• 한국응용과학기술학회지
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• 제15권2호
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• pp.49-57
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• 1998

This study is to develop a new synthetic method for the nitroarenes via non-electrophilic substitution. Direct nitration at the C-1 position of isoquinoline has never been reported and substitution in isoquinoline under the normal nitration condition occurs at C-5 and C-8. We have demonstrated a facile one-step sythetic method for the nitration of isoquinolines at the C-1 position, which involves the electrophilic attack of a $DMSO-Ac_2O$ complex, followed by nucleophilic addition of nitrate ion to this intermediate. Since the reaction is simple and mild, this method has preparative merit since 1-nitroisoquinolines are not readily accessible by other methods. Application to the synthesis of poly nitroarenes from the corresponding anilines was also described.

• Bulletin of the Korean Chemical Society
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• 제33권2호
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• pp.689-691
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• 2012

• 공업화학
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• 제10권7호
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• pp.1092-1095
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• 1999

기존의 혼산 공정으로 방향족 니트로 화합물을 얻는 방법은 묽은 황산이 주성분인 폐산을 처리해야 한다. 폐황산이 발생하지 않는 질산, 이산화질소와 오존을 사용하는 새로운 니트로화 공정을 3 mol 규모로 시험하였다. 디클로로에탄, p-니트로톨루엔 3 mol과 질산 6 mol의 혼합용액에 이산화질소 14.3 mol을 3번에 나누어 투입하고 오존을 0.871 mol/h의 유속으로 주입시키면 5.5시간만에 97% 이상의 전환율을 보였다. 이 방법은 일부 방향족 화합물의 니트로화 반응에서 기존의 혼산 공정을 대체할 수 있을 것이다.

• 공업화학
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• 제9권7호
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• pp.1085-1089
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• 1998

방향족 화합물의 니트로화 반응에 있어서 현재 산업적으로 쓰이는 진한 질산-진한 황산의 혼산 공정은 막대한 양의 폐산 발생으로 인한 폐수 문제와 강산 조건으로 인해 작업 과정에 문제가 많다. 이러한 문제점을 개선하기 위하여 혼산을 사용하지 않고 톨루엔을 니트로화 시키는 연구를 실시하였다. 이산화질소와 오존을 함께 사용하였으며, 산촉매로 진한 질산을 첨가할 경우 반응성이 증대될 뿐만 아니라, 이산화질소의 양으로 니트로화 정도를 조절할 수 있었다. 얼음 중탕에서 6당량의 이산화질소를 톨루엔과 함께 넣고 2당량/시의 유속으로 오존을 불어넣을 경우 2시간 내에 92 mole% 이상까지 디니트로화 반응을 진행시킬 수 있었다. 모노니트로화 반응의 경우 3당량의 진한 질산과 3당량의 이산화질소를 넣고, 1.5당량/시의 유속으로 오존을 불어넣을 경우 30분만에 반응이 완결되었다. 이 방법은 방향족 화합물의 니트로화 반응에서 심각한 환경문제를 야기하는 기존의 혼산 공정을 대체할 수 있을 것으로 기대된다.

• Journal of Microbiology and Biotechnology
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• 제27권2호
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• pp.297-305
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• 2017

