• 대한기계학회논문집B
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• 제36권4호
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• pp.405-412
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• 2012

MCFC 발전시스템에서 연소기는 연료극의 배가스 중에 포함된 미반응 가스를 연료로 사용하여 공기극에 $H_2O$와 $CO_2$ 농도가 높은 고온의 혼합가스를 공급하는 역할을 한다. 하지만 이러한 배가스는 가연한계 이하로 내려가게 되어 통상적인 연소방식에 의한 완전연소가 어렵기 때문에 이를 해결하기 위하여 촉매연소기를 사용한다. 완전연소 및 이에 다른 공해물질의 저감 특성에 따라 최근 촉매연소는 환경친화적인 연소방식으로 주목받고 있다. 따라서 본 연구에서는 MCFC 발전시스템의 BOP 시스템에 적용되는 촉매연소기에 대한 실험연구를 수행하였다. 본문에서는 실험장치를 설명한 후 촉매연소 시스템의 설계변수, 즉, $H_2$ 연료 첨가에 따른 연료조성, 유입가스의 온도, 과잉 공기비, 촉매의 종류, 그리고 시동 스케줄에 따른 촉매연소 특성을 고찰하였다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2010년도 추계학술대회 초록집
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• pp.131.1-131.1
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• 2010

This study was conducted for engineering optimization for the gasification process which is the key factor for success of Taean IGCC gasification plant which has been driven forward under the government support in order to expand to supply new and renewable energy and diminish the burden of the responsibility for the reduction of the green house gas emission. The gasification process consists of coal milling and drying, pressurization and feeding, gasification, quenching and HP syngas cooling, slag removal system, dry flyash removal system, wet scrubbing system, and primary water treatment system. The configuration optimization is essential for the high efficiency and the cost saving. For this purpose, it was designed to have syngas cooler to recover the sensible heat as much as possible from the hot syngas produced from the gasifier which is the dry-feeding and entrained bed slagging type and also applied with the oxygen combustion and the first stage cylindrical upward gas flow. The pressure condition inside of the gasifier is around 40~45Mpg and the temperature condition is up to $1500{\sim}1700^{\circ}C$. It was designed for about 70% out of fly ash to be drained out throughout the quenching water in the bottom part of the gasifier as a type of molten slag flowing down on the membrane wall and finally become a byproduct over the slag removal system. The flyash removal system to capture solid particulates is applied with HPHT ceramic candle filter to stand up against the high pressure and temperature. When it comes to the residual tiny particles after the flyash removal system, wet scurbbing system is applied to finally clean up the solids. The washed-up syngas through the wet scrubber will keep around $130{\sim}135^{\circ}C$, 40~42Mpg and 250 ppmv of hydrochloric acid(HCl) and hydrofluoric acid(HF) at maximum and it is turned over to the gas treatment system for removing toxic gases out of the syngas to comply with the conditions requested from the gas turbine. The result of this study will be utilized to the detailed engineering, procurement and manufacturing of equipments, and construction for the Taean IGCC plant and furthermore it is the baseline technology applicable for the poly-generation such as coal gasification(SNG) and liquefaction(CTL) to reinforce national energy security and create new business models.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2009년도 하계학술대회 논문집
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• pp.113-114
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• 2009

