• 한국응용과학기술학회지
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• 제25권3호
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• pp.275-281
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• 2008

The esterification of free fatty acid in Jatropha oil added by propylene glycol using p-TSA catalyst was done, and then the transesterification of Jatropha oil added by 1.0vol% GMS as an emulsifier using TMAH, and mixed catalyst(60wt%-TMAH+ 40wt%-KOH) respectively was followed at $60^{\circ}C$. The esterification conversion at the 1:8 molar ratio of free fatty acid to methanol using 8.0wt% p-TSA was 94.7% within 60min. The overall conversion at the 1:8 molar ratio of Jatropha oil to methanol and $60^{\circ}C$ using mixed catalyst was 95.4%. The kinematic viscosity of Biodiesel using TMAH and mixed catalyst in 24h met the ASTM D-6751 above $30^{\circ}C$, and showed a little more than its criterion.

• 한국응용과학기술학회지
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• 제26권2호
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• pp.179-185
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• 2009

The esterification of the reactants of Jatropha oil and methanol added by propyleneglycol was done using p-TSA catalyst. And then the emulsification of triglyceride and methanol was conduced by 1.0vol% GMS. The emulsified reactants were transesterified at $65^{\circ}C$ using TMAH and mixed catalyst (50wt%-TMAH+50wt%-NaOH) respectively. The esterification conversion at the 1:8 molar ratio of free fatty acid to methanol using 8.0wt% p-TSA was 94.7% within 80min. The overall conversion at the 1:8 molar ratio of mixed fat(50wt% Beef Tallow) to methanol and $65^{\circ}C$ using mixed catalyst was 95.4% The cloud point of Biodiesel decreased with the addition of petroleum diesel.

• Elastomers and Composites
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• 제46권1호
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• pp.37-44
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• 2011

Adipic acid(AA)와 diethylene glycol(DEG) 사이에서 일어나는 반응의 속도에 대한 유기나노점토(Cloisite 30B)의 영향을 규명하기 위하여 383K와 423 K에서 Br${\phi}$nsted acid인 p-toluene sulfonic acid(p-TSA)와 Lewis acid인 butylchlorotin dihydroxide를 촉매로 사용하여 에스테르 반응을 수행하였다. 촉매의 양은 전체반응물의 0.14 mol%만큼 사용하였다. 반응 생성물의 산가로부터 계산된 전환율 vs. 시간의 자료를 사용하여 반응속도를 해석하였다. [OH]/[COOH] 초기 몰비가 2인 상태에서 수행되는 polyester-diol 합성반응의 속도는 p-TSA 촉매하에서는 AA에 대하여 2차 반응으로, butylchlorotin dihydroxide 촉매하에서는 AA에 대하여 1차 반응으로 잘 해석되었으며 두 반응의 활성화 에너지는 각각 42.2 kJ/mol, 63.8 kJ/mol이었다. AA와 DEG에 Cloisite 30B를 5 wt% 첨가시키면 p-TSA 촉매는 활성이 크게 줄어 반응속도가 매우 느려졌으며, 이 때 활성화 에너지는 72.9 kJ/mol로 높게 계산되었다. Butylchlorotin dihydroxide 촉매는 Cloisite 30B의 첨가에 관계없이 거의 일정한 활성을 유지하였다. Butylchlorotin dihydroxide 촉매하에서 Cloisite 30B를 첨가한 반응의 활성화 에너지는 61.8 kJ/mol로 Cloisite 30B를 첨가하지 않은 반응의 활성화 에너지보다 약간 낮았다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2001년도 추계학술발표대회
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• pp.894-897
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• 2001

This experiment was to determine the optimum conditions for D-sorbitol cyclization in the presence of p-toluenesulfonic acid(p-TSA) as acid catalyst before the esterification of sorbitol with fatty acids. The optimum conditions of hydration reaction to obtain maximum yield of 1,4-sorbitan were at $130^{\circ}C$, 200mmHg reduced pressure, after l50min and l%(w/w) p-TSA. In this condition the yield of 1,4-sorbitan was approximately 90%.

