• 공업화학
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• 제10권2호
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• pp.259-262
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• 1999

금속 규소와 구리 촉매가 함유된 접촉물과 메탄올의 반응에 의한 메톡시실란의 합성에서의 TMOS 반응 생성속도를 산출하였다. 활성 자리 수의 변화에 따른 영향을 제거하기 위해서 유속 전이 기술을 사용하여 주입되는 메탄올의 유속을 반응도중 급격히 변화시켰다. 실험 결과 TMOS 생성속도에 영향을 미치는 인자는 반응에 참여하는 메탄올 농도가 아닌 접촉물질의 사용량임을 확인하였으며, 이를 바탕으로 TMOS 생성 메카니즘에서 접촉 물질의 표면에서 중간생성물이 형성되는 반응 단계가 반응 율속단계라고 추정되었다. 최적 공정조건에서 규소 1 g당 최대 TMOS 생성속도는 $210^{\circ}C$에서 0.030 (g/min)이었으며, 이때의 활성화 에너지는 값은 8.5 kcal/mol, 반응 생성속도 상수의 온도 의존성은 식 $k=4.09{\times}10^4\;exp$ ($-4.73{\times}10^3/T$)로 나타났다.

• 한국식품과학회지
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• 제34권6호
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• pp.1057-1061
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• 2002

초임계 유체 추출법에 의해 감초의 triterpenoid saponin(glycyrrhizin)을 추출하기 위해 50 MPa, $60^{\circ}C$와 3mL/min의 조건에서 보조용매와 soaking의 효과를 알아보았다. 순수한 초임계 이산화탄소만을 이용하여 추출한 결과 감초의 glycyrrhizin은 거의 추출되지 않았다. 99.9% methanol, ethanol과 isopropanol을 보조용매로 초임계 이산화탄소에 첨가하여 추출한 경우, 추출수율의 상승에는 큰 영향을 미치지 아니하였다. 시료를 물로 soaking하여 90% methanol을 보조용매로 사용하여 초임계 이산화탄소에 의해 추출한 경우, soaking 용매의 사용량이 증가할수록 추출수율은 증가하였고, 최고 21.68mg/g(회수율 53.25%)의 수율을 보여주었다. 한편 시료의 soaking 없이 70% methanol을 보조용매로 사용하였을 때는 유기용매추출법에 의한 수율보다 더 높은 수율을 나타내었고, 시료를 물로 soaking하여 70% ethanol을 보조용매로 초임계 이산화탄소에 첨가하여 추출하였을 때, 추출수율과 추출속도는 상승하였고, 시료의 90%(w/w)에 해당하는 물로 시료를 soaking한 경우 70% methanol을 보조용매로 사용하였을 때와 거의 동일한 추출수율을 얻을 수 있었다.

• Nuclear Engineering and Technology
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• 제49권8호
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• pp.1654-1659
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• 2017

The boundary layer of a two-dimensional forced convective flow along a persistent moving horizontal needle in an electrically conducting magnetohydrodynamic dissipative nanofluid was numerically investigated. The energy equation was constructed with Joule heating, viscous dissipation, uneven heat source/sink, and thermal radiation effects. We analyzed the boundary layer behavior of a continuously moving needle in Blasius (moving fluid) and Sakiadis (quiescent fluid) flows. We considered Cu nanoparticles embedded in methanol. The reduced system of governing Partial differential equations (PDEs) was solved by employing the Runge-Kutta-based shooting process. Computational outcomes of the rate of heat transfer and friction factors were tabulated and discussed. Velocity and temperature descriptions were examined with the assistance of graphical illustrations. Increasing the needle size did not have a significant influence on the Blasius flow. The heat transfer rate in the Sakiadis flow was high compared with that in the Blasius flow.

• 한국응용과학기술학회지
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• 제22권2호
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• pp.106-115
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• 2005

Bio-diesel as fatty acid methyl ester was derived from such oils as soybean, peanut and canola oil by lipase catalyzed continuous trans-esterification. So the activation of lipase(Novozym - 435) was kept to be up to 4:1, the limiting molar ratio of methanol to oil under one-step addition of methanol due to the miscibility of oil and methanol through the static mixer for 4hrs and the elimination of glycerol on the surface of lipase by 7wt% silica gel. Therefore the overall yield of fatty acid methyl ester from soybean oil appeared to be 98% at 50$^{\cdot}C$ of reaction temperature under two-steps addition of methanol with 2${\times}$2:1 of methanol to oil molar ratio at an interval of 5.5hrs, 7wt% of lipase, 24 number of mixer elements, 0.2ml/min of flow rate and 7wt% of silica gel.

• Journal of Microbiology
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• 제43권6호
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• pp.499-502
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• 2005

Methylophaga sp. strain SK1 is a new restricted facultative methanol-oxidizing bacterium that was isolated from seawater. The aim of this study was to characterize the electron carriers involved in the methanol oxidation process in Methylophaga sp. strain SK1. The gene encoding cytochrome $c_L$ (mxaG) was cloned and the recombinant gene was expressed in Escherichia coli $DH5\alpha$ under strict anaerobic conditions. The recombinant cytochrome $c_L$ had the same molecular weight and absorption spectra as the wild-type cytochrome $c_L$ both in the reduced and oxidized forms. The electron flow rate from methanol dehydrogenase (MDH) to the recombinant cytochrome $c_L$ was similar to that from MDH to the wild-type cytochrome $c_L$. These results suggest that recombinant cytochrome $c_L$ acts as a physiological primary electron acceptor for MDH.

