcp precipitates. It was confirmed that PIFcp might be somewhat stable crystal structure of silk-I type according to the thermal analysis as well as x-ray diffraction method.

• Journal of the Korean Chemical Society
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• v.50 no.3
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• pp.247-255
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• 2006

The purpose of this study was to investigate the correlation between concepts on chemical reaction rates and concepts on chemical equilibrium in high school students. The subjects of the investigation consisted of 120 third grade students attending high school in K city of Kyunggi province. For this study, questionnaire relevant to the subject of chemical reaction rates and chemical equilibrium was developed and the answers were analyzed. As a result of the study, a large percentage of high school students answered questions on reaction rates correctly, but only a small percentage of the students could give explanations. Many high school students answered questions on the rates of forward reactions correctly, but not the questions on the rates of reverse reactions. For the concepts on chemical equilibrium, many high school students gave correct answers when faced with equilibrium questions that only required the understanding of one side of the reaction. But the students could not answer the questions requiring understanding of both forward and reverse reactions as well. Overall, there was a little high correlation between concepts on chemical reaction rates and concepts on chemical equilibrium in high school students. Especially, high school students with little understanding of reverse reaction rates did not understand that chemical equilibrium is a dynamic equilibrium. Also, high school students with little understanding of the collision mechanism regarding chemical reaction rates did not understand the effect of concentration and catalyst factors on chemical equilibrium. And the correlation between concepts on chemical reaction rates and concepts on chemical equilibrium related to concentration and catalyst factors was low. In conclusion, the formation of scientific concepts on chemical reactions rates can decrease misconceptions on chemical equilibrium. Also the teaching-learning method limited to one side of a reaction can cause difficulty in forming the concepts on chemical dynamic equilibrium. Therefore, the development of a teaching-learning method which covers both the forward and reverse reactions can be effective in helping students form the concepts on chemical equilibrium.

• Microbiology and Biotechnology Letters
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• v.20 no.4
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• pp.422-429
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• 1992

The effect of various water-activity depressors, such as pol yo Is, sugars, and polymers, on the conversion yields of the enzymatic synthesis of maltosyl-$\beta$-cyclodextrin from $\beta$-cyc1odextrin and maltose through reverse reaction of pullulanase was investigated. PEG 6000 of concentration of 10% (w/w) was found to be the most acceptable water-activity depressor resulting for increment of conversion yield from 43.0% to 55.9%, corresponding maltosyl-$\beta$-cyc1odextrin concentration of 3.02 g/100 ml H20. Water activity was changed from initial 0.966 to 0.914 upon addition of 20% (w/w) of PEG 6000. The conversion yields were inversely proportional to the water activities, and the increased conversion yield was caused by water activity depression which inhibited the hydrolysis reaction of maltosyl-$\beta$-CD to maltose and $\beta$-cyc1odextrin. The changes of enthalpy ($\Delta$H), entropy ($\Delta$S), and Gibbs free energy ($\Delta$G) were calculated to be 36.788 kJ/mole, 0.067 kJ/mole K. and 14.433 kJ/mole, respectively. The synthesis of maltosyl-$\beta$-CD could be increased substantially by the intermittent feeding of $\beta$-cyclodextrin. PEG 6000 could be separated effectively from reaction mixture using ultrafiltration membrane for reutilization.

• Korean Chemical Engineering Research
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• v.51 no.1
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• pp.58-67
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• 2013

PBT (polybutylene terephthalate) has excellent mechanical properties such as low absorption, dimensional stability, abrasion resistance. It is used in manufacturing electronic components, the automobile part and the various precise parts. Bis (hydroxybutyl) terephthalate (BHBT) which is a PBT monomer, can be produced by transesterification reaction of DMT (dimethyl terephthalate) with 1,4-butandiol (BD). The kinetics of transesterification reaction of DMT with BD using zinc acetate as a catalyst was studied in a batch reactor. Previous kinetic studies was carried out in a semibatch reactor where generated methanol was removed so that reverse reactions were not considered in the kinetic expressions, resulting in inaccuracy of the kinetic model. Mathematical models of a batch reactor for the transesterification reaction were developed and used to characterize the reaction kinetics and the composition distribution of the reaction products. More accurate models than previous models was obtained and found to have a good agreement between model predictions and experimental data.

