• 공업화학
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• 제31권6호
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• pp.630-634
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• 2020

We developed a processing recipe to synthesize flexible polyurethane foam with a pore size of 335 ± 107 ㎛. The gelling reaction time was varied from 0 to 30 minutes and the physical properties of the foam were evaluated. The gelling reaction where the polypropylene glycol and tolylene 2,4-diisocyanate (TDI) were reacted to form urethane prepolymer, proceeded until a chemical blowing agent, deionized water, was introduced. Fourier transform infrared (FT-IR) spectra showed that the composition of the foam did not change but the foam height reached a peak value when the gelling reaction time was 10 minutes. We found that increasing the gelling time lessened the coalescence and helped the formation of cells. Lastly, the repeatability of polyurethane foam was confirmed by one-way analysis of variance (ANOVA) by synthesizing ten identical polyurethane foams under the same experimental conditions, including the gelling reaction time. Overall, the new time parameter in-between the gelling and blowing reactions will give extra stability in manufacturing identical polyurethane foams and can be applied to various polyurethane foam processes.

• 한국환경과학회지
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• 제10권6호
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• pp.401-405
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• 2001

For the purpose of developing a new process f3r the elimination of oil components from oily waste water, experimental researches using oil gelling agent were performed. The process is composed of three units, that is, decantator, gelling column and adsorption column. 10g of gelling agent in the gelling column could effectively absorb 15.65g of oil from ship washing waste water and 16.93g of oil from steel industry waste water. COD in waste waters dramatically diminished not in the gelling column but in the adsorption column. The .gelling is hindered by other organic components in waste water, and the optimum space time f3r the gelling column Is 20min. 1g of gelling agent absorbed 3.7-4.0g of oil from waste waters with 25 min in the batch operation.

• 한국세라믹학회지
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• 제31권2호
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• pp.194-200
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• 1994

Pitchstone(Volcanic ejecta) reacts with CaO in hot water and increases its sedimentary volume by forming Ca(OH)2 and calcium silicate hydrates. ALC was prepared from the various gelling and curing conditions using the ratio of pitchstone/CaO was 2(CaO/SiO2 mol ratio=0.81), and then the products, crystalline phases and physical properties of ALC with experimental conditions was investigated. The crystalline phase of tobermorite with laths and plate type and the porosity were increased, the thermal conductivity was decreased with increasing gelling temperature and time. But modulus of rupture has maximum value when gelling time was 2 hrs. Othwrwise the bulk density nearly unchanged with increasing curing temperature, but the modulus of rupture was increased.

• 한국축산식품학회지
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• 제38권1호
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• pp.14-25
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• 2018

Chemical compositions, trypsin inhibitory activity, and gelling properties of albumen from duck egg during salting of 30 days were studied. As the salting time increased, moisture content decreased, the salt content and surface hydrophobicity increased (p<0.05). Trypsin inhibitory activity and specific activity were continuously decreased throughout the salting time of 30 days (p<0.05). This coincided with the decrease in band intensity of inhibitor with molecular weight of 44 kDa as examined by inhibitory activity staining. Nevertheless, no differences in protein patterns were observed in albumen during the salting of 30 days. Based on texture profile analysis, hardness, springiness, gumminess, chewiness, and resilience of albumen gel decreased with increasing salting time. Conversely, salted albumen gels exhibited higher cohesiveness and adhesiveness, compared to those of fresh albumen. Scanning electron microscopic study revealed that gel of salted albumen showed the larger voids and less compactness. In general, salting lowered trypsin inhibitory activity and gelling property of albumen from duck egg to some extent. Nevertheless, the salted albumen with the remaining inhibitor could be an alternative additive for surimi or other meat products to prevent proteolysis.

• Archives of Pharmacal Research
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• 제19권4호
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• pp.280-285
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• 1996