The use of peroxidase in the nitration of phenols is gaining interest as compared with traditional chemical reactions. We investigated the kinetic characteristics of phenol nitration catalyzed by horseradish peroxidase (HRP) in an aqueous-organic biphasic system using n-butanol as the organic solvent and ${NO_2}^-$ and $H_2O_2$ as substrates. The reaction rate was mainly controlled by the reaction kinetics in the aqueous phase when appropriate agitation was used to enhance mass transfer in the biphasic system. The initial velocity of the reaction increased with increasing HRP concentration. Additionally, an increase in the substrate concentrations of phenol (0-2 mM in organic phase) or $H_2O_2$ (0-0.1 mM in aqueous phase) enhanced the nitration efficiency catalyzed by HRP. In contrast, high concentrations of organic solvent decreased the kinetic parameter $V_{max}/K_m$. No inhibition of enzyme activity was observed when the concentrations of phenol and $H_2O_2$ were at or below 10 mM and 0.1 mM, respectively. On the basis of the peroxidase catalytic mechanism, a double-substrate ping-pong kinetic model was established. The kinetic parameters were ${K_m}^{H_2O_2}=1.09mM$, ${K_m}^{PhOH}=9.45mM$, and $V_{max}=0.196mM/min$. The proposed model was well fit to the data obtained from additional independent experiments under the suggested optimal synthesis conditions. The kinetic model developed in this paper lays a foundation for further comprehensive study of enzymatic nitration kinetics.

• Bulletin of the Korean Chemical Society
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• 제27권7호
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• pp.1056-1058
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• 2006

• Bulletin of the Korean Chemical Society
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• 제35권4호
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• pp.1241-1243
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• 2014

• 공업화학
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• 제7권3호
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• pp.530-535
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• 1996

니트로클로로벤젠 유도체는 염료, 의약품, 향료 등의 중간체로 쓰인다. 가장 널리 쓰이는 니트로화 반응공정은 질산과 황산의 혼합산을 사용한다. 혼산공정에서는 반응중 생성된 물 때문에 묽은 황산이 주성분인 폐산을 처리해야 한다. 이산화질소와 오존을 함께 사용하여 니트로화 반응을 진행시킬 수 있다. 6당량의 이산화질소, 1.0당량/hr의 오존유속, 반응온도 $0^{\circ}C$에서 클로로벤젠의 모노니트로화 반응은 3시간만에 완결되나, 디니트로화 반응은 12시간 소요된다. 일부 방향족 화합물의 니트로화 공정에서 이 방법은 질산-황산을 사용하지 않으므로 환경문제를 야기한 기존방법을 대체할 수 있을 것이다.

• Bulletin of the Korean Chemical Society
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• 제33권4호
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• pp.1279-1284
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• 2012

Silica supported $Cs_{2.5}H_{0.5}PMo_{12}O_{40}$ catalyst was prepared through sol-gel method with ethyl silicate-40 as silicon resource and characterized by X-ray diffraction, infrared spectroscopy, scanning electron microscopy, nitrogen adsorption-desorption and potentiometric titration methods. The $Cs_{2.5}H_{0.5}PMo_{12}O_{40}$ particles with Keggin-type structure well dispersed on the surface of silica, and the catalyst exhibited high surface area and acidity. The catalytic performance of the catalysts for benzene liquid-phase nitration was examined with 65% nitric acid as nitrating agent, and the effects of various parameters were tested, which including temperature, time and amount of catalyst, reactants ratio, especially the recycle of catalyst was emphasized. Benzene was effectively nitrated to mononitro-benzene with high conversion (95%) in optimized conditions. Most importantly, the supported catalyst was proved has excellent stability in the nitration progress, and there were no any other organic solvent and sulfuric acid were used in the reaction system, so the liquid-phase nitration of benzene that we developed was an eco-friendly and attractive alternative for the commercial technology.

• Tribology and Lubricants
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• 제13권4호
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• pp.33-39
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• 1997

In order to establish a new temperature criterion to prevent the pistons from ring sticking due to deposit formation, bench test and engine test were performed. The effects of oil degradation and temperature on deposit formation was studied by a modified panel coking test. Oil degradation was analyzed by FTIR. Oil oxidation and nitration were selected as a factors to evaluate oil degradation. Bench test results show that oil oxidation is more effective to the deposit formation than oil nitration. And the temperature increase accelerates deposit formation and deposit formation increase rapidly above 26$0^{\circ}C$. Especially, in case of degraded oil, the deposit formation increases so rapidly that ring sticking can occur. The effect of piston temperature on the deposit formation was confirmed by engine test.