• 한국응용과학기술학회지
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• 제31권3호
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• pp.446-452
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• 2014

Methanol was directly produced by the partial oxidation of methane with four-component mixed oxide catalysts. Four-component(Mo-Bi-Cr-Si) mixed oxide catalysts were prepared by the co-precipitation and sol-gel methods. The catalyst prepared by the sol-gel method showed about eleven times higher surface area than that prepared by the co-precipitation method. From the $O_2$-TPD experiment of the prepared catalysts, it was proven that there exists two types of oxygen species, and the oxygen species that participates in the partial oxidation reaction is the lattice oxygen desorbing around $750^{\circ}C$. The optimum reaction condition for methanol production was $420^{\circ}C$, 50 bar, flow rate of 115 mL/min, and $CH_4/O_2$ ratio of 10/1.5, providing methane conversion and methanol selectivity of 3.2 and 26.7%, respectively.

• 대한전기학회:학술대회논문집
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• 대한전기학회 1996년도 하계학술대회 논문집 C
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• pp.1409-1411
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• 1996

Direct Methanol Fuel Cell(DMFC) using Pt-Ru electrocatlayst and Nafion menbrane can provide high performance if operating conditions are well designed. In this study, operating temperature, pressure, and fuel flow rate were changed to obtain optimum operating conditions of DHFC single cell. Performance of DMFC were increased by the increase of operating temperature. The concentration of fuel methanol was 2.0M $CH_{3}OH$ and pressure difference of cathode and anode was 2 atm were showed maximum performance of DMFC single cell with showing the current density of 160 $mA/cm^2$ at 0.2V cell voltage.

• 오토저널
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• 제5권3호
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• pp.33-44
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• 1983

This paper deals with the experimental study on the behavior of fuel (methanol) in intake manifold by using the basic apparatus which is manufactured the visible straight tube type model. In this study, the new device for liquid film thickness measurement and vaporization rate measurement are introduced to investigate the variation of liquid film thickness along the intake manifold and to observe the effect of vaporization of injected fuel. the results are summarized as follows: 1) The vaporization rate increases in proportion to decreasing of throttle valve angle and growing air fuel ratio. 2) The liquid film thickness along the intake manifold is mostly independent for the throttle valve angle in low air velocity and then affected in high air velocity, but the distribution of the liquid film thickness on circumferential position almost constant in the region of 300mm down stream from carburetor. 3) The mean liquid film thickness is 0.04 - 0.18mm in case of methanol in the region of air velocity Va = 12m/s - 55m/s and decreases with decreasing the throttle valve angle.

• Journal of Microbiology and Biotechnology
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• 제12권3호
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• pp.476-482
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• 2002

Methanol dehydrogenase (MDH) and c-type cytochromes from marine methanol-oxidizing bacterium, Methylophaga sp. MP, were purified and characterized. The native MDH had a molecular mass of 148 kDa and its isoelectric point was 5.5. Two c-type cytochromes, $c_L\;and\;c_H$, were found, and their isoelectric points were 3.4 and 8.0, respectively. The purified MDH had higher thermal stability than that of the other soil methylotrophic bacteria. The electron flow rate from MDH to cytochrome $c_L$was higher than that from MDH to cytochrome $c_H$, indicating that the physiological primary electron acceptor for MDH is cytochrome $c_L$. The electron transfer from MDH to phenazine ethosulfate (PES, artificial electron acceptor) in the two dye (PES/DCPIP)-linked assay system was not inhibited by NaCl, whereas the electron flow from MDH to cytochrome $c_L$ in the cytochrome/DCPIP-linked assay system was suppressed significantly by NaCl. Metal chelating agents such as EDTA showed the same effects on the MDH activity.

• 멤브레인
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• 제6권3호
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• pp.173-181
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• 1996

실리콘 코팅한 복합막을 이용하여 톨로엔이나 메탄올 같은 휘발성 유기화합물의 제거 및 회수에 관한 연구를 수행하였다. 사용된 막은 코팅층의 두께가 얇고($~1\mu$m), 지지층의 기고율이 커서 투과저항은 적었으며 코팅층과 지지층은 플라즈마 중합에 의해 결합되어 있어서 높은 압력에도 견딜 수 있었다. Feed의 유속은 60cc/min. 이하일 때 사용된 모듈에 위해 휘발성 유기화합물의 제거율은 96~99%이었으며, feed의 농도가 높을수록 제거율은 더 증가하였다. 이 공정은 휘발성 유기화합물의 농도가 높고 유속이 낮은 흐름을 처리하는데 아주 적합함을 알 수 있었다. 사용된 막을 통한 휘발성 유기 화합물들의 투과도는 $4~30 \times 10^{-9}gmol/sec \cdot cm^{2}\cdot cmHg$이었고, 질소의 투과도는 $3~9 \times 10^{-10}gmol/sec \cdot cm^{2} \cdot cmHg$의 범위에 있었다. 휘발성 유기화합물과 질소의 선택도는 유속과 휘발성 유기화합물의 농도에 따라 톨루엔/질소의 경우 10~55, 메탄올/질소의 경우 15~125의 값을 얻었다.