• Proceedings of the Optical Society of Korea Conference
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• 2005.07a
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• pp.28-29
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• 2005

본 논문에서는 MEH-PPV와 DFPP의 폴리머 물질을 이용하여 photovoltaic device가 제작되었고, 그림 1에 두 물질의 분자 구조가 보여진다. Photovoltaic cell의 전기-광학적 특성은 활성층의 폴리머 물질에 의해 결정된다. 이러한 특성을 알아보기 위해서 홉수 스펙트럼이 측정되었다. DFPP는 chloroform, chlorobenzen, THF, acetone에 잘 녹았으며, 본 논문에서는 chloroform이 용매로 사용되었다. 제작 공정은 다음과 같다. 인듐 주석 산화물 (ITO)이 증착된 유리기판은 photolithography 공정을 거친 후, 왕수(HNO$_{3}$ + HCL)로 식각됨으로서 전극의 패턴이 제작되었다. 그리고 ITO 전극 패턴 된 유리기판 위에 PEDOT (CH8000, Baytron)이 코팅된 후 Ar이 주입되는 Convection Oven을 이용하여 120$^{\circ}$C에서 2시간 동안 열처리되어 수분이 제거되었다. 활성층에는 MEH-PPV와 DFPP가 9:1과 2.33:1로 혼합된 폴리머가 사용되었고, 이것은 0.3 %w.t.가 되도록 chloroform에 넣어 5시간 동안 스핀바를 돌려서 용해되었다. 이 용액은 ITO 전극 패턴이 형성된 글라스 위에 3000 rpm으로 45 초간 스핀코팅 되었다. 이 때 얻어진 유기물 박막층은 80$^{\circ}$C의 Ar이 주입되는 convection oven에서 3시간 동안 경화되었다. 경화된 단층 유기물 박막층 위에 Li-Al이 1000 ${\AA}$의 두께로 증착되어 전극이 형성되었고, 이후 질소가 채워진 globe box에서 소자는 encapsulation되어 산소와 수분에 대한 영향으로부터 차단되었다. 상기의 공정으로 제작된 소자의 박막구조는 그림 2에서 보여진다. 그림 3은 MEH-PPV와 DFPP를 혼합했을 때의 흡수 스펙트럼이다. 최대 흡수 파장은 511 nm였다. 그리고 photovoltaic cell의 V-I 특성 결과가 그림 4와 같이 측정되었다. 측정에서는 300${\sim}$700 nm의 파장대를 갖는 태양광 모사계가 사용되었고, 셀의 면적은 10 mm$^{2}$였다. 그림 5의 I-V 특성으로부터 MEH-PPV와 DFPP가 9:1 로 혼합했을 때보다 2.33:1 로 혼합했을 때, photovoltaic device의 효율이 향상됨을 확인할 수 있다. 빛이 75 mW/cm$^{2}$ 의 세기로 조사될 때 9:1과 2.33:1로 혼합된 소자의 open circuit voltage (V$_{oc}$)는 비슷하지만, short circuit current Density (J$_{sc}$)는 각각 -1.39 ${\mu}$A/cm$^{2}$ 와 -3.72${\mu}$A/cm$^{2}$ 로 약 2.7배 정도 증가되었음을 볼 수 있다. 이러한 결과를 통해 electron acceptor인 DFPP의 비율이 높아질수록 photovoltaic cell의 conversion efficiency가 더 크게 됨을 확인할 수 있다. 그러므로 효율이 최대가 되는 두 폴리머의 혼합 비율이 최적화되는 조건을 찾는 것은 매우 중요한 연구가 될 것이다.

• Korean Journal of Crystallography
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• v.4 no.2
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• pp.74-85
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• 1993

Single crystals of LiNbO3 have found extensive application in electro-optic and nonlinear optic devices. However, laser-induced refartive index inhomogeneities, which have been labeled opical damage impose limits on device optical damage in LiNbO3 is imporved if more than 4.5 rml% MgO is added to the melt The laser damage thrueshold increased as much as 100 times better then that of undoped crystals. The MgO doped cystal has thus been urterlsiv81y studied since then. In the study, Mgo:LiNbOs(MLA) single crystals dopsd with 0, 2.5, 5.0, 7.5, 10.0 mol% MgO have been grown by the czocrualski technique. The metls were prepared in the platinum crluible and 15∼20mm diameter crystals were grown with a length of 20∼30mm in a resitance heater. The growth rate was 2.5mm/hr, the rotation speed 15rpn. Before sawing MLN single crystals were annealed for 24 hours under atmosphere at a temperature of 1080℃. After sawing, we have found an annual ring cross section of MNA crystals only in the direction of perpendicilar to the c-axis. Nonuniform dispusion of MgO was pointed out that the cuties of the state of oxide were strongly affected by oxygen partial pressure in.

