• 한국초전도ㆍ저온공학회논문지
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• 제9권1호
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• pp.18-21
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• 2007

Highly textured MgO template by ion-beam-assisted deposition(IBAD) was successfully fabricated using a continuous reel-to-reel(R2R) mode. To enlarge the deposition area, the previous IBAD system was modified into the system with 14-pass and five heating zone. Every processing step was carried out using this multi-turn IBAD system. The overall process consists of R2R electropolishing of a hastelloy C276 tape, deposition of $Al_2O_3$ diffusion barrier, $Y_2O_3$ seed layer, IBAD-MgO and homoepi-MgO layer. The IBAD-MgO templates were fabricated using the IBAD system with 216 cm-length deposition zone and 32 cm diameter ion source. The texture of MgO films developed during the IBAD process was monitored by in-situ reflection high energy electron diffraction(RHEED) to optimize the IBAD process. Recently, 100 m long IBAD-MgO tape with in-plane texture of $\Delta{\phi}<10^{\circ}$ was successfully fabricated using the modified IBAD system. In this report, the detailed deposition condition of getting a long length IBAD-MgO template with a good epitaxy is described.

• 플랜트 저널
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• 제18권4호
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• pp.58-65
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• 2023

본 연구에서는 난지물재생센터에서 공급되는 바이오가스의 메탄 함량을 높이고 불순물을 정제하기 위해 3단 분리막 정제 공정을 설계하고 설치하여 실증 운전하였다. 2 Nm³/h 정제 공정에서 생산되는 바이오메탄의 메탄농도를 95%, 96.5%, 98%의 3가지 경우로 설정하고 분리막의 막면적비를 1:1, 1:2, 1:1:1, 1:2:1, 1:2:2의 5가지로 변경하여 분리막의 막면적에 대한 최적조건을 도출하였다. 2 Nm³/h의 최적조건을 반영하여 30 Nm³/h 규모의 3단 분리막 공정을 설치하였으며 메탄농도 98% 이상의 바이오메탄 생산을 실증하였다. 2 Nm³/h의 정제장치 운전결과 메탄 설정농도 98%에서 메탄 회수율은 분리막 2단 운전결과 막면적비가 1:1인 경우 95.6%이며 1:2에서 메탄의 회수율은 96.8%로 증가하는 결과를 나타내었고 분리막 3단 운전의 메탄 회수율은 막면적비를 1:2:1로 운전하였을 때 96.8%로 가장 높게 나타났다. 이산화탄소 제거율은 2단공정 막면적비 1:1에서 96.4%이며 1:2에서 95.7%였다. 3단공정에서 막면적비 1:2:1에서 95.4%로 2단공정이 3단공정보다 높은 결과를 보였다. 30 Nm³/h 규모의 바이오가스 정제 실증운전에서 정제 후 메탄농도는 98%이었으며, 메탄의 회수율은 97.1 %, 이산화탄소의 제거율은 95.7%이며 부식의 원인인 황화수소는 검출되지 않았으며 막면적비 1:2:1의 실증운전에서 메탄농도 98%이상의 바이오메탄 생산이 가능했다.

• Nuclear Engineering and Technology
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• 제49권7호
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• pp.1547-1554
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• 2017

VESTA (Verification of Ex-vessel corium STAbilization) and VESTA-S (-small) test facilities were constructed at the Korea Atomic Energy Research Institute in 2010 to perform various corium melt experiments. Since then, several tests have been performed for the verification of an ex-vessel core catcher design for the EU-APR1400. Ablation tests of an impinging $ZrO_2$ melt jet on a sacrificial material were performed to investigate the ablation characteristics. $ZrO_2$ melt in an amount of 65-70 kg was discharged onto a sacrificial material through a well-designed nozzle, after which the ablation depths were measured. Interaction tests between the metallic melt and sacrificial material were performed to investigate the interaction kinetics of the sacrificial material. Two types of melt were used: one is a metallic corium melt with Fe 46%, U 31%, Zr 16%, and Cr 7% (maximum possible content of U and Zr for C-40), and the other is a stainless steel (SUS304) melt. Metallic melt in an amount of 1.5-2.0 kg was delivered onto the sacrificial material, and the ablation depths were measured. Penetration tube failure tests were performed for an APR1400 equipped with 61 in-core instrumentation penetration nozzles and extended tubes at the reactor lower vessel. $ZrO_2$ melt was generated in a melting crucible and delivered down into an interaction crucible where the test specimen is installed. To evaluate the tube ejection mechanism, temperature distributions of the reactor bottom head and in-core instrumentation penetration were measured by a series of thermocouples embedded along the specimen. In addition, lower vessel failure tests for the Fukushima Daiichi nuclear power plant are being performed. As a first step, the configuration of the molten core in the plant was investigated by a melting and solidification experiment. Approximately 5 kg of a mixture, whose composition in terms of weight is $UO_2$ 60%, Zr 10%, $ZrO_2$ 15%, SUS304 14%, and $B_4C$ 1%, was melted in a cold crucible using an induction heating technique.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2009년도 하계학술대회 논문집
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• pp.456-456
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• 2009

Boron doping on an n-type Si wafer is requisite process for IBC (Interdigitated Back Contact) solar cells. Fiber laser annealing is one of boron doping methods. For the boron doping, uniformly coated or deposited film is highly required. Plasma enhanced chemical vapor deposition (PECVD) method provides a uniform dopant film or layer which can facilitate doping. Because amorphous silicon layer absorption range for the wavelength of fiber laser does not match well for the direct annealing. In this study, to enhance thermal affection on the existing p-a-Si:H layer, a ${\mu}c$-Si:H intrinsic layer was deposited on the p-a-Si:H layer additionally by PECVD. To improve heat transfer rate to the amorphous silicon layer, and as heating both sides and protecting boron eliminating from the amorphous silicon layer. For p-a-Si:H layer with the ratio of $SiH_4$ : $B_2H_6$ : $H_2$ = 30 : 30 : 120, at $200^{\circ}C$, 50 W, 0.2 Torr for 30 minutes, and for ${\mu}c$-Si:H intrinsic layer, $SiH_4$ : $H_2$ = 10 : 300, at $200^{\circ}C$, 30 W, 0.5 Torr for 60 minutes, 2 cm $\times$ 2 cm size wafers were used. In consequence of comparing the results of lifetime measurement and sheet resistance relation, the laser condition set of 20 ~ 27 % of power, 150 ~ 160 kHz, 20 ~ 50 mm/s of marking speed, and $10\;{\sim}\;50 {\mu}m$ spacing with continuous wave mode of scanner lens showed the correlation between lifetime and sheet resistance as $100\;{\Omega}/sq$ and $11.8\;{\mu}s$ vs. $17\;{\Omega}/sq$ and $8.2\;{\mu}s$. Comparing to the singly deposited p-a-Si:H layer case, the additional ${\mu}c$-Si:H layer for doping resulted in no trade-offs, but showed slight improvement of both lifetime and sheet resistance, however sheet resistance might be confined by the additional intrinsic layer. This might come from the ineffective crystallization of amorphous silicon layer. For the additional layer case, lifetime and sheet resistance were measured as $84.8\;{\Omega}/sq$ and $11.09\;{\mu}s$ vs. $79.8\;{\Omega}/sq$ and $11.93\;{\mu}s$. The co-existence of $n^+$layeronthesamesurfaceandeliminating the laser damage should be taken into account for an IBC solar cell structure. Heavily doped uniform boron layer by fiber laser brings not only basic and essential conditions for the beginning step of IBC solar cell fabrication processes, but also the controllable doping concentration and depth that can be established according to the deposition conditions of layers.

• 한국수산과학회지
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• 제30권4호
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• pp.556-561
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• 1997

해수로부터 분리한 V. cholerae non-O1 FM-3 이 생산하는 hemolysin의 특성에 관하여 연구한 결과를 요약하면 다음과 같다. 1. V. cholerae non-O1 FM-3이 생산하는 hemolysin은 대수증식기일 때 가장 높은 활성을 나타내었으며, Sephadex G-100 gel column chromatography로 부분정제한 후 hemolysin의 특성을 실험한 결과, pH 7.0, $4^{\circ}C$에서 가장 안정하였으며, $60^{\circ}C$, 30분 가열에 의해 완전히 실활되었다. 2. 적혈구와 hemolysin이 반응할 때, $Na^+,\;K^+$과 같은 1가 양이온을 첨가하면 약간의 활성증가를 보였으며, $Ca^{2+},\;Mg^{2+},\;Mn^{2+}$과 같은 2가 양이온을 첨가하였을 때 급격한 활성증가를 보였고, 반면 $Zn^{2+}$ 첨가시에는 급격히 활성이 저하되었다. 3. 적혈구 현탁액과 hemolysin을 각각 다른 온도대에서 반응시킨 결과, $4^{\circ}C$에서도 온도와 관계없이 적혈구막과 hemolysin의 결합이 가능한 온도 비의존적인 제1단계와, 용혈황성의 최적온도대인 $37^{\circ}C$에서만 용혈작용이 일어나는 온도 의존적인 제2단계로 나누어졌다.