• KSBB Journal
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• 제18권3호
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• pp.222-228
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• 2003

당알콜인 D-sorbitol을 화학 촉매 p-toluenesulfonic acid(p-TSA)를 이용하여 탈수반응을 수행하여 고리구조의 1,4-sorbitan을 제조 후 효소적으로 고정화 리파제 Novozym 435를 이용하여 아크릴산과 에스테르화 반응을 수행한 결과 아래와 같은 결론을 얻었다. D-Sorbitol을 p-TSA를 화학촉매로 하여 탈수반응을 통한 고리화 반응의 생성물인 1,4-sorbitan의 최대수율을 얻을 수 있는 최적조건은 1% (w/w)의 p-TSA를 이용하여 200 mmHg의 감압조건에서 13$0^{\circ}C$에서 150분 반응 후 약 90%의 1,4-sorbitan을 얻을 수 있었으며, 부산물과 미반응의 D-sorbitol의 양을 최소화시킬 수 있었다. 화학적 촉매반응의 생성물로 얻은 1,4-sorbitan을 고정화 리파제 (Novozym 435)를 이용하여 반응매질 t-butanol에서 아크릴산과의 에스테르화 반응을 수행한 결과, 5$0^{\circ}C$에서 고정화효소는 최대 활성을 보였으며, 최적 첨가량은 3% (w/v)이었다. 또한 초기농도가 반응의 전환율에 미치는 영향을 조사한 결과 1,4-sorbitan 50 8/L의 초기농도에서 55.8%의 최대 전환율을 얻었으며, 63.5%의 반응수율을 보인 1:3의 몰비가 최적으로 조사되었다.

• 한국응용과학기술학회지
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• 제26권4호
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• pp.394-399
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• 2009

The esterification of palmitic acid in Jatropha Oil using 8wt% p-TSA catalyst was done at the 1:8 molar ratio of oil to methanol and $65^{\circ}C$. The conversion of palmitic acid appeared to be 95.3% in 60min. After that, the continuous transesterification of the oil using 0.5wt% KOH, 0.8wt% TMAH mixed catalyst[40vol% KOH(0.5wt%) + 60vol% TMAH(0.8wt%)] and 1.1wt% TMAH was conducted with the flow rates and the molar ratios at $65^{\circ}C$. The overall conversion of Jatropha Oil increased with the decrease of flow rate and showed 95.6% with 9ml/min of flow rate at the 1:8 molar ratio of oil to methanol and $65^{\circ}C$. But it showed 87% with 15ml/min of flow rate at the same conditions. The recovery of methanol(%) appeared to be 86% at the 1:8 molar ratio of oil to methanol, mixed catalyst and $65^{\circ}C$.

• Macromolecular Research
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• 제10권2호
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• pp.122-126
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• 2002

A molecularly imprinted polymer (MIP) having both amidine and imidazole functional groups in the active site has been prepared using p-nitrophenyl phosphate as a transition state analogue (TSA). The imprinted polymer MIP with amidine and imidazole found to have the highest hydrolysis activity compared with other MIPs with either amidine or imidazole groups only. It is postulated a cooperative effect between amidine and imidazole in the hydrolysis of p-nitrophenyl methyl carbonate (NPMC) as a substrate when both groups were arranged in proximity by molecular imprinting. The rate enhancement of the hydrolysis by MIP was 60 folds over the uncatalyzed solution reaction and two folds compared with the control non-imprinted polymer CPI having both functional groups. The enzyme-mimetic catalytic hydrolysis of p-nitrophenyl acetate by MIP was evaluated in buffer at pH 7.0 with $K_{m}$ of 1.06 mM and $k_{cat}$ of 0.137 $h^{-1}$ . . .

• KSBB Journal
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• 제19권5호
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• pp.385-389
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• 2004

In this research, the chemo-enzymatic synthesis of sorbitan methacrylate was investigated to optimize reaction conditions. Firstly, sorbitan was manufactured by sorbitol cyclic reaction in the presence of p-toluenesulfonic acid (p-TSA) as catalyst material. Secondly, sorbitan methacrylate was synthesized by immobilized lipase Novozyme 435 with acyl donors in t-butanol. As a result of enzymatic synthesis of sorbitan methacrylate, the conversion yield reached about $65\%$ in the condition of initial sorbitan conc. 50 g/L, enzyme content $3\%$ (w/v) , molar ratio 1:3, reaction temperature 50^{circ}C and reaction time 42 hrs using methyl methacrylate as acyl donor. Comparing with acyl donors and reaction temperature, the conversion yield reached about 18, 65 and $80\%$ with methacrylic acid, methyl methacrylate and vinyl methacrylate as acyl donor, respectively. And optimum reaction temperature was 60, 50, and 50^{circ}C, respectively