• Journal of Ginseng Research
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• v.31 no.3
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• pp.147-153
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• 2007

Effect of puffing treatment on saponins, total sugars, acidic polysaccharide, phenolic compounds, microstructure and pepsin digestibility of dried red ginseng tail root were tested. Puffing samples of dried red ginsneng tail root were pre-pared at 20rpm, 15 $kg/cm^2$, $120{\sim}150^{\circ}C$, and for 30 min by a rotary type apparatus of 5 L capacity. Crude saponin content of puffing red ginseng tail root was increased 26.5% compared to non-puffing, especially $Rg_3$ content was increased from 0.49 mg/g to 0.72 mg/g. Total sugar content was not changed, but acidic polysaccharide content was slightly decreased from 7.15% to 6.44% by puffing treatment. Total phenolic compounds was increased from 7.86% to 9.94% by puffing. In terms of individual phenolic compounds, salicylic acid was quantified in puffing tail root, but gentisic acid was quantified in non-puffing. Syringic acid was the most predominant phenolic acid, increased to about 6 times by puffing treatment. On the other hand, gallic acid, p-coumaric acid, caffeic acid and ferulic acid were highly decreased. Microstructure of cross-section in puffing tail root was shown to more uniform shape compared to non-puffing. Pepsin digestibilities of puffing and non puffing red ginseng tail root were 22.4% and 46.2%, respectively (p<0.05). The results indicated that puffing treatment might be useful increasing the bioactive components, preference and digestibility.

• Proceedings of the Plant Resources Society of Korea Conference
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• 1999.10a
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• pp.46-57
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• 1999

Ginseng(Panax ginseng C.A. Meyer) is important medicinal plant but requires 4-year cultivation for root harvest because of slow growth. In contrast, ginseng callus and hairy roots grow vigorously and may Produce the same or more biologically active compounds for human health than natural ginseng roots. Therefore, ginseng callus and hairy roots can be used for commercial purposes. Polyacetylene, one of anti-cancer compounds in ginseng, was not detected in the callus cultured on the medium containing 2, 4-B, but cells derived from the callus growth was excellent, The ginseng calli cultured on the medium containing 2mg11 CPA and 0.05mg/1 BA was grown vigorously and produced panaxydol, one of ginseng polyacetylene. The biosynthesis of polyacetylene in callus was not affected by addition of NAA and sucrose in media. The SH medium was better than the MS medium for ginseng callus growth and biosynthesis of panaxydol. Another ginseng anti-cancer compounds, ginsenoside-Rg$_3$, Rh$_1$and Rh$_2$ were detected in ginseng hairy roots by heat treatment. Those of Panax ginseng were obtained after root disks of three-year old roots were infected with Agrobacterium rhizogenes Rl000 $A_4$T in dark condition after one month of culture. The optimum growth of hairy roots was achieved in the culture of 1/2 MS liquid medium in dark(22$^{\circ}C$) under 60 rpm gyratory shaking. Hairy roots grew well in 5 ι Erlenmeyer flasks, 1ι roller drums, 10ι jar-fermenters, and especially in 20ι air-lift .culture vessels. All heat treatments had remarkably different ginsenoside contents. Eleven ginsenosides were determined in heat treatment, eight in freeze dried hairy roots. Contents of ginsenoside-Rbl , Rb2, Rc, Rd. Re, Rf, and Rg$_1$tested in all heat treatments were less than those of freeze dried hairy roots. Contents of glnsenoside-Rg$_2$ in heat treatment for 1 hour at 105$^{\circ}C$ was 4.92mg/g dry wt, 3.9 times higher than 1.27 mg/g dry wt of freeze dried hairy roots. The optimum condition of heat treatment for the production of ginsenoside-Rg$_3$and Rhl was 2 hours at 105$^{\circ}C$, and ginsenoside content was 2.58mg/g dry wt and 3.62mg/g dry wt, respectively. The production of ginsenoside-Rh2 was the highest in heat treatment for 2 hours at 105$^{\circ}C$ among treatments examined, and ginsenoside-Rh$_2$content was 1.08mg/g dry wt.