Silicon carbide is one of the most attractive and promising wide band-gap semiconductor material with excellent physical properties and huge potential for electronic applications. Up to now, the most successful method for growth of large SiC crystals with high quality is the physical vapor transport (PVT) method [1, 2]. Since further reduction of defect densities in larger crystal are needed for the true implementation of SiC devices, many researchers are focusing to improve the quality of SiC single crystal through the process modifications for SiC bulk growth or new material implementations [3, 4]. It is well known that for getting high quality SiC crystal, source materials with high purity must be used in PVT method. Among various source materials in PVT method, a SiC powder is considered to take an important role because it would influence on crystal quality of SiC crystal as well as optimum temperature of single crystal growth, the growth rate and doping characteristics. In reality, the effect of powder on SiC crystal could definitely exhibit the complicated correlation. Therefore, the present research was focused to investigate the quality difference of SiC crystal grown by conventional PVT method with using various SiC powders. As shown in Fig. 1, we used three SiC powders with different particles size. The 6H-SiC crystals were grown by conventional PVT process and the SiC seeds and the high purity SiC source materials are placed on opposite side in a sealed graphite crucible which is surrounded by graphite insulation[5, 6]. The bulk SiC crystal was grown at $2300^{\circ}C$ of the growth temperature and 50mbar of an argon pressure. The axial thermal gradient across the SiC crystal during the growth is estimated in the range of $15\sim20^{\circ}C/cm$. The chemical etch in molten KOH maintained at $450^{\circ}C$ for 10 min was used for defect observation with a polarizing microscope in Nomarski mode. Electrical properties of bulk SiC materials were measured by Hall effect using van der Pauw geometry and a UV/VIS spectrophotometer. Fig. 2 shows optical photographs of SiC crystal ingot grown by PVT method and Table 1 shows electrical properties of SiC crystals. The electrical properties as well as crystal quality of SiC crystals were systematically investigated.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1991년도 한국자동제어학술회의논문집(국제학술편); KOEX, Seoul; 22-24 Oct. 1991
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• pp.1639-1645
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• 1991

Because of the important role LD converters play in the production of high quality steel, various dynamic models have been attempted in the past by many researchers not only to understand the complex chemical reactions that take place in the converter process but also to assist the converter operation itself using computers. And yet no single dynamic model was found to be completely satisfactory because of the complexity involved with the process. The process indeed involves dynamic energy and mass balances at high temperatures accompanied by complex chemical reactions and transport phenomena in the molten state. In the present study, a mathematical model describing the dynamic behavior of LD converter process has been developed. The dynamic model describes the time behavior of the temperature and the concentrations of chemical species in the hot metal bath and slag. The analysis was greatly facilitated by dividing the entire process into three zones according to the physical boundaries and reaction mechanisms. These three zones were hot metal (zone 1), slag (zone 2) and emulsion (zone 3) zones. The removal rate of Si, C, Mn and P and the rate of Fe oxidation in the hot metal bath, and the change of composition in the slag were obtained as functions of time, operating conditions and kinetic parameters. The temperature behavior in the metal bath and the slag was also obtained by considering the heat transfer between the mixing and the slag zones and the heat generated from chemical reactions involving oxygen blowing. To identify the unknown parameters in the equations and simulate the dynamic model, Hooke and Jeeves parttern search and Runge-Kutta integration algorithm were used. By testing and fitting the model with the data obtained from the operation of POSCO #2 steelmaking plant, the dynamic model was able to predict the characteristics of the main components in the LD converter. It was possible to predict the optimum CO gas recovery by computer simulation

• 대한치과보철학회지
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• 제38권5호
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• pp.595-605
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• 2000

Dental ceramics have good aesthetics, biocompatibility, low thermal conductivity, abrasion resistance, and color stability. However poor resistance to fracture and shrinkage during firing process have been limiting factors in their use, particularly in multiunit ceramic restorations. A new method for making all-ceramic crowns that have high strength and low processing shrinkage has been developed and is referred to as the Vita In-Ceram method. This study was performed to investigate the effect of $CeO_2$ addition in borosilicate glasses on the strength of alumina-glass composites. Porous alumina compacts were prepared by slip casting and sintered at $1,100^{\circ}C$ for 2 hours. Dense composites were made by infiltration of molten glass into partially sintered alumina at $1,140^{\circ}C$ for 4 hours. Specimens were polished sequentially from #800 to #2000 diamond disk. and the final surface finishing on the tensile side was received an additional polishing sequence through $1{\mu}m$ diamond paste. Biaxial flexure test was conducted by using ball-on-three-ball method at a crosshead speed of 0.5mm/min. To examine the microstructural aspect of crack propagation in the alumina-glass composites, Vickers-produced indentation crack was made on the tensile surface at a load of 98.0 N and dwell time of 15 sec, and the radial crack patterns were examined by an optical microscope and a scanning electron microscope. The results obtained were summarized as follows; 1. The porosity rates of partially sintered alumina decreased with the rising of firing temperature. 2. The maximum biaxial flexure strength of 423.5MPa in alumina-glass composites was obtained with an addition of 3 mol% $CeO_2$ in glass composition and strength values showed the aspect of decrease with the increase of $CeO_2$ content. 3 The biaxial flexure strength values of alumina-glass composites were decreased with rising the firing temperature. 4. Observation of the fracture surfaces of alumina-glass composites indicated that the enhancement of strength in alumina-glass composites was due to the frictional or geometrical inter-locking of rough fracture surfaces and ligamentary bridging by intact islands of materials left behind the fracture front.

