• Journal of the Korean Institute of Gas
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• v.10 no.2 s.31
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• pp.1-6
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• 2006

In this study we proposed on effect of the photodecomcomposition of coated nanofiber by $Pd/TiO_2$ for the removal of formaldehyde gas as indoor air pollutant. The photocatalytic reactor was setup in the inside of rectangular box (volume 2 l), UV lamp and the coating nanofiber with $Pd/TiO_2$. This study investigated the reaction rate and the adsorption constant of Langmuir-Heinshelwood, conversion of formaldehyde gas on temperature ($40^{\circ}C{\sim}80^{\circ}C$), effect of conversion (%) under different concentration, and effect of conversion (%) with humidity level on added $SO_2$ gas. As results, the rate constant (k) and adsorption constant (ft) were 114.94ppmv/min, $0.0036ppmv^{-1}$, respectively. and the conversion (%) of formaldehyde gas on temperature ($40^{\circ}C{\sim}80^{\circ}C$) was decreased to about 24%, compare with the first conversion (%). In conversion effect of increasing humidity levels, the presence of sulfur dioxide further decreased than without sulfur dioxide. the decreasing reason of conversion with presence sulfur dioxide judged as a cause of interference factor on the decrease of contact chance with photocatalysts.

• Clean Technology
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• v.20 no.1
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• pp.7-12
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• 2014

Hydrogenolysis of glycerol to propylene glycol was performed over binary and ternary metal oxide catalysts. The conversion of glycerol and selectivity to propylene glycol were increased on Cu/Zn and Cu/Cr mixed oxides compared to pure CuO and ZnO oxides. The addition of alumina into Cu/Zn mixed oxide very highly increased the conversion of glycerol and selectivity to propylene glycol. The conversion of glycerol was increased with increasing the reaction temperature but the selectivity to propylene glycol was shown to have maximum value at $200^{\circ}C$ and then decreased at $250^{\circ}C$. The conversion of glycerol and selectivity to propylene glycol were decreased with increasing the glycerol concentration.

• Korean Journal of Plant Tissue Culture
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• v.28 no.4
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• pp.221-225
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• 2001

Some factors of wounding methods, solidifying agents, origin of leaf explants, cone. of acetosyring-one, and MES affecting regeneration and transformation by Agrobacterium tumefaciens were investigated to establish an efficient transformation system of apple. Wounding by cutting the leaves merely showed the tendency of regeneration and transformation with higher efficiency compared with that of wounding by non-traumatic forcep when carrying out co-cultivation for three days after bacterial inoculation. While examining the solidifying agents of medium with the combination of agar (A)＋Gelrit $e^{ }$ (G) in g. $L^{-1}$ , the higher concentration of Gelrit $e^{ }$ increased the efficiency of regeneration. However, there was no difference in the efficiency of transformation from the treatments of 2.5 G, 3.5 A+1.2 G, and 7.0 G. The origin of leaf explants showed no difference statistically in the efficiency of regeneration and transformation, but that from the shoots of proliferation medium showed the tendency with higher efficiency. The concentration of above 0.1 mM acetosyringon had an increase in the efficiency of regeneration and transformation and the concentration of 0.15 mM had the highest efficiency of transformation in the treatment of acetosyringone with different concentration. There was no effect of MES on regeneration and transformation.ion.

• Proceedings of the Korean Institute of Information and Commucation Sciences Conference
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• 2007.10a
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• pp.600-603
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• 2007

미래 지식정보사회는 컴퓨터, 통신, 방송 등 모든 정보통신 기기가 하나의 네트워크에 연결되는 BcN 기반의 네트워크사회(Broadband Network Society)로 빠르게 진화할 전망이다. BeN은 엑세스망, IP전달망, 제어/서비스망(교환망 IP전환)의 3개 계층을 모두 포함하는 개념이나 엑세스망, IP전달망은 기존과 통일한 IP방식으로 추진 중이어서 IP기반의 제어/서비스망 신규 구축 및 교환망의 IP로의 전환을 협의의 BcN이라 정의 한다. PSTN에서 BcN망으로 전환 시 BeN망의 구성 요소는 소프트스위치, TGW, AGW, SGW, 응용서버, 미디어서버 등이 있다. PSTN망이 BcN망으로 전환시 크게 3단계의 과정을 거친다. 1단계로 2007년 상반기에 전남 목포지역의 지능망 서비스가 불가한 시외교환기가 BcN으로 전환되었다. 전환 후의 IP망을 경유하는 음성호의 트래픽을 측정한 결과는 발생호는 증가하였으며 완료율은0.06% 감소하였지만 관리 기준내의 양호한 수준이었다. 향후 음성호의 통화 품질을 높이기 위해서 품질 측정을 통한 기준 미달 항목을 조치하고 트래픽 측정을 통한 소통율, 완료율 불량 구간에 대한 지속적인 개선 활동을 해야 한다.

• Korean Journal of Environmental Agriculture
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• v.17 no.3
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• pp.239-245
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• 1998

To investigate the formation of bound residue with soil organic materials by oxidative coupling, nitroaromatics and their reduced metabolites, the insecticide parathion and the herbicide asulam were incubated with oxidoreductase, laccase or horseradish peroxidase, in the presence or absence of humic monomers. Most of aminotoluenes and amino-nitrophenols were completely transformed while most of nitrotoluenes and nitrophenols remained unchanged by a lactase or horseradish peroxidase in the presence or absence of humic monomers. Amino-nitrotoluenes were not transformed without humic monomers, but the addition of various humic monomers caused a considerable difference in the transformation of amino-nitrotoluenes by a lactase or horseradish peroxidase. Amino-nitrotoluenes were most transformed in the presence of catechol, syringaldehyde and protocatechuic acid. The insecticide parathion with nitro group and its metabolite were not mostly transformed in the presence or absence of humic monomers. The herbicide asulam with amino group remained unchanged without humic monomers as well, but the stimulating effect on the transformation of asulam was caused by the addition of catechol, syringaldehyde, protocatechuic acid or caffeic acid with a lactase.

• Proceedings of the KSAR Conference
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• 2001.03a
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• pp.17-17
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• 2001

착상전 수정란 단계에서 형질전환 수정란의 선발은 형질전환동물의 효율을 증대시킬 수 있는 방법이다. 성공적인 형질전환동물의 생산을 위해서는 생산된 수정란의 mosaicism 빈도를 감소시켜 전체 할구에서의 유전자 발현을 유도하는 것이 최적일 것이다. 따라서 본 연구에서는 돼지의 웅성 생식세포를 이용한 형질전환동물의 생산에 있어서 다양한 정자세포 이용시 형질전환 수정란의 생산성 및 mosaicism 빈도를 조사하였다. 아울러 돼지 웅성생식세포내 GFP 유전자도입시 세포들의 생존율 및 원형정자세포분리 후 배양에 따른 형태적 변화를 관찰하였다. 돼지의 웅성 생식세포내 GFP 유전자 도입은 전기자극법 (1.3 ㎸/cm, 200 $\mu\textrm{s}$) 에 의하여 수행되었으며, 이 때 생존율은 60-70%이였다. 유전자가 도입된 전체 세포중 원형정자세포군의 분리는 유식세포분리기에 의하여 수행하였으며, 전체집단에 대한 분리군의 비율은 평균 16.2%이였다. 형질전환 수정란의 생산은 정자 (ICSI), 원형정자세포 (ROSI), 배양후 확장된 원형정자세포(ELSI)를 이용하였으며 각각의 난할율은 ICSI (82.9%), ROSI (59.1%), ELSI (62.1%)로 유의한 차이를 나타내었다. 그리고 8세포기까지의 배발달율은 각각 61.1, 40.9 및 48.6%이였으며, 상실배 및 포배기형성율은 각각 24.6, 18.1 및 32.4%이였다. 형광현미경하에서 GFP 단백질이 발현된 8세포기 수정란을 대상으로 각각의 할구를 primer extension pream-plification (PEP) PCR 방법으로 분석한 결과, ICSI 및 ROSI 실시후 대부분 (15/20, 9/10) 의 수정란은 3~4개의 할구에서만 GFP 유전자의 존재여부를 확인할 수 있었으며, 전체 할구에서 GFP 유전자가 모두 확인된 수정란은 없었다. 반면에 배양된 확장 원형정자세포를 이용하여 생산한 수정란의 경우, 4/10 (40%)에서 전체 할구내에 GFP 유전자의 존재를 확인할 수 있었다. 이러한 결과는 비록 배발달율 및 GFP 유전자 발현율에 있어서는 ELSI방법이 ICSI 등의 방법보다 현저히 낮았지만, mosaicsism 빈도가 낮아 바람직한 형질전환 수정란 생산에서는 오히려 유용한 방법이라고 사료된다. 또한 외래 유전자의 도입효율 면에서 후기 원형정자나 성숙정자보다 초기 원형정자세포에 외래유전자를 도입한 다음, 성숙시킨 확장원형 정자세포를 이용하는 방법이 보다 우수하다는 것을 시사하였다. 따라서 본 연구결과는 포유동물의 웅성 생식세포를 이용하여 nonmosaicisn을 나타내는 형질전환수정란을 생산하고 선발할 수 있는 일련의 기술적 과정을 정립하였다고 사료된다.

• Journal of the Korean Applied Science and Technology
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• v.32 no.2
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• pp.281-289
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• 2015

This study investigated the conversion of oil products from polypropylene by using dispersed Co and Mo catalyst on reaction time and concentration change for knowledging liquefation characteristics at low-temperature (425, 450 and $475^{\circ}C$) pyrolysis in a batch reactor. The reaction time was set in 20~80 minutes and the oil products formed during pyrolysis were classfied into gas, gasoline, kero, diesel and heavy oil according to the domestic specification of petroleum products. The pyrolysis conversion rate was showed as Mo catalyst > Co catalyst > Thermal in all reaction time at reaction temperature $450^{\circ}C$. The conversion rate and yields of the pyrolysis products were the most height when Co and Mo Catalyst ratio was 50:50.

• Applied Chemistry for Engineering
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• v.9 no.6
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• pp.878-883
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• 1998

The methane combustion reaction was conducted over Pb-ZSM-5 catalysts. ZSM-5 synthesized at low temperature and atomospheric pressure was used as a support. The change of methane conversion with $SiO_2/Al_2O_3$ molar ratio was tested. The methane conversions of the synthesized Pb-ZSM-5 catalyst was compared with those of a commercial Pd-ZSM-5(PQ Co.) and $PdO/{\gamma}-Al_2O_3$. The methane conversion increased with the decrease in $SiO_2/Al_2O_3$ molar ratio. The combustion rate of methane also increased with the decrease in $SiO_2/Al_2O_3$ molar ratio. The synthesized Pb-ZSM-5 showed better methane conversion than that of the commercial one. It is found that a crucial factor in methane combustion reaction is oxygen adsorption strength on the catalysts.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.39 no.3
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• pp.261-269
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• 2015

In this study, numerical analysis of curved channel steam-methanol reformer was conducted using the computational fluid dynamics (CFD) commercial code STAR-CCM. A pre-numerical analysis of reference model with a cylindrical channel reactor was performed to validate the combustion model of the CFD commercial code. The result of advance validation was in agreement with reference model over 95%. After completing the validation, a curved channel reactor was designed to determine the effects of shape and length of flow path on methanol conversion efficiency and generation of hydrogen. Numerical analysis of the curved-channel reformer was conducted under various flow rate ($10/15/20{\mu}l/min$). As a result, the characteristics of flow and mass transfer were confirmed in the cylindrical channel and curved channel reactor, and useful information about methanol conversion efficiency and hydrogen generation was obtained for various flow rate.

• Applied Chemistry for Engineering
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• v.25 no.2
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• pp.204-208
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• 2014

This study investigated the effect of hydrogen permeance and selectivity, catalyst amount, $H_2O/CO$ ratio in a feed stream, and Ar sweep gas on the performance of a water gas shift reaction in a membrane reactor. It was observed that a minimum hydrogen selectivity of 100 was needed in a membrane reactor to obtain a hydrogen yield higher than the one at equilibrium and the hydrogen yield enhancement gradually decreased as the hydrogen permeance increased. The CO conversion in a membrane reactor initially increased with the catalyst amount and reached a plateau later for a membrane reactor with a low hydrogen permeance while the high CO conversion independent of a catalyst amount was observed for a membrane reactor with a high hydrogen permeance. For the $H_2O/CO$ ratio in a feed stream higher than 1.5, a hydrogen permeance had little effect on the CO conversion in a membrane reactor and it was found that a minimum Ar molar flow rate of $6.7{\times}10^{-6}mol\;s^{-1}$ was needed to achieve the CO conversion higher than the one at equilibrium in a membrane reactor.