• Journal of Korean Society on Water Environment
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• v.28 no.5
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• pp.729-742
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• 2012

Recently, to using chemical coagulation process for T-P removal in STP effluent as tertiary treatment process is generalized in the country. The importance of analysis technique to save the treatment & maintenance cost during coagulation process is becoming more increased each day. Thus, it is necessary for the analysis technique during coagulation process to be presented well the characteristic of coagulation in field apply. There are a few analysis techniques such as Jar Test, zeta potential analysis and streaming current detecting techniques. But there are difficult to apply in field immediately due to long test time and difficult analysis techniques. And using PDA technique, it is reviewed applicability of the techniques as field index on pilot plant of P-CAP system The P-CAP system is composed of an in-line static mixer, a Flocculation Tank and the CAP reactor with 2 stage weir for effluent. Pre-test is performed to fix the mixing velocity in the Flocculation Tank using the PDA equipment and it fixed with 30RPM. Also, Jar Test is performed to select optimum dose of each coagulant for each T-P concentration level of influent. Result of continuous test on pilot plant of P-CAP system, the FSI in the Flocculation Tank is increased consistently by increasing each dosing concentration of coagulant such as LAS and PAC in the low level influent T-P concentration comparatively. It is considered that formed Al-hydroxide complexes for dosed coagulant are caused FSI variation. Furthermore, it seems that FSI value in the high level influent T-P concentration appeared lower than the opposite influent condition relatively because it is formed simultaneously Al-hydroxide complexes as solid type and Al-phosphorus complexes as soluble type. Thus, relation of FSI by PDA technique and T-P removal of final effluent on pilot plant of P-CAP system are very limited for the kind of coagulant and the characteristics of influent. And it though that FSI value by PDA technique with analyzing of turbidity in Flocculation Tank will be used restrictedly on field as the relative field-index.

• Journal of Life Science
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• v.17 no.1 s.81
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• pp.137-142
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• 2007

For the production of natural pigments with microbe, the strains which produced monascus pigment were isolated, and then culture condition and extraction condition were investigated. These results are summarized as follows; The strain which ran produce monascus natural pigment was isolated from natural microbial sources and we made mutant of this strain with UV($235_{nm}$, 30 second) irradiation. The mutant was identified as Monascus sp. MK2-2. The optimal culture conditions were investigated optimal medium containing 0.3% rice powder, 0.2% yeast extract, 0.3% $NH_4H_2PO_4$ and $30^{\circ}C$ in a rotary shaker (120 rpm) for 5 days (initial pH 5.0), while the pigment production was determined at 24 hr intervals. The effective carbon sources were wheat flour > rice powder > fructose, and effective nitrogen sources were sodium nitrate > $KNO_3$ for production of the monascus natural pigment. The pigment capacity is good from 17 to 22 in C/N ratio. The production amount of monascus natural pigment was 0.38 g per 1 kg of rice. Also, extract of red yeast rice had anti-thrombosis activity like a degree of aspirin.

• Proceedings of the Korean Vacuum Society Conference
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• 2013.02a
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• pp.330-332
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• 2013

