• 한국분말야금학회:학술대회논문집
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• 한국분말야금학회 2000년도 춘계학술강연 및 발표대회 강연 및 발표논문 초록집
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• pp.9-10
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• 2000

An important business-field of world-wide steel-industry is the coating of thin metal-sheets with zinc, zinc-aluminum and aluminum based materials. These products mostly go into automotive industry. in particular for the car-body. into building and construction industry as well as household appliances. Due to mass-production, the processing is done in large continuously operating plants where the mostly cold-rolled metal-strip as the substrate is handled in coils up to 40 tons unwind before and rolled up again after passing the processing plant which includes cleaning, annealing, hot-dip galvanizing / aluminizing and chemical treatment. In the liquid Zn, Zn-AI, AI-Zn and AI-Si bathes a combined action of corrosion and wear under high temperature and high stress onto the transfer components (rolls) accounts for major economic losses. Most critical here are the bearing systems of these rolls operating in the liquid system. Rolls in liquid system can not be avoided as they are needed to transfer the steel-strip into and out of the crucible. Since several years, ceramic roller bearings are tested here [1.2], however, in particular due to uncontrollable Slag-impurities within the hot bath [3], slide bearings are still expected to be of a higher potential [4]. The today's state of the art is the application of slide bearings based on Stellite\ulcorneragainst Stellite which is in general a 50-60 wt% Co-matrix with incorporated Cr- and W-carbides and other composites. Indeed Stellite is used as the bearing-material as of it's chemical properties (does not go into solution), the physical properties in particular with poor lubricating properties are not satisfying at all. To increase the Sliding behavior in the bearing system, about 0.15-0.2 wt% of lead has been added into the hot-bath in the past. Due to environmental regulations. this had to be reduced dramatically_ This together with the heavily increasing production rates expressed by increased velocity of the substrate-steel-band up to 200 m/min and increased tractate power up to 10 tons in modern plants. leads to life times of the bearings of a few up to several days only. To improve this situation. the Mechanical Alloying (MA) TeChnique [5.6.7.8] is used to prOduce advanced Stellite-based bearing materials. A lubricating phase is introduced into Stellite-powder-material by MA, the composite-powder-particles are coated by High Energy Milling (HEM) in order to produce bearing-bushes of approximately 12 kg by Sintering, Liquid Phase Sintering (LPS) and Hot Isostatic Pressing (HIP). The chemical and physical behavior of samples as well as the bearing systems in the hot galvanizing / aluminizing plant are discussed. DependenCies like lubricant material and composite, LPS-binder and composite, particle shape and PM-route with respect to achievable density. (temperature--) shock-reSistibility and corrosive-wear behavior will be described. The materials are characterized by particle size analysis (laser diffraction), scanning electron microscopy and X-ray diffraction. corrosive-wear behavior is determined using a special cylinder-in-bush apparatus (CIBA) as well as field-test in real production condition. Part I of this work describes the initial testing phase where different sample materials are produced, characterized, consolidated and tested in the CIBA under a common AI-Zn-system. The results are discussed and the material-system for the large components to be produced for the field test in real production condition is decided. Outlook: Part II of this work will describe the field test in a hot-dip-galvanizing/aluminizing plant of the mechanically alloyed bearing bushes under aluminum-rich liquid metal. Alter testing, the bushes will be characterized and obtained results with respect to wear. expected lifetime, surface roughness and infiltration will be discussed. Part III of this project will describe a second initial testing phase where the won results of part 1+11 will be transferred to the AI-Si system. Part IV of this project will describe the field test in a hot-dip-aluminizing plant of the mechanically alloyed bearing bushes under aluminum liquid metal. After testing. the bushes will be characterized and obtained results with respect to wear. expected lifetime, surface roughness and infiltration will be discussed.

• 한국응용과학기술학회지
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• 제20권1호
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• pp.33-43
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• 2003

$LiMn_2O_4$ catalyst for $CO_2$ decomposition was synthesized by oxidation method for 30 min at 600$^{\circ}C$ in an electric furnace under air condition using manganese(II) nitrate $(Mn(NO_3)_2{\cdot}6H_2O)$, Lithium nitrate ($LiNO_3$) and Urea $(CO(NH_2)_2)$. The synthesized catalyst was reduced by $H_2$ at various temperatures for 3 hr. The reduction degree of the reduced catalysts were measured using the TGA. And then $CO_2$ decomposition rate was measured using the reduced catalysts. Phase-transitions of the catalysts were observed after $CO_2$ decomposition reaction at an optimal decomposition temperature. As the result of X-ray powder diffraction analysis, the synthesized catalyst was confirmed that the catalyst has the spinel structure, and also confirmed that when it was reduced by $H_2$, the phase of $LiMn_2O_4$ catalyst was transformed into $Li_2MnO_3$ and $Li_{1-2{\delta}}Mn_{2-{\delta}}O_{4-3{\delta}-{\delta}'}$ of tetragonal spinel phase. After $CO_2$ decomposition reaction, it was confirmed that the peak of $LiMn_2O_4$ of spinel phase. The optimal reduction temperature of the catalyst with $H_2$ was confirmed to be 450$^{\circ}C$(maximum weight-increasing ratio 9.47%) in the case of $LiMn_2O_4$ through the TGA analysis. Decomposition rate(%) using the $LiMn_2O_4$ catalyst showed the 67%. The crystal structure of the synthesized $LiMn_2O_4$ observed with a scanning electron microscope(SEM) shows cubic form. After reduction, $LiMn_2O_4$ catalyst became condensed each other to form interface. It was confirmed that after $CO_2$ decomposition, crystal structure of $LiMn_2O_4$ catalyst showed that its particle grew up more than that of reduction. Phase-transition by reduction and $CO_2$ decomposition ; $Li_2MnO_3$ and $Li_{1-2{\delta}}Mn_{2-{\delta}}O_{4-3{\delta}-{\delta}'}$ of tetragonal spinel phase at the first time of $CO_2$ decomposition appear like the same as the above contents. Phase-transition at $2{\sim}5$ time ; $Li_2MnO_3$ and $Li_{1-2{\delta}}Mn_{2-{\delta}}O_{4-3{\delta}-{\delta}'}$ of tetragonal spinel phase by reduction and $LiMn_2O_4$ of spinel phase after $CO_2$ decomposition appear like the same as the first time case. The result of the TGA analysis by catalyst reduction ; The first time, weight of reduced catalyst increased by 9.47%, for 2${\sim}$5 times, weight of reduced catalyst increased by average 2.3% But, in any time, there is little difference in the decomposition ratio of $CO_2$. That is to say, at the first time, it showed 67% in $CO_2$ decomposition rate and after 5 times reaction of $CO_2$ decomposition, it showed 67% nearly the same as the first time.

• 한국수산과학회지
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• 제33권5호
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• pp.448-454
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• 2000

IOSP를 이용하여 적조생물입자에 대한 응집실험을 한 결과는 다음과 같다. 본 실험에 사용한 IOSP의 평균 지름은 $11.6{\mu}m$이고, 약$ 77{\%}$의 입자가 $5.0{\~}20.0{\mu}$의 범위에 속하며 변동계수는 $60.1{\%}$이었다. IOSP의 금속성분을 분석한 결과는 $98{\%}$가 칼슘으로서 생석회(CaO)와 같은 성분이었다. IOSP의 전자현미경 사진을 분석한 결과 표면이 매끈한 부정형의 입자로 되어 있었다. IOSP에 해수를 첨가하면 해수중의 $Mg^(+2)$ 이온과 급속하게 반응하여 입자의 표면 주위에 점질성의 $Mg(OH)_2$ 흡수층 (absorption layer)을 형성하여 응집 침전하고 해수의 pH를 10.0 정도까지 상승시켰다. IOSP는 $pH=6.2{\~}12.7$에서 $11.1{\~}50.1 mV$로서 IOSP의 입자가 완전히 용해될 때까지 positive zeta potential을 나타낸 반면 OSP는 pH=9.2, 11.9에서 각각 -42.5, -56.9mV로서 negative zeta potential을 나타내었다. $pNa=2.0{\~}4.0 (10^(-4){\~}10^(-2)M Na^+)$에서 IOSP, OSP의 zeta potential은 거의 일정한 값을 나타내었으나 $pNa=0.0 (1 M Na^+)$에서는 IOSP의 EDL이 매우 크게 압축되어 zeta potential은 거의 0.0mV를 나타내었고 OSP는 -25.4mV의 여전히 높은 negative zeta potential을 나타내었다. IOSP는 $Mg^(+2)$ 이온의 농도가 증가함에 따라 positive zeta potential이 증가하다가 $pMg=3.0 (10^(-3)M Mg^(+2))$에서 감소하는 결과를 나타내었다. 해수 중에서 IOSP는 4.8mV의 positive zeta potential을 나타내었고, OSP와 RTO는 각각 -30.7mV, -9.2mV의 negative zeta potential을 나타내었다. 해수중에서 IOSP의 $Mg(OH)_2$ 흡수층과 적조생물입자 사이에는 positive-negative EDL 반응이 일어나서 이들 둘 사이에는 항상 전기동력학적 인력이 작용하고, 동시에 $Mg(OH)_2$ 흡수층에 의한 전하중화로 인하여 입자 상호간의 응집반응은 극단적 인력이 작용하는 primary minimum에서 일어나고, DLVO 이론에 따라 응집반응은 비가역적아며 매우 신속하게 일어났다. 적조생물입자의 응집제거 효율은 IOSP의 농도 50mg/l까지 급격한 증가를 보이다가 IOSP의 농도가 계속 증가함에 따라서 점점 완만한 증가를 나타내었다. 즉 IOSP의 농도가 증가함에 따라서 지수함수적으로 증가하였다 ($Y=53.81{\times}X^(0.1); R^2=0.9868$).응집 침전은 IOSP 400mg/l 이상에서 거의 완전히 일어났다. IOSP $100mg/l$을 사용하고 G-value를 $1, 6, 29, 139 sec^(-1)$로 단계적으로 증가시키면서 응집 실험을 한 결과 적조생물입자의 응집제거 효율이 각각 $70.5, 70.5, 81.7, 85.3{\%}$로 증가하였다. 이는 응집 반응에서 입자간 충분한 충돌이 일어날 수 있도록 교반하는 것이 매우 중요함을 나타내 주는 것이다.

• Maxillofacial Plastic and Reconstructive Surgery
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• 제31권2호
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• pp.136-142
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• 2009

Bone density in the recipient implant site seems to be an important factor for long term success of endosseous implants. Preoperative evaluation of bone density is very helpful to assist the clinician with the treatment planning of implant therapy. Accurate information on bone density will help the surgeon identify suitable implant sites, thereby improving the success rate of the procedure. Purpose; The aim of this study was to evaluate a correlation between bone density measured preoperatively with computerized tomography and histologically measured bone density by bone biopsy. Patients and methods; Twenty seven patients were selected. All the patients were in good health, with no systemic disorder and additional bone graft. Preoperatively the patients underwent CT scanning to evaluate Houmsfield Unit(HU). Each patients wore a surgical template for implant placement. During surgery 2mm in diameter and 6mm in length specimens were taken. Histomorphometric analysis was performed using digitalized image analysis software Axiovision 4.3. Also, the Resonance frequency analysis(RFA) and insertion torque values were recorded. Results; The highest histomorphometric values was found in the posterior mandible $32.3{\pm}3.8$, followed by $29.9{\pm}2.6$ for the posterior maxilla, $29.4{\pm}2.6$ for the anterior maxilla, $28.6{\pm}2.3$ for the anterior mandible(p=0.214). The hounsfield unit was $989.2{\pm}258.1$ in the posterior mandible, $845.0{\pm}241.5$ in the anterior maxilla, $744.5{\pm}92.6$ in the anterior mandible, $697.3{\pm}136.9$ in the posterior maxilla(p=0.045). This results may suggest that there are strong correlation between the histomorphometric values and hounsfield unit(r=0.760, p<0.05). The RF measurements were $81.9{\pm}2.4$ ISQ in the posterior mandible, $79.0{\pm}1.4$ ISQ in the anterior mandible, $78.3{\pm}4.6$ ISQ in the posterior maxilla, $76.5{\pm}5.0$ ISQ in the anterior maxilla(p=0.048). The insertion torque values was $43.2{\pm}4.2\;Ncm$ in the posterior mandible, $42.0{\pm}0.0\;Ncm$ in the anterior mandible, $41.3{\pm}4.1\;Ncm$ in the posterior maxilla, $40.8{\pm}3.8\;Ncm$ in the anterior maