• Korean Journal of Crystallography
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• v.8 no.2
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• pp.138-143
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• 1997

The crystal structure of isoimperatorin, f-[(3-methyl-2-butenyl)oxy]-7H-furo[3,2-g][1] benzopyran-7-one, has been determined from single crystal x-ray diffraction study; C16H14O4, Monoclinic, P21/c, a=8.865(1) Å, b=9.331(1) Å, c=16.156(1) Å, β=98.12(1)', V=1322.9(2) Å3, T=293(2)K, z=4, Cu Kα(λ=1.5418 Å). The structure was solved by direct method and refined by full-matrix least squares to a final R=5.72% for 1922 unique observed Fo>4o(F0) reflections and 182 parameters.

• Journal of the Korean Ceramic Society
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• v.39 no.5
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• pp.479-483
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• 2002

Silicon dioxide thick film using silica optical waveguide cladding was fabricated by Plasma Enhanced Chemical Vapor Deposition(PECVD) method, at a low temperature ($320^{\circ}$C) and from $(SiH_4+N_2O)$ gas mixtures. The effects of deposition parameters on properties of $SiO_2$ thick films were investigated by variation of $N_2O/SiH_4$ flow ratio and RF power. After the deposition process, the samples were annealed in a furnace at $1150^{\circ}$C, in N2 atmosphere, for 2h. As the $N_2O/SiH_4$ flow ratio increased, deposition rate decreased from 9.4 to 2.9 ${\mu}m/h$. As the RF power increased, deposition rate increased from 4.7 to 6.9 ${\mu}m/h$. The thickness and the refractive index measurements were measured by prism coupler. X-ray Photoelectron Spectroscopy(XPS) and Fourier Transform-infrared Spectroscopy(FT-IR) were used to determine the chemical states. The cross-section of films was observed by Scanning Electron Microscopy(SEM).

• The Transactions of The Korean Institute of Electrical Engineers
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• v.59 no.8
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• pp.1401-1405
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• 2010

We have successfully demonstrated of metal-insulator-semiconductor (MIS) capacitors with $HfO_2$/p-Si structures. The $HfO_2$ film was grown at $200^{\circ}C$ on H-terminated Si wafer by atomic layer deposition (ALD) system. TEMAHf and $H_2O$ were used as the hafnium and oxygen sources. A cycle of the deposition process consisted of 0.1 s of TEMAHf pulse, 10 s of $N_2$ purge, 0.1 s of $H_2O$ pulse, and 60 s of $N_2$ purge. The 5 nm thick $HfO_2$ layer prepared on Si substrate by ALD exhibited excellent electrical properties, including low leakage currents, no mobile charges, and a good interface with Si.

• The Transactions of The Korean Institute of Electrical Engineers
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• v.58 no.12
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• pp.2420-2424
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• 2009

We have successfully demonstrated of metal-insulator-semiconductor (MIS) capacitors with $Al_2O_3/p-Si$ structures. The $Al_2O_3$ film was grown at $200^{\circ}C$ on H-terminated Si wafer by atomic layer deposition (ALD) system. Trimethylaluminum [$Al(CH_3)_3$, TMA] and $H_2O$ were used as the aluminum and oxygen sources. A cycle of the deposition process consisted of 0.1 s of TMA pulse, 10 s of $N_2$ purge, 0.1 s of $H_2O$ pulse, and 60 s of $N_2$ purge. The 5 nm thick $Al_2O_3$ layer prepared on Si substrate by ALD exhibited excellent electrical properties, including low leakage currents, no mobile charges, and a good interface with Si.

• The Journal of Internal Korean Medicine
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• v.21 no.1
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• pp.13-22
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• 2000

목적 : 본(本) 연구(硏究)는 배기음(排氣飮)이 인간(人間)의 장관내(腸管內)에서 산화물(酸化物)에 의해 유발(誘發)된 세포(細胞)의 사망(死亡) 및 DNA의 손상(損傷)을 방지할수 있는지를 검증(檢證)하기 위한 실험(實驗)이다. 방법 : 배양(培養)된 인체장관(人體腸管) 세포계열(細胞系列)인 Caco-2 세포(細胞)에서 세포(細胞)의 사망(死亡)은 trypan bile의 소실정도에 의해서 평가했으며, DNA의 손상(損傷)은 double stranded DNA의 파괴정도를 측정하여 평가하였다. $H_2O_2$는 표본(標本) 산화제(酸化劑)로 사용되었다. 결과 : $H_2O_2$에 노출된 세포들의 세포사망(細胞死亡) 정도는 노출시간과 용량에 비례하여 증가하는 양상을 보였다. 배기음(排氣飮)은 $H_2O_2$에 의해 유발(誘發)되는 세포방지를 방지하였고, 0.05-1%의 농도범위에 걸쳐서는 그 효과가 용량에 비례하여 증가하는 양상을 보였다. $H_2O_2$에 의해 유발(誘發)된 세포손상(細胞損傷)은 catalase(hydrogen peroxide scavenger enzyme)와 deferoxamine(iron chelator)에 의해 억제되었다. 그러나 강력한 항산화제(抗酸化劑)인 DPPD는 $H_2O_2$에 의해 유발(誘發)되는 세포손상(細胞損傷)에는 영향을 주지 못했다. $H_2O_2$에 의해 유발(誘發)된 지질(脂質)의 과산화(過酸化)는 배기음(排氣飮)과 DPPD에 의해 억제되었다. $H_2O_2$에 의해 유발(誘發)된 DNA의 손상(損傷)은 배기음(排氣飮)에 의해 방지되었으며 용량에 의존하는 양상을 보였다. $H_2O_2$에 의해 유발(誘發)된 DNA의 손상은 catalase와 deferoxamine에 의해 억제되었지만 DPPD는 억제시키지 못했다. 배기음(排氣飮)은 $H_2O_2$에 의해 유발(誘發)된 ATP의 소실을 회복시켰다. 이러한 실험결과 $H_2O_2$에 의해 유발(誘發)된 세포(細胞)의 손상(損傷)은 지질(脂質)의 과산화(過酸化)와는 다른 독립적인 기전에 의해 일어남을 나타낸다. 결론 : 이러한 결과들로 볼 때 Caco-2 세포(細胞)에서 배기음(排氣飮)이 항산화작용(亢酸化作用)보다는 다른 기전을 통하여 Caco-2 세포안에서 산화제(酸化劑)에 의해 유발(誘發)된 세포(細胞)의 사망(死亡)와 DNA의 손상(損傷)을 방지할 수 있다는 것을 가리킨다. 따라서 본 연구(硏究)는 배기음(排氣飮)이 반응성산소기(反應性酸素基)에 의해 매개된 인체(人體) 위장관질환(胃腸管疾患)의 치료(治療)에 사용할 수 있을 가능성(可能性)이 있음을 제시하고 있다.

• Clean Technology
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• v.17 no.1
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• pp.41-47
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• 2011

[ $MnO_2$ ]catalysts were prepared by precipitation method using potassium manganate and manganese acetate. The effect of calcination temperatures of $MnO_2$ catalysts for CO oxidation has been studied and their physicochemical properties were studied by X-ray diffraction (XRD), $N_2$ sorption, temperature programmed reduction of $H_2$ ($H_2-TPR$), and temperature programmed desorption of CO (CO-TPD) techniques. $MnO_2$ calcined at $300^{\circ}C$ catalyst has a large surface area $181m^2/g$ having a narrow pore size distribution at 9 nm. The results of XRD and $H_2-TPR$ showed that the catalysts calcined at different temperatures showed mixed oxidation states of Mn such as $Mn^{4+}$ and $Mn^{3+}$. CO-TPD showed that the quantity of $CO_2$ desorbed was decreased with increasing the calcination temperatures. The catalytic activity over the catalyst calcined at $300^{\circ}C$ exhibited the highest conversion reaching to 100% at $200^{\circ}C$. $H_2O$ vapor showed an inhibiting effect on the efficiency of the catalyst because of co-adsorption with CO on the active sites of manganese oxide catalysts and the initial catalytic activity of CO oxidation could be regenerated by removing $H_2O$ vapor in the reactants.

• Journal of Korean Society of Environmental Engineers
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• v.30 no.10
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• pp.999-1005
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• 2008

The main reaction for soil washing with using sodium hydroxide(NaOH) and hydrogen peroxide(H$_2$O$_2$) was desorption and flotation of petrochemical contaminant by means of oxygen bubble. We found the rate of decomposition by rate constant according to various temperature. For the purpose of optimizing the operation factor, we examined the effect of concentration of NaOH and H$_2$O$_2$, washing time, and soil:water ratio. The rate of decomposition for H$_2$O$_2$ in liquid phase is the first order reaction by its concentration. The rate constant of k$_1$ was 0.9439 $\times$ exp(-1376.82/RT) when concentration of NaOH was lower than 0.1 M, and the rate constant of k$_2$ was 17.3588 $\times$ exp(-2320.06/RT) when it was higher than NaOH of 0.1 M. It found that NaOH was facilitated at the beyond of specific concentration. We confirmed the optimum concentration of NaOH/H$_2$O$_2$ by means of rate constants during soil washing. Also, the optimum conditions during soil washing were washing time of 15 min, soil : water ratio of 1 : 3, and NaOH/H$_2$O$_2$ concentration of 0.25 M/0.1 M.

• Korean Journal of Crystallography
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• v.8 no.1
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• pp.1-5
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• 1997

The crystal structure of the title compound consists of discrete 4-N,N-dimethylamino-4'-N'-methyl-stilbazolium, $C_{16}H_{19}N_2$, and tosylate, $C_7H_7SO_3$, dimer. The 4-N,N-dimethylamino-4'-N'-methyl-stilbazolium molecule has a trans conformation at the central C=C double bond: the dihedral angle between the phenyl and the pyridyl rings is $5.7(2)^{\circ}$ and the whole molecule is planar within $0.138(8){\AA}$. Tosylate molecules display hydrogen-bonded dimers with the O-H...O distances of 2.855(9) and $2.899(8){\AA}$, respectively. The shortest intermolecular contact is the distance $3.10(1){\AA}$ between O(3) and C(16).

• Bulletin of the Korean Chemical Society
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• v.23 no.9
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• pp.1263-1307
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• 2002

Pseudo-first-order rate constants (kobs) have been determined for the nucleophilic substitution reactions of p-nitrophenyl diphenyl phosphinate (PNPDPP) with substituted phenoxides (XC6H4O - ) and butane-2,3-dione monoximate (Ox- ) in 0.1 M borate buffer (pH = 10.0) at 25.0 ${\pm}0.1^{\circ}C$. The kobs value increases sharply upon addition of cethyltrimethylammonium bromide (CTAB) to the reaction medium up to near 7 ${\times}$ 10-4 M CTAB and then decreases smoothly upon further addition of CTAB. The rate enhancement upon the addition of CTAB is most significant for the reaction with -O2CC6H4O- and least significant for the one with C6H5O- , indicating that the reactivity of these aryloxides in the presence of CTAB cannot be determined by the basicity alone. The strength of the interaction of these anionic aryloxides with the positively charged micellar aggregates has been suggested to be an important factor to determine the reactivity in the presence of CTAB. The kobs value for the reaction with Ox- increases also upon the addition of CTAB. However, the increase in the kobs value is much more significant for the reaction with Ox- than for the one with ClC6H4O- , indicating that Ox- is less strongly solvated than ClC6H4O- in H2O. The ${\alpha}-effect$ shown by Ox- in H2O has been attributed to the ground-state solvation difference between Ox- and ClC6H4O- .

• Journal of Korean Society of Environmental Engineers
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• v.27 no.4
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• pp.394-401
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• 2005

A nonthermal plasma-assisted fuel reformer was developed and the effects of operating variables on the performance of this reformer were studied. The $H_2$-rich reformed gas from the reformer was injected into a diesel engine under an idle condition and the effects of the amount of injected gas on the NO and soot reduction were investigated. It was found that with increasing electric power consumption, the degree of facility of ignition of the reforming reaction in the reformer could be enhanced. The performance of the reformer including $H_2$ concentration, $H_2$ recovery, and energy conversion was affected only by the O/C mole ratio. This was because the equilibrium reaction temperature was governed by the O/C mole ratio. With increasing O/C mole ratio, the $H_2$ recovery and energy conversion passed through the maximum values of 33.4% and 66%, respectively, at an O/C mole ratio between 1.2 and 1.5. The reason why the $H_2$ recovery and energy conversion increased with increasing O/C mole ratio when the O/C mole ratio was lower than $1.2{\sim}1.5$ appeared to be that the complete oxidation reaction occurred more enough with increasing O/C mole ratio in this low O/C mole ratio range and accordingly the reaction temperature increased. Whereas the reason why the $H_2$ recovery and energy conversion decreased with increasing O/C mole ratio when the O/C mole ratio was higher than $1.2{\sim}1.5$ appeared to be that the complete oxidation reaction was further advanced and the $H_2$ recovery and energy conversion decreased. As the weight ratio of reformed diesel to total diesel which entered the diesel engine was increased to $18.2{\sim}23.5%$, NO and soot reduction efficiencies increased and reached as values high as 68.5% and 23.5%, respectively.