• 대한전기학회:학술대회논문집
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• 대한전기학회 1988년도 전기.전자공학 학술대회 논문집
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• pp.315-318
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• 1988

PHOTO-RESIST 자체문제로인해 감소되는 최소해상력, 촛집심도여유 및 CRITICAL DIMENSION (C.D.) 조정여유도등을 연구하였다. 기존에 사용중인 PHOTO-RESIST(큰 분자량)와 PHOTO-RESIST자체내에 CONTRAST 촉진 물질(CEM)이 첨가된것(INNER CEM TYPE) 및 PHOTO-RESIST구성성분중 작은 분자량/좁은 분자량 산포가 형성된 RESIN 의 PHOTO-RESIST(LOW MOLECULAR WEIGHT CONTROL TYPE)등 세가지 PHOTO-RESIST를 사용 하여 상기의 항목을 분석하였다. INNER CEM TYPE 및 LOW MOLECULAR WEIGHT CONTROL TYPE의 PHOTO-RESIST는 기존에 사용중인 RESIST보다, 최소 RESOLUTION은 약 0.2 - 0.3 um, DEPOCUS MARGIN은 약 0.8 - 1.2 um 및 C.D. CONTROL LATITUDE 향상된 것 등이 우수하였다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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• pp.325-328
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• 2000

The effects of DO and pH on the mass production of pullulan with high-molecular weight from A. pullulans ATCC 42023 were evaluated. The maximum pullulan production yield (51%) was obtained at pH non control (initial pH 6.5) and DO control (above 50%) condition. The pullulan degrading enzyme was activated when the pH of broth reached lower than 5.0 and portion of low molecular weight pullulan was increased. The formation of a black pigment was observed at the initial stationary phase, 40hr of fermentation. Therefore, the fermentation should be carried out in pH non control and DO control condition and harvested before reaching stationary phase around 40h for the production of high molecular weight pullulan.

• 한국염색가공학회지
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• 제30권2호
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• pp.130-140
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• 2018

In the bio-synthesis of poly(3-hydroxybutyrate)(PHB), which is a kind of poly(3-hydroxyalkanoate)(PHA), aimed to control the low molecular weight of PHB and obtain a telechelic PHB. As a result of incubation of R. eutropha at $30^{\circ}C$ with ethylene glycol added as a chain transfer agent, PHB content on the dry cell weight increased up to 24h, however, it decreased after that, and the molecular weight of PHB increased from 9h to 12h, and then, decreased up to 72h. The decrease of the content and the molecular weight of PHB indicates that PHB was decomposed as an energy source in bacterial cells and was incorporated into metabolic pathways. $^1H-NMR$ of the obtained PHB after incubation for 72h was measured to determine the terminal groups of the PHB during incubation. As the results of $^1H-NMR$ measurement, the peaks derived from ethylene glycol in both terminals of PHB were observed. Which indicate that the terminal reaction was caused by the addition of ethylene glycol, and that telechelic PHB having hydroxyl group at the both terminals where molecular weight was controlled was successfully synthesized.

• Macromolecular Research
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• 제13권2호
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• pp.147-151
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• 2005

The main objective of this study was to modulate pH-sensitive polymers (poly($\beta-amino esters$)) by controlling their molecular weight during their synthesis. These pH-sensitive and biodegradable polymers were synthesized by Michael-type step polymerization. 1,4-Butane diol diacrylate was used as the unsaturated carbonyl compound and piperazine as the nucleophilic compound. Various molecular weight polymers were obtained by varying the mol ratio of piperazine/1,4-butane diol diacrylate. The synthesized polymers were characterized by $^{1}H-NMR$ and their molecular weights were measured by gel permeation chromatography(GPC). The dependence of the molecular weight on the mol ratio was evaluated by the titration method. Also, the pH dependent turbidity of the polymers was determined by UV-Vis spectrophotometry. This pH dependent property of the polymers could be very useful for preparing drug carriers that are sensitive to pH.

• KSBB Journal
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• 제13권1호
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• pp.114-118
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• 1998

실크의 피브로인 단백짐의 가수분해에 의한 실크 펠타이드의 제조를 위하여 설크의 가용화 조건이 분자량 분포에 미치는 영 향을 고찰하였다 염 화칼숨, ethylenediamine 및 황산에 의해 가용화된 실크의 평균 분자량은 각각 41600, 3308과 1268 dalton 으로서 염화칼숨을 제외한 나머지 두 가용화 방법에서 평균 분 자량이 수천 dalton인 실크 용액을 얻을 수 있었으며 분산계수 는 3-4의 범위뜰 보였다. 가용화 및 분말화한 후 6시간 동안 단백질 분해효소 처리에 의하여 600-1200 dalton의 중량평균 분 자량을 갖는 살크 접타이드틀 얻을 수 있었다. 24시간 염산에 의한 산분해 처리에 의해 얻은 실크 웹타이드의 평균 분자량은 145 dalton으로 80%의 높은 유리 아미노산 함량을 나타내었다. 여러가지 가용화 방법 및 가수분해 방법 중 낮은 농도의 황산용 액으로 우선 실크를 가용화한 후 중화 및 효소처리에 의해 웹타 이드로 가수분해하는 방법이 과도한 아미노산의 유리를 억제하 면서 분자량의 조절도 용이할 것으로 판단되었다.