• 식물병연구
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• 제21권4호
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• pp.315-320
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• 2015

Soybean mosaic virus(SMV)는 potyvirus 속에 속하며, 모자이크, 괴사, 기형 등의 병징을 야기하고 국내에서는 11개 계통(G1 to G7, G5H, G6H, G7H, G7a)이 보고되어있다. Reverse transcription loop-mediated isothermal amplification(RT-LAMP) 방법은 등온에서 유전자 증폭이 가능하게 하며, 이 방법은 PCR 과정이나 전기영동 없이도 바이러스에 감염된 식물을 검출할 수 있는 이점이 있다. RT-LAMP의 최적반응 조건은 $58^{\circ}C$, 60분으로 확인되었다. 특이성 검정을 위해 콩에서 발생하는 여러 바이러스들과 보유중인 SMV의 9 계통에서 그 특이성을 확인하였다. 그 결과 SMV에 대한 RT-LAMP primer들의 종 특이성이 확인되었으며, SMV의 계통들에 대해서도 적용이 가능한 것으로 확인되었다. 항온수조와 heating block과 같은 간편한 등온 장치에서 재현성을 확인하기 위해 Thermocycler 기기와 비교하여 증폭 여부를 확인한 결과 반응의 차이는 나타나지 않았다. RTLAMP 반응 이후, 반응물을 전기영동과 SYBR Green I을 이용하여 자연광과 UV광에서 증폭 여부를 확인하였다. 그 결과 전기 영동, 자연광, portable UV light와 UV transilluminator에서 모두 반응이 확인되었다.

• 대한화학회지
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• 제4권1호
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• pp.18-26
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• 1957

There are two problems to be solved by our efforts in the enamel frit. One is how we can cover the enamel frit thin with complete milk white as possible, and the other is how it can be, made resistant for chemicals than before one. The frit which can solved the two problems just mentioned above is titanium enamel frit. This frit has been developed in America after War Ⅱ, and now the research for concerning antimony frit into titanium frit is under development entirely. In order to develope the enamel industry in Korea, it is urgent problem to convert antimony frit into titanium frit. By the way the titanium frit is emulsified titanium oxide crystal which made through reheating the supersaturated solution of titanium oxide in the basis of glass. Unfortunately, there are many obscure points in active fact or which influence on its composition and characteristics yet. However, this task was tried for the first in Korea. As first step, the test was carried on the reference books, and we can be possible convert antimony frit into titanium frit as a result of this experiment. As a conclusion, for the purpose of developing the enamel industry in Korea, we studied that the research for converting antimony enamel frit which has been used popularly into titanium enamel frit which is more economic and resistant for chemicals. As a result of experiments, the following points concerning with titanium frit have become clearly. 1. It is better when the composition of titanium enamel frit has as following table.Man Duck San Silica 24 An Yang Feldspar 20 Borax 28 Sodium Nitrate 4 Cryolite 7 Calcium Carbonate 3.6∼1 Titanium Oxide 10 Calcium phosphate 0 ∼3.2 Calcium Fluoride 0∼1.8 Antimony Oxide 0∼0.5 2. The amount of $TiO_2$, to be added is $10%\;to\;12{%,\;CaF_2\;is\;under\;1.8%,\;P_2O_5\;is\;under\;1.6%,\;Sb_2O_3\;is\;under\;0.5%$. 3. In the titanium frit, the limit of iron oxide amount to be included is under 0. 5%. 4. Comparing the titanium enamel frit with antimony enamel frit not only the titanium frit can be savely 20.6% in the price of raw materials, but one time of glazing and heating process is omitted in each case, and it is known the titanium frit is more resistant for chemicals than antimony frit.

• 대한화학회지
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• 제4권1호
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• pp.15-17
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• 1957

