• Archives of Pharmacal Research
• /
• 제8권4호
• /
• pp.191-195
• /
• 1985

The polymerization of title compound (MCEC, I) with phenols led to give corresponding resole type polymer. Phenol and p-methoxyphenol polymer had a relative higher molecular weight and a property of elastomer, but p-chloro-and p-nitrophenol polymer had a lower ones. Also, phenol and p-meth-oxyphenol gave to crosslinking polymer by elongation of reaction period and rising of temperature.

• 공업화학
• /
• 제2권3호
• /
• pp.199-208
• /
• 1991

양이온 중합은 electron이 풍부한 단량체들을 중합하는데 널리 이용되나 많은 부 반응과 빠른 중합속도 때문에 반응을 제어하기가 어렵다. 최근에 이러한 반응 제어에 많은 연구가 되고 있는데 특히 living 중합에 의하여 중합반응을 제어하는 방법에 대한 연구가 활발하다. 본고에서는 종합활성점의 해리상태를 조절하여 중합반응을 제어하고 living 중합을 도모하는 방법에 대하여 기술하였다. 그리고 현재까지 알려진 여러 방법들을 이러한 기본원리하에서 설명하였다.

• Macromolecular Research
• /
• 제8권4호
• /
• pp.147-152
• /
• 2000

The activity of periodic acid as an initiator for the polymerization of acrylamide in aqueous medium was investigated. The rate of polymerization was found to be proportional to the monomer concentration to the 1.5th power in the range of 1.41-5.64 mol/L. The reaction order to the periodic acid concentration was 0.49, which indicated a bimolecular mechanism for the termination reaction in the range of 0.5-4.0$\times$10$\^$-2/ mol/L. Propagation rate increased with raising the temperature according to an Arrhenius expression resulting in the exhibition of an apparent activation energy of 87.8 kJ/mol in the temperature range of 60-80$\^{C}$. The addition of hydroquinone as a radical scavenger stopped the polymerization of acrylamide initiated by periodic acid. These results support that the polymerization proceeds via a radical chain mechanism .

• Macromolecular Research
• /
• 제8권6호
• /
• pp.247-252
• /
• 2000

Suspension polymerizations of styrene were conducted in the aqueous phase with tricalcium phosphate (TCP) as a stabilizer and $\alpha$, $\alpha$'-azobis(isobutyronitrile) (AIBN) as an initiator. Various amounts of initiator and stabilizer were selected and the reaction was carried out at a selected temperature between 60 to 80 $\^{C}$. It was found that the combination of 5 wt% stabilizer and 2.427$\times$10$\^$-3/ mol/L of costabilizer is the minimum amount for suspension polymerization reaction to produce particles in the aqueous phase. Particles were found to be polydisperse in diameter, regardless of reaction conditions. Class transitions were observed to be around 95$\^{C}$, nearly independent of reaction temperature and initiator. Homogenizer was found to be essential in forming particles in the proximity of tens of micrometers in diameter in suspension polymerization with TCP as stabilizer.

• Macromolecular Research
• /
• 제14권4호
• /
• pp.466-472
• /
• 2006

The kinetic behavior of emulsion polymerizations of styrene in the presence of sulfonated N-hydroxy ethyl aniline (SHEA) was investigated with two initiators: 2,2'-azobisisobutyronitrile (AIBN) and potassium persulfate (KPS). SHEA was synthesized using a stepwise polyurethane reaction method from 3-hydroxy-1-propane sulfonic acid sodium salt, isophorone diisocyanate (IPDI), and N-(2-hydroxyethyl) aniline. Stable core-shell poly(styrene/sulfonated N-hydroxy ethyl aniline, St/SHEA) latex particles were successfully prepared by using an appropriate amount of AIBN, in which SHEA plays the role of 'surfmer', i.e., acting as both a surfactant in the emulsion polymerization and a monomer in the chemical oxidative polymerization. The kinetic behavior was dissimilar to that of typical emulsion polymerization systems. A long inhibition period and low rate of polymerization were observed due to radical loss by the oxidative polymerization of SHEA. It was concluded, due to the low water-solubility of AIBN and retardation reaction by SHEA, that the initial loci of polymerization were monomer droplets. However, growing polymer particles as polymerization loci became predominant as polymerization proceeded. It was suggested that AIBN was more effective than KPS in the preparation of the core-shell type poly(St/SHEA) latex particles. With KPS, no substantial polymerization was observed in any of the samples.