소 분위기에서 플라즈마 표면 처리의 경우 기판 표면에 존재하는 수소와 탄소 유기물들이 산소와 반응하여 $H_2O$와 $CO_2$ 등으로 제거되며 표면에 오존 결합을 유도하여 표면 에너지를 증가시키는 것으로 알려져 있다. ZnO 나노구조물을 성장시키는 방법으로는 MOCVD (Metal-Organic Chemical Vapor Deposited), PLD (Pulsed Laser Deposition), VLS (Vapor-Liquid-Solid), Sputtering, 습식화학합성법(Wet Chemical Method) 방법 등이 있다. 그중에서도 습식화학합성법은 쉽게 구성요소를 제어할 수 있고, 저비용 공정과 낮은 온도에서 성장 가능하며 플렉서블 소자에도 적용이 가능하다. 그러므로 본 연구에서는 플라즈마 표면처리에 따라 표면에너지를 변화하여 습식화학합성법으로 성장시킨 ZnO nanorods의 밀도를 제어하고 photolithography 공정 없이 패터닝 가능성을 유 무를 판단하는 연구를 진행하였다. 기판은 Si wafer (100)를 사용하였으며 세척 후 표면에너지 증가를 위한 플라즈마 표면처리를 실시하였다. 분위기 가스는 Ar/$O_2$를 사용하였으며 입력전압 400 W에서 0, 5, 10, 15, 60초 동안 각각 실시하였다. ZnO nanorods의 seed layer를 도포하기 위하여 Zinc acetate dehydrate [Zn $(CH_3COO)_2{\cdot}2H_2O$, 0.03 M]를 ethanol 50 ml에 용해시킨 후 스핀코팅기를 이용하여 850 RPM, 15초로 5회 실시하였으며 $80^{\circ}C$에서 5분간 건조하였다. ZnO rods의 성장은 Zinc nitrate hexahydrate [$Zn(NO_3)_2{\cdot}6H_2O$, 0.025M], HMT [$C6H_{12}N_4$, 0.025M]를 deionized water 250 ml에 용해시켜 hotplate에 올리고 $300^{\circ}C$에서 녹인 후 $200^{\circ}C$에서 3시간 성장시켰다. ZnO nanorods의 성장 공정은(Fig. 1)과 같다. 먼저 플라즈마 처리한 시편의 표면에너지 측정을 위해 접촉각 측정 장치[KRUSS, DSA100]를 이용하였다. 그 결과 0, 5, 10, 15, 60 초로 플라즈마 표면 처리했던 시편이 각각 Fig. l, 2와 같이 $79^{\circ}$, $43^{\circ}$, $11^{\circ}$, $6^{\circ}$, $7.8^{\circ}$로 측정되었으며 이것을 각각 습식화학합성법으로 ZnO nanorods를 성장 시켰을 때 Fig. 3과 같이 밀도 차이를 확인할 수 있었다. 이러한 결과를 바탕으로 기판의 표면에너지를 제어하여 Fig. 4와 같이 나타나며 photolithography 공정없이 ZnO nanorods를 패터닝을 할 수 있었다. 본 연구에서는 플라즈마 표면 처리를 통하여 표면에너지의 변화를 제어함으로써 ZnO nanorods 성장의 밀도 차이를 나타냈었다. 이러한 저비용, 저온 공정으로 $O_2$, CO, $H_2$, $H_2O$와 같은 다양한 화학종에 반응하는 ZnO를 이용한 플렉시블 화학센서에 응용 및 사용될 수 있고, 플렉시블 디스플레이 및 3D 디스플레이 소자에 활용 가능하다.

• Proceedings of the Korean Powder Metallurgy Institute Conference
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• 1994.10b
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• pp.15-15
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• 1994