1. Preparation of Titanium tetrachloride; The following precesses were strictly followed as the preliminary step to obtain pure $TiOCl_2$, titanyl chloride; First, pure Titanium Oxide mixed with carbon is rolled into pills. After drying up perfectly, these pills are heated at 900∼1000${\circ}C$. And then the pills are subjected to the flow of $Cl_2$ gas in a quartz tube heated to 900-1000${\circ}C$. Thus Titanium tetrachloride is obtained. 2. Preparation of $TiOCl_2$ ; Yellowish trobrown solution is made by pouring 80 g of conc. HCl (sp.gr. 1.19) to 45 gr of Titanium tetrachloride (approx. 2 times of theoretical amount). Then this solution is kept settled for 5-days in a desiccator filled with phosphorous pentoxide at room temperature. As the colorless amorphous solid thus obtained is washed with aceton, 36.5 g of the pure salt are obtained. 3. Determination of composition. The analysis of the sample taken from the deposit desiccated gives the following data; (A) Qualitative analysis; a) $Ti(OH)_4$ is precipitated by adding NaOH in water solution of the salt. b) Adding $AgNO_3$ solution, the water solution of the salt gives white precipitate of AgCl. c) When acid and $H_2O_2$ are added, the solution turns its color to redish brown (This proves that $TiO^{++}$ was converted into $TiO^{++}$ by oxidation of $H_2O_2$. (B) Quantitative analysis; a) $Ti(OH)_4$ precipitated by $10{\%}$ NaOH isalitatsubjected consecutively to the filtration and ignition in porcelain crucible at approx. 1000${\circ}C$. , then $TiO_2$ thus formed is weighed and calculated into Ti content. b) Chlorine involved in water solution of the salt is determined by Vorhardt method. Result: The values obtained from previous analysis, devied by their atomic weight gives the following composition: Ti : Cl = 1 : 2 Therefore $TiOCl_2$ should be given as its molecular formula. 4. Summary. When $TiCl_4$ is additated into conc. HCl, $TiO^{++}$ formed exists as a stable form, and forms $TiOCl_2$. However $TiOCl_2$ is unstable to heating. When the temperature is raised to $65{\circ}C$the decomposition of the solution is accelerated, and gives $TiO_2$ aq. $TiOCl_2$ in addition is highly hygroscopic.

• 공업화학
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• 제31권4호
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• pp.443-451
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• 2020

본 연구에서는, 축분 고형연료의 연료적 가치를 판단하기 위해 물리화학적 특성과 열분해 동역학 분석을 수행하였다. 원소분석과 공업분석결과는 축분 고형연료는 휘발성 물질(64.94%), 탄소(44.35%) 및 수소(5.54%)의 함량이 높았다. 축분 고형연료의 저위발열량(3,880 kcal/kg) 또한 가축분뇨 고형 연료 기준(3,000 kcal/kg)보다 높았다. 열중량분석결과 축분연료는 3개의 분해온도구간을 가졌다. 첫 번째 온도구간(130~330 ℃)은 추출물의 기화, 헤미셀룰로우스 및 셀룰로우스의 분해로 구성되었다. 두 번째(330~480 ℃)와 세 번째(550~800 ℃) 온도 구간들은 리그닌의 분해와 carbonaceous materials 분해에 의한 것이었다. Friedman, FWO, KAS 같은 model free 분석방법에 의해 구해진 축분 고형연료의 열분해에 대한 활성화 에너지 값은 전환율 0.1에서 0.9 범위에서 173.98에서 525.79 kJ/mol로 나타났다. 특히, 전환율이 0.6보다 높은 구간에서 활성화에너지가 크게 증가하였다. Curve fitting 방법을 사용한 동역한 분석은 축분 고형연료가 5단계의 분해 단계로 구분될 수 있는 다단계 반응에 의해 분해됨을 제안하였다.

• 자원리싸이클링
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• 제16권4호
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• pp.3-9
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• 2007

고열 및 파절단에 의하여 폭발위험이 있는 폐리튬일차전지를 재활용하기 위해서는 폐리튬일차전지의 안정적 해체공정이 필수적이다. 본 연구에서는 폐리튬일차전지의 안정적 해체를 위한 최적 방전공정 조건을 연구하였다. $0.5kmol{\cdot}m^{-3}$ 황산용액을 이용하여 안정화를 진행한 결과, $35^{\circ}C$에는 4일째에 그리고 $50^{\circ}C$에는 1일째에 안정적 파쇄가 가능하였으며, 높은 반응온도에서 보다 빠른 안정화 결과를 얻을 수 있었다. 황산만을 사용하여 안정화를 진행할 경우, 재활용 가능한 폐리튬일차전지 금속의 손실이 크기 때문에 황산과 증류수를 이용하여 2단으로 안정화하는 공정을 제안하였으며, $0.5kmol{\cdot}m^{-3}$ 황산으로 6시간 안정화시킨 후, 증류수로 24시간 안정화한 결과, 폐리튬일차전지는 안정적으로 파쇄되었으며 금속의 손실도 적어 향후 재활용공정의 경제성 향상이 가능하다고 판단되었다.