• Korean Chemical Engineering Research
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• v.51 no.1
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• pp.144-150
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• 2013

The kinetics of the transesterification of dimethyl terephthalate (DMT) with ethylene glycol (EG) was studied in a batch reactor. Bishydroxyethyl terephthalate (BHET), which is poly(ethylene terephthalate) (PET) monomer, can be produced by the transesterification reaction. Zinc acetate was used as a catalyst. Previous kinetic studies was carried out in a semi-batch reactor where generated methanol was removed so that reverse reactions were not considered in the kinetic expressions, resulting in inaccuracy of the kinetic model. Mathematical models of a batch reactor for the tranesterification reaction were developed and used to characterize the reaction kinetics and the composition distribution of the reaction products. More accurate models than previous ones were obtained and found to have a good agreement between model predictions and experimental data. Effect of process variables on the esterification reaction was investigated based on the experimental and simulation results.

• Korean Chemical Engineering Research
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• v.53 no.2
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• pp.253-261
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• 2015

The kinetics of the transesterification of dimethyl terephthalate (DMT) with diethylene glycol (DEG) was studied in a batch reactor. bis-hydroxyethoxytethyl-terephthalate (BHEET), which is polyester polyol monomer, can be produced by the transesterification reaction. Zinc acetate was used as a catalyst. Previous kinetic studies was carried out in a semi-batch reactor where generated methanol was removed so that reverse reactions were not considered in the kinetic expressions, resulting in inaccuracy of the kinetic model. Mathematical models of a batch reactor for the tranesterification reaction, which took the reverse reaction into account, were developed and used to characterize the reaction kinetics and the composition distribution of the reaction products. More accurate models than previous ones were obtained and found to have a good agreement between model predictions and experimental data. Effect of process variables on the esterification reaction was investigated based on the experimental and simulation results.

• Polymer(Korea)
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• v.26 no.4
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• pp.422-430
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• 2002

The kinetics of polycondensation of bishydroxyethyl naphthalate has been studied in the range of 241 -$260^{\circ}C$ using antimony trioxide catalyst. The reaction was performed in a batch reactor and the concentration of reaction mixture was measured with HPLC. The activation energy values of forward and reverse reaction determined from molecular species model were found to be 19.7 and 31.4 kcal/mole, respectively, and the equilibrium constants were in the range of 1.4-2.0, which were larger than that of polycondensation of PET and varied to some degree with temperature. It was confirmed by applying the Flory's distribution function that the reaction rate of the hyroxyethyl group does not depend on the molecular size. By applying functional group model, we observed that there was few difference between the activation energy of the forward reaction and that of reverse reaction, therefore the equilibrium constant has almost constant value of 1.4. The rate constants obtained from functional group model was about 3-4 times larger than that from molecular species model, which showed that both model explains the reaction system well. Although the molecular species model should predict the concentration of as many as ten molecules, it fits for the experimental results well.

• Journal of Energy Engineering
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• v.8 no.1
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• pp.150-158
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• 1999

본 연구는 저온플라즈마를 이용하여 배기가스중의 SOx와 NOx를 동시에 처리하는 공정을 개발하는 것으로서, 최적의 반응제 선정과 효율적인 공정의 구성을 위해 SOx, NOx와 반응제와 반응기구를 밝히고자 하였다. 실험은 1.0 N㎥/h의 모사가스를 이용한 기초실험과 20 N㎥/h의 실제 연소가스를 이용한 실험으로 진행되었으며, 반응제로는 NH3와 파리핀계 및 올레핀계 탄화수소를 사용하였다. NH3를 반응제로 한 SO2 제거반응은 비플라즈마 조건에서는 NH4HSO3, 플라즈마 조건에서는 (NH4)2SO4의 생성반응이었고, 두 조건 모두 높은 제거율을 나타냈다. 반응제를 사용하지 않은 플라즈마 조건에서 SO2는 환원반응이 일어나고 O2 농도의 증가는 역반응을 증가시키는 화학평형에 의해 SO2의 제거율이 감소되었다. 플라즈마 조건에서 NO는 O2농도가 낮은 경우는 NO의 환원반응이 주로 일어나고, O2 농도가 높을 경우는 산화반응이 지배적이었다. 올레핀계 탄화수소는 플라즈마 조건에서 NO 산화 반응에 탁월한 효과를 보였을 뿐만 아니라 SO2 제거에도 효과를 보여 최대 40%의 제거율을 나타냈으며, NH3의 사용을 줄일 수 있음을 확인하였다.