M MA ODS 합금의 보다 폭넓용 실용확훌 위해 크게 요구되고 있는 적정 접합기술 개발의 한 방안￡로, 마찰압접(Friction Welding) 방법의 가능성옳 조사하기 위하여 마찰압력과 시간, 마 찰 후 접촉압력(Upset Pressure) 풍을 다양하게 변화시켜 접합체톨 제조한 후, 접합체 강도에 대한 인장시험과 접합계연의 결합 및 미세구조에 대한 현미경 관찰, EDS에 의한 원소분석, 접 합이옴부의 경도분포와 파단면 분석 풍율 행하였다. 실험에 사용된 모재는 기계적 합금법으로 제조된 Inca사의 Ni기 MA 754 합금이었으며, 직경 l 10 mm, 길이 50 mm로 가공한 후, 아세통￡로 초음파 세척하여 접합에 사용하였다. 접합온 브 레이크식 마찰압접기틀 사용하여 행하였으며, 회전시험편의 회전수는 2400 rpm이었A며, 다른 한쪽의 고정시험편과의 마찰압력 및 마찰시간온 각각 50 - 500 MPa과 1-5초로, 또한 업셋압 력도 50 - 600 MPa로 변화시켰다. 이때 업셋압력은 모든 시편에 대해 일정하게 6초동안 가하 였다. 얻어진 접합체는 각 압접조건 당 2개 이상의 접합시험편에 대해 상온 인장강도톨 측정하 였으며, 파단이 일어난 위치를 확인한 후 파면에 대한 분석율 주사전자현미경(SEM)과 에너지 분산형 분광분석기mDS)릎 사용하여 행하였다. 컵합이옴부의 첩합성올 확인하기 위하여, 접합 체를 접합변에 수직으로 절단, 연마한 후 광학현미경과 SEM, EDS 퉁으로 관찰, 분석하여 접 합부의 형상과 결합형성 여부, 접합계면의 미세조직 퉁옳 조사하였다. 또한 마찰압접에 따론 모재와 접합계연부의 경도분포훌 접합이옴부로부터 모재쪽으로 일정 간격율 두어 마이크로 비 커스 경도기로 측정, 조사하였다. 이상의 설험 결과, 다옴과 같온 결론옳 얻었다. ( (1) 접합체 강도가 모채 강도의 95% 이상이 되는 양호한 렵합체흩 얻기 위한 마찰압력 조건 온, 2400 rpm의 회전속도와 6초의 업셋압력 유지시간에서 마찰압력과 업셋압력, 그리고 마찰시 간이 각각 400 MPa 이상과 500 MPa 이상,2초입율 확인하였다. ( (2) 컵합이옴부의 관찰 결과, 모든 마찰압접 조건에서 컵합이옴부는, 기폰 모재의 texture 조직 을 유지하고 있는 모재부 영역(영역 ill)과 첩합계면부에 인접하여 업셋압력이 주어질 때 단조 효과에 의해 계연 외부로 metal flow가 일어나면서 형성된 영역 II, 매우 미세한 결정립으로 구성된 중앙부의 영역 1 로 이투어져 있옴융 확인하였다. ( (3) 최적접합조건이 충족되지 않온 경우, 접합부의 영역 I 에서 관찰된 void와 균열, 불균일한 접합계면 통의 접합결함에 Al과 Y. Ti 퉁￡로 구성된 산화물률이 용집되어 있옴을 확인하였 다-( (4) 접합체의 파단 양상온 크게 접합부 파단과 모재부 파단, 이률의 혼합형 파단i로 나눌수 있었다. 모재부 파단의 경우, 파단면이 매끄럽고 파변상의 결정립도 매우 미세하였으며, 산확물 의 용집도 찾아보기 어려웠 나, 접합부 파단의 경우에는 파변의 굴곡이 비교척 심하고 연성 입계파괴의 형태를 보였￡며, 결정립도 모채부 파단의 경우에 비해 조대하였다. 조대하였다.

• Journal of Biomedical Engineering Research
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• v.25 no.1
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• pp.57-64
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• 2004

The non pulsation blood pump is divided into axial flow and centrifugal style according to the direction of inlet and outlet flow. An axial flow blood pump can be made smaller than a centrifugal blood pump because centrifugal pump's rpm is fewer than axial flow pump. Hemolysis is an important factor for the development of an axial flow blood pump. It is difficult to identify the areas where hemolysis occurs. Evaluation of hemolysis both in in-vitro and in-vivo test requires a long-time and more expensive. Computational fluid dynamics(CFD) analysis enables the engineer to predict hemolysis on a computer which just can get not only amount of htmolysis but also location of hemolysis. It takes shorter time and less expensive than in-vitro test. The purpose of this study is to git Computational fluid dynamics in axial flow pump and to verify the accuracy of prediction by the possibility of design comparing CFD results with in-vitro experimental results. Also, wish to figure out the correction method that can bring improvement in shape of axial flow blood pump using CFD analysis.

• Microbiology and Biotechnology Letters
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• v.35 no.3
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• pp.226-230
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• 2007

In order to achieve high-level expression of interferon-${\alpha}1$ (IFN-${\alpha}1$) during fed-batch fermentation of recombinant E. coli, effects of oxygen supply and induction temperature on the expression of recombinant proteins were evaluated. Supplementation of oxygen and its transfer into cells is one of the most important parameters involved in the design and operation of mixing-sparging equipment for bioreactors. Generally, higher oxygen supply stimulates cell growth of aerobic microorganism and consequently the amount of products is increased. In this study, the optimum aeration strategy for the higher production of IFN-${\alpha}1$ during fed-batch fermentation of recombinant E. coli was surveyed. The growth of the cells was also monitored with four different concentrations of dissolved oxygen (DO; limiting, 20%, 35%, 50%) conditions. The DO was controlled by varying aeration rates of air and pure oxygen. Oxygen uptake rate (OUR) and specific oxygen uptake rate (SOUR) were evaluated and compared for the enhanced growth and induction of the cells and IFN-${\alpha}1$, respectively. We confirmed that increased DO by additional oxygen supply, up to 35%, can improve the production of IFN-${\alpha}1$ during the fermentation.