• 한국안전학회지
• /
• 제25권3호
• /
• pp.61-65
• /
• 2010

Most of the chemical reactions performed in the chemical industry are exothermic, meaning that thermal energy is released during the reaction. It is also important to understand the thermal hazards such as thermal stabilities and runaway reactions, which are governed by thermodynamics and reaction kinetics of the mixed materials. The paper was described the evaluation of thermal behavior caused by an exothermic batch process in manufacture of the vinyl acetate resin. The aim of the study was to evaluate the thermal stabilities of raw materials with operating conditions such as a reaction inhibitor, heating rate, reaction atmosphere and the mount of methanol charged in the vinyl acetate polymerization process. The experiments were performed in the differential scanning calorimeter(DSC), C 80 calorimeter, and thermal screening unit($TS^u$). It was suggested that we should provide the thermal characteristics for raw materials to present safe precautions with operating conditions in the vinyl acetate polymerization process.

• 한국세라믹학회지
• /
• 제36권2호
• /
• pp.151-158
• /
• 1999

유기단분자인 $\varepsilon$-Caprolactame을 montmorillonite의 층사이에 삽입하여 증합반응시켜 고분자화해 줌으로써 무기고분자와 유기고분자를 화학결합에 의해 연결시켜 주었다. X-선 및 IR-분석결과 층내에서의 $\varepsilon$-Caprolactame의 고분자반응이 성공적으로 이루어졌음이 입증되었다. 고분자 반응생성물을 좀 더 자세히 분석조사하기 위해 고분자 물질을 층사이로부터 격리시켜 X-선회절분석 및 IR 분석한 결과와 montmorillonite없이 $\varepsilon$-Caprolactame만 고분자화시켜 얻은 순수고분자에 대한 동일한 분석 결과를 비교해 본 결과 서로 동일한 화합물임이 입증되었다.

• 한국세라믹학회지
• /
• 제42권4호
• /
• pp.224-231
• /
• 2005

The polymerization of $\varepsilon-caprolactone$ in the layers of the [DEACOOH]-Montmorillonite intercalations complex was attempted using 10-Carboxy-n-decyldimethylethylammonium bromide and Na-Montmorillonite to achieve [DEACOOH]-Polycaprolactone-Montmorillonite in which the inorganic material (montmorillonite) and the organic material (polycaprolactone) are chemically linked each other. The results of X-ray- and IR-analysis for the samples obtained after polymerization showed that the polymerization reaction has been successfully accomplished. In order to study the polymeric reaction products more precisely we have separated the polymerized product from the silicate layers and analyzed it with X-ray diffractometer, IR-spectrometer and TEM. The comparison of the results of X-ray- and IR-analysis for the separated polymer with them for the polymer which was synthesized by the reaction of $\varepsilon-caprolactone$ only with the organic cation without montmorillonite showed that the obtained both polymers are the same compounds.

• Bulletin of the Korean Chemical Society
• /
• 제20권6호
• /
• pp.663-666
• /
• 1999

The 4-methylene-1,3-dioxolane(4-MDO) derivatives with dimethoxyphenyl group on the 2-position of 1,3-dioxolane ring, 2-(x,y-dimethoxyphenyl)-4-MDO derivatives (x,y=2,3(1b), 2,4(2b), 2,5(3b) and 3,4(4b)) were prepared by acelalizationof the corresponding benzaldehyde with 3-chloro-1,2-propanediol, followed by dehydrochlorination. 2-(Dimethoxy)phenyl-4-MDO derivatives underwent polymerization wiht ring opening as will as cyclization reaction to afford a mixture of the ring-opened polymer and 3(2H)-dihydrofuranone derivative with boron trifluoride as a cationic catalyst. Both the methylene group and 1,3-dioxolane ring were participated in the reaction with cationic catalyst. The key intermediate of the polymerization is a benzyl cation generated by ring opening, and the cyclization reaction proceed via proton addition to oxygen atom of 1,3-dioxolane ring.

• Journal of Microbiology and Biotechnology
• /
• 제5권3호
• /
• pp.177-180
• /
• 1995

In horseradish peroxidase-catalyzing polymerization of phenol under the water/dioxane solvent system, the optimal concentration of hydrogen peroxide was found to be 10 mmol/I. Feeding of hydrogen peroxide at its optimal concentration improved the polymerization performance by reducing reaction time and increasing molecular weights. Monomer conversions and the molecular weights of the enzymatically produced polymer were in the ranges of 83.1~94.2$%$ and 58000~68000, respectively.