The sustained release dosage form which delivers melatonin (MT) in a circadian fashion over 8 h is of clinical value for those who have disordered circadian rhythms because of its short halflife. The purpose of this study was to evaluate the gelling properties and release characteristics of alginate beads varying multivalent cationic species $(Al^{+++}, \; Ba^{++}, \; Ca^{++}, \; Mg^{++}, \; Fe^{+++}, \; Zn^{++})$. The surface morphologies of Ca- and Ba-alginate beads were also studied using scanning electron microscope (SEM). MT, an indole amide pineal hormone was used as a model drug. The $Ca^{++}, \; Ba^{++}, \; Zn^{++}, \; Al^{++}\; and\; Fe^{+++}\; ions\; except\; Mg^{++}$ induced gelling of sodium alginate. The strength of multivalent cationic alginate beads was as follows: $Al^{+++}\llFe^{+++} the induced hydrogel beads were very fragile and less spherical. Fe-alginate beads were also fragile but stronger compared to Al-alginate beads. Ba-alginate beads had a similar gelling strength but was less spherical when compared to Ca-alginate beads. Zn-alginate beads were weaker than Ca- and Ba-alginate beads. Very crude and rough crystals of Ba- and Ca-alginate beads at higher magnifications were observed. However, the type and shape of rough crystals of Ba- and Ca-alginate beads were quite different. No significant differences in release profiles from MT-loaded multivalent cationic alginate beads were observed in the gastric fluid. Most drugs were continuously released upto 80% for 5 h, mainly governed by the passive diffusion without swelling and disintegrating the alginate beads. In the intestinal fluid, there was a significant difference iq the release profiles of MT-loaded multivalent cationic alginate beads. The release rate of Ca-alginate beads was faster when compared to other multivalent cationic alginate beads and was completed for 3 h. Ba-alginate beads had a very long lag time (7 h) and then rapidly released thereafter. MT was continuously released from Feand Zn-alginate beads with initial burstout release. It is assumed that the different release rofiles of multivalent cationic alginate beads resulted from forces of swelling and disintegration of alginate beads in addition to passive diffusion, depending on types of multivalent ions, gelling strength and drug solubility. It was estimated that 0.2M $CaCl_2$ concentration was optimal in terms of trapping efficiency of MT and gelling strength of Ca-alginate beads. In the gastric fluid, Ca-alginate beads gelled at 0.2 M $CaCl_2$ concentration had higher bead strength, resulting in the most retarded release when compared to other concentrations. In the intestinal fluid, the decreased release of Ca-alginate beads prepared at 0.2 M $CaCl_2$ concentration was also observed. However, release profiles of Ca-alginate beads were quite similar regardless of $CaCl_2$ concentration. Either too low or high $CaCl_2$ concentrations may not be useful for gelling and curing of alginate beads. Optimal $CaCl_2$ concentrations must be decided in terms of trapping efficiency and release and profiles of drug followed by curing time and gelling strength of alginate beads.

• 문화기술의 융합
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• 제4권4호
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• pp.167-171
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• 2018

알스트로메리아는 경제적으로 중요한 절화 작물 중 하나이다. 그러나 낮은 증식률과 번식기간이 길고 바이러스 질병 감염이 높기 때문에 대량증식이 어렵다고 알려져 있다. 따라서 기내 조직배양을 이용한 대량증식 시스템 쳬계 확립이 필요하다. 본 연구에서는 BA와 NAA 그리고 여러 가지 배지 고형제를 이용하여 알스트로메리아 최적의 생장 효율을 찾기 위하여 실험을 진행하였다. 먼저 BA 1.0 mg/L 와 NAA 0.1 mg/L를 첨가한 배지에서 무처리구에 비하여 신초 및 뿌리의 개수가 약 1.5배 증가하였고 비대한 신초와 뿌리를 나타내었다. 여러 가지 배지 고형제들 중 gelrite 0.25%를 첨가한 배지에서 타 처리구에 비해 최대 50% 향상된 길이를 나타내었고, 근경 개수 및 생체중 증가량에 있어서도 가장 높은 효율을 나타내었다. 본 연구결과를 토대로 알스트로메리아 신품종 개발 및 대량증식 시스템 체계 확립에 도움을 줄 것으로 기대된다.

• 대한토목학회논문집
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• 제2권4호
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• pp.1-9
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• 1982

밀도(密度)가 다른 동일시료토(同-試料土)에 시멘트계(系), 물유리계(系) 및 아크릴아미드계(系) 등의 약액(藥液)을 침투주입(浸透注入)시켜 고결토(固結土)에 대한 토질성상변화(土賢性狀變化)를 구명(究明)한 것이다. 더욱, 매우 잘 다져진 지반(地盤) 그리고 유수중(流水中)에서의 주입효과(注入効果)를 검토(檢討)하기 위하여 1액(液) 1계류식(系流式)과 2액(液) 1계류식(系流式)의 특수주입장치(特殊注入裝置)를 설계제작(設計製作)하여 침투주입(浸透注入)을 시도(試圖)하였다. 고결토(固結土)의 전단강도(剪斷强度) 및 차수효과(遮水効果)의 증대(增大)는 주로 점착력(粘着力)에 의한 것으로서 느슨한 상태의 경우는 박막점착력(薄膜粘着力)에 의해서, 조밀한 경우는 구조성점착력(構造性粘着力)에 의해서 증대(增大)된다. 유수중(流水中)에서의 주입효과(注入効果)는 매우 저하(低下)하여 유속(流速) 및 gel time의 변화(變化)에 따라 45~80%의 유효고결률(有効固結率)이 얻어졌으며, 더욱 주입재(注入材)의 입도(粒度)는 침투성(浸透性) 및 이동거리(移動距離)에는 크게 영향(影響)을 미치나 유효고결률(有効固結率)에는 별다른 영향(影響)이 없다는 사실을 알 수 있었다. 관입저항분포도(貫入低抗分布圖)와 등강도곡선(等强度曲線)에 의해 다짐정도(程度)가 매우 큰 지반(地盤)에 대한 고결범위(固結範圍), 고결강도(固結强度) 및 약액침투상황(藥液浸透狀況) 등의 주입효과(注入効果)를 합리적(合理的)으로 판정(判定)할 수 있었다.

• 폴리머
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• 제39권2호
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• pp.210-218
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• 2015

본 연구에서는 아민계 젤화 촉매 dimethylcyclohexyl amine(DMCHA)과 칼륨계 젤화 촉매 potassium octoate(PO)가 경질 폴리우레탄 발포체의 반응거동에 미치는 영향에 대해 연구하였다. Polymeric 4,4'-diphenyl methane diisocyanate, 폴리에스터 폴리올, 실리콘 유화제, 발포제 그리고 젤화 촉매를 사용하여 경질 폴리우레탄 발포체를 제조하였다. DMCHA 촉매의 함량이 0에서 2.0 g으로 증가함에 따라 반응 시간이 약 330초에서 약 35초로 감소하였고, 발열 반응으로 최대 반응온도는 약 217에서 약 $234^{\circ}C$로 증가하였다. PO 촉매의 함량이 0에서 2.5 g으로 증가할수록 반응 시간은 약 79초에서 약 38초로 감소함을 보였고, 특히 젤 타임, 택 프리 타임의 단축에 기여하였으며, 최대 반응온도가 약 182에서 약 $271^{\circ}C$로 증가하였다. 단열 온도 상승법을 이용하여 전환율을 구하였고, 반응식의 상수들을 계산하였다. 반응속도상수 $k_0$는 DMCHA 촉매의 양이 증가할수록 큰 값을 갖는 것을 확인하였고, PO 촉매의 경우 촉매량 증가와 큰 관계없이 유사한 값을 나타냈다.

• 공업화학
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• 제16권3호
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• pp.379-384
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• 2005

Polymeric 4,4'-diphenylmethane diisocyanate (PMDI), 여러 관능기와 OH 값을 가지는 7종의 폴리올, 실리콘 계면활성제, 두 종류의 촉매 그리고 세 종류의 발포제를 사용하여 폴리우레탄폼(PUF)을 제조하였다. 발포제로는 염화불화탄소(CFC-11), 염화불화탄화수소(HCFC-141b)와 불화탄화수소(HFC-365mfc)가 이용되었다. HCFC-141b를 사용한 PUF의 기초특성과 cell 구조에 대한 겔화촉매와 blowing 촉매의 영향을 조사하였다. Cell 크기는 촉매의 양에 따라 감소하였다. 겔화촉매의 경우에 밀도 변화는 거의 없지만 압축강도는 촉매양이 0에서 2 pph로 증가함에 따라 11.9에서 $12.66kg_f/cm^2$로 증가하였다. 3 종의 발포제를 이용한 PUF의 겔화시간, 밀도와 압축강도를 측정하였으며, 물리적 특성에 있어서는 큰 차이를 나타내지 않았다. 그러나 다른 두 종류의 발포계와 비교했을 때 HCFC-141b를 사용한 PUF의 cell 구조는 불균일함을 알 수 있었다.

• 한국세라믹학회지
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• 제21권2호
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• pp.127-134
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• 1984

Basic research on the formation of monolithic glasses from metal alkoxide has been done concerning gelling of silicon alkoxides and dehydration of those gells. The felling time were increased with increasing of Carbon number of alkyl radical of alkoxide and am-ount of water and the lower pH value of water. Large portions of water and organic materials were rem-oved below 25$0^{\circ}C$ and shrinkage of glass took place above 80$0^{\circ}C$ Therefore heating up to 25$0^{\circ}C$ and above 75$0^{\circ}C$ must be done gradually with rate of 0.5$^{\circ}C$/min.