• 한국임상수의학회지
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• 제25권4호
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• pp.263-267
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• 2008

This study was performed to compare the efficacy of carboxymethylchitosan fabric (CMCF) with that of the combination of CMCF and low molecular weight heparin (LMWH) for the prevention of postoperative uterine adhesion in rats. Adhesions were induced by suturing both the uterine serosa and peritoneum abrased until petechial bleeding occurred. Fourteen days later, adhesions were evaluated clinically and histopathologically. The mean tensile strength was significantly decreased in the CMCF and CMCF+LMWH groups compared to that of control group, and the CMCF+LMWH group had the lowest tensile strength. The distance of adhesion site was highest in the CMCF group and slightly decreased in the CMCF+LMWH group comparing to that of control group. The inflammatory cell infiltration and neovascularization of the CMCF group were significantly lower than those of the control group. It was observed that the damage at intestinal serosa was significantly decreased in the CMCF+LMWH group comparing to that of control group. Therefore, it was concluded that CMCF and LMWH may be useful to prevent postoperative uterine adhesion in rats.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1993년도 한국자동제어학술회의논문집(국내학술편); Seoul National University, Seoul; 20-22 Oct. 1993
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• pp.766-771
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• 1993

A mathematical model is developed to represent the batch reactor for free radical polymerization of PMMA The model is validated by comparing the simulation result with the experimental data. A computational scheme is proposed to determine the trajectory of the reactor temperature that will produce polymer product having the desired molecular weight distribution. For this instantaneous number average chain length and polydispersity are introduced to calculate the reactor temperature. The former is assumed to be a second order polynomial of the sum of the living and dead polymer concentrations. Various reactor temperature, trajectories are observed depending on the reactor conditions and prescribed molecular weight distributions. Fuzzy and PID control algorithms are applied to trace the reactor temperature trajectory. While the PID control gives rise to an overshoot when the trajectory changes its direction, the fuzzy controller yields a more satisfactory performance because it secures information on the trajectory pattern.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 춘계학술발표대회
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• pp.283-286
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• 2000

A. pullulans ATCC 42023를 사용하여 고분자량의 pullulan을 대량생산하기 위한 연구로써, 용존산소량과 pH가 균체 성장 및 pullulan 생산에 미치는 영향에 대하여 연구하였다. pullulan의 분해 효소에 대한 저항성을 가지고 산업적으로 유용한 고분자량의 pullulan을 생산하기 위해서 pH를 6.5로 조절할 경우, 분자량 20만 이상의 high molecular weight의 productivity가 가장 높았으며 용존산소량의 증가로 pullulan productivity를 증가시킬 수 있었다.

• 한국고분자학회:학술대회논문집
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• 한국고분자학회 2006년도 IUPAC International Symposium on Advanced Polymers for Emerging Technologies
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• pp.159-160
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• 2006

We developed novel catalyst, PHENICS composed of the combination of a cyclopentadienyl group to perform a high catalytic activity and a bulky phenoxy group, which performs the production of high molecular weight polyolefin. The polymerization activity of PHENICS at high temperature is higher than well-known CGC catalyst. PHENICS showed the excellent ability of comonomer incorporation into polymer chain. The obtained copolymer had a high molecular weight. The PHENICS catalyst is also active to the copolymerization of ethylene and several vinyl comonomers such as styrene, norbornen, and conjugated dienes. We will discuss new cocatalysts for PHENICS to improve activity and the ability of molecular weight control.

• Journal of Microbiology and Biotechnology
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• 제12권1호
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• pp.1-7
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• 2002

The effects of DO and pH on the mass production of pullulan with high molecular weight and the morphology of A. pullulans ATCC 42023 were evaluated. A. pullulans showed a maximum production of pullulan (11.98 g/l) when the initial pH of the culture broth was 6.5 in a shake-flask culture. In a batch culture, the mixture of a yeast-like and mycelial cell forms was found at a pH of 4.5, and the maximum production of pullulan (13.31 g/l) was obtained. However, a high proportion of high molecular weight pullulan (M.W.>2,000,000) was produced at a pH of 6.5, with a yeast-like morphology. The maximum pullulan production yield ($51\%$) was obtained at a pH noncontrol (initial pH 6.5) and DO control (above $50\%$) condition. Pullulan degrading enzyme was activated when the pH of the broth was lower than 5.0 and the portion of low molecular weight pullulan was increased. The formation of a black pigment was observed at an initial stationary phase, at 40 h of fermentation. Therefore, the fermentation should be carried out in a pH noncontrol (initial pH of 6.5) and DO control (above $50\%$) condition, and should be harvested before reaching the stationary phase (around 40 h) for the production of high molecular weight pullulan.