• 한국수소및신에너지학회논문집
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• 제17권4호
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• pp.353-361
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• 2006

As one of the thermochemical water splitting hydrogen production cycles, which could be operated at the lower temperature below 1200 K, we investigated the feasibility of the cyclic operation of Ispra Mark 2 cycle with the addition of $ZrO_2$. The cycle is theoretically composed of three reaction steps; (1) 1st step($2MnO_2{\rightarrow}Mn_2O_3+0.5O_2$), (2) 2nd step($Mn_2O_3+4NaOH{\rightarrow}2Na_2O{\cdot}MnO_2+H_2+H_2O$) and (3) 3rd step($2Na_2O{\cdot}MnO_2H_2O{\rightarrow}4NaOH+2MnO_2$). From the TPR tests, the temperature ranges for $O_2$ production in 1st step and $H_2$ production in 2nd step were $550{\sim}750^{\circ}C$ and $650{\sim}750^{\circ}C$, respectively. In $MnO_2/Mn_2O_3/NaOH$ system, the formation of molten products due to the reaction between manganese oxides and NaOH were greatly decreased with the addition of $ZrO_2$. In addition, the results of a cyclic test were discussed with the viewpoint of $H_2$ production amounts and the feasibility of the process improvement.

• 분석과학
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• 제23권1호
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• pp.45-53
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• 2010

우라늄 화합물 중에 함유된 염소를 정량하기 위하여 수증기증류 및 열가수분해를 이용한 량 염소의 분리 및 정량법을 개발하였다. 수증기 증류에 의한 시료 중의 염소를 분리하기 위하여 수증기 발생장치, 증류플라스크 및 냉각기 등으로 구성된 장치를 제작 설치하였다. LiCl 표준용액과 모의사용후핵 연료 일정량을 혼합하여 만든 우라늄 화합물 시료 중의 염소를 분리하기 위하여 혼산(0.2 M ferrous ammonium sulfate-0.5M sulfamic acid 3 mL + phosphoric acid 6 mL + sulfuric acid 15 mL)을 이용하여 $140^{\circ}C$로 증류시키고 $90{\pm}5\;mL$를 수집하였다. 열가수분해에 의한 시료 중의 염소를 분리하기 위하여 공기공급장치, 온수공급장치, 석영반응관, 연소로 및 연소보트, 그리고 휘발 염소 흡수장치로 구성된 열가수분해장치를 제작 설치하였다. 일정량의 우라늄 화합물 시료에 반응촉진제($U_3O_8$)를 가하고 1 mL/min의 공기유속과 $80^{\circ}C$의 공급수 온도를 유지하고 $950^{\circ}C$에서 1시간 반응시켜 시료 중의 염소를 분리하였다. 두 방법에 의하여 수집된 각 흡수용액은 일정부피로 희석하고 이온크로마토그래피로 정량하여 회수율을 측정하였다. 금속전환체 잔류 용융염 중의 미량 염소를 이온크로마토그래피로 정량하기 위하여 시료를 공기 및 건조 산화시키고 분쇄한 후 열가수분해하여 염소를 회수하였다.

• 한국자기학회지
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• 제3권3호
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• pp.201-207
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• 1993

$Pr_{15}Fe_{77}B_{8}$ 조성의 합금을 Ar분위기에서 유도용해로를 이용하여 주조하 였다. 이 합금을 석영관에 넣어 고주파 유도로를 이용하여 용해한 후 0.6 nm의 분출구를 통해 회전하는 Cu wheel위에 분사하여 비본형태로 제조하였다. 이 리본을 열간변형하여 결정방향성을 주었는데 이를 위 해 먼저 $680^{\circ}C$에서 $21.8\;kg/mm^{2}$의 압력으로 hot-press하여 92%의 densification을 갖는 시편을 얻을 수 있었다. 이 시편을 다양한 조건하에서 die-upset을 행하였다. 변형율이 높을 수록 $_{i}H_{c}$는 저하되었으나, $B_{r}$은 현저하게 증가되었으며, XRD 분석 결과(006)면에서의 회절강도가 증가되었다. 따라서 압축방향으로 자화용이축이 형성되었음을 알 수 있었다. Die-upset시의 변형속도가 빠를 수록 $_{i}H_{c}$는 증가되었으나, $B_{r}$은 감소되었다. 가공온도에 따른 $B_{r}$의 변화는 $750^{\circ}C$ 까지 상승한 후 감소되었다. 이 조성의 $4{\pi}M_{s}$는 11.8 kG였고 $750^{\circ}C$에서 0.05 mm/sec의 가공속도로 변형률 0.8로 die-upset한 경우에는 $B_{r}$이 11.0 kG로 우수한 자기이방성을 가지고 있으나, die-upset후에 $_{i}H_{c}$가 낮은 문제점이 있다.

• 한국결정성장학회지
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• 제22권3호
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• pp.115-121
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• 2012

사파이어 단결정은 GaN계 화합물 증착이 용이하여 고휘도의 청색을 구현하기 위한 LED(Light Emitting Diode)용 기판으로 크게 각광받고 있다. 공업용 사파이어의 제조 방법으로는 Kyropoulos법, Czochralski법 HEM(Heat Exchager Method)등 다양한 방법이 시도되고 있으며, 그 중 Kyropoulos법은 고품질의 대구경 사파이어 단결정 성장이 가능한 대표적인 방법으로 알려져 있다. 그러나 Kyropoulos 공정의 특성상 결정성장로 내에서 용융 사파이어의 유동장이 단결정의 최종 품질을 결정하는데, 유동장의 변화와 이에 따르는 결정성장 거동을 관찰하기가 어렵다는 단점이 있다. 대구경화와 동시에 고품질의 사파이어 단결정을 생산하기 위해서는 성장로내의 유동장 해석을 통해 결정 성장조건을 최적화 하는 것이 필요하다. 본 연구에서는 유한요소법을 기반으로 한 전산유동해석을 통해 Kyropoulos 성장로 내의 도가니 형상의 종횡비(h/d)에 따른 용융 사파이어의 대류거동을 관찰하여 도가니의 형상이 단결정 성장에 미치는 영향을 분석하였으며, 성장로의 설계시 도가니의 종횡비를 작게 고려하면 용융 사파이어의 대류속도를 늦추고 계면의 convexity를 줄여 사파이어 단결정의 품질향상에 도움이 된다는 결과를 얻었다.

• 한국산학기술학회논문지
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• 제14권6호
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• pp.3108-3113
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• 2013

이 연구에서는 옥텐의 함량이 다른 4가지 메탈로센 LLDPE (mLLDPE)를 각각 HDPE와 여러 조성에서 혼합한 후 시료들의 결정화 거동 및 기계적인 물성을 관찰하여 mLLDPE/HDPE의 혼화성에 관하여 연구하였다. 옥텐의 함량이 4.1, 6.8, 9.8 및 12.5 mol.% 인 네 종류의 mLLDPE에 HDPE를 100/0, 80/20, 60/40, 40/60/ 20/80 및 0/100의 비율로 용융 혼합하여 시료를 제조하였고, 이 시료의 결정화 온도, 용융온도를 DSC를 이용하여 측정하였다. 또한 각 시료의 기계적 물성을 인장 시험기를 이용하여 측정하였다. HDPE와 mLLDPE의 결정화 온도 및 용융온도는 상대편 고분자의 존재에 의하여 변하는 것으로 보아 용융상태에서 두 물질이 서로 같이 존재하는 구조, 즉 완전히 균일상이거나 최소한 부분적 상용성이 있음을 알 수 있었다. 용융온도가 낮은 mLLDPE의 용융피크는 HDPE를 첨가함에 따라증가하는 것으로 보아 mLLDPE의 결정상에는 HDPE가 같이 결정화가 되어 있는 것을 알 수 있었다. 그러나 HDPE결정에 mLLDPE가 같이 결정화 되어있는지는 확인할 수 없었다. 열분석과 기계적 물성을 측정한 결과 HDPE와 mLLDPE의 상용성은 mLLDPE에서 존재하는 옥텐의 함량이 낮을수록 증가하는 것을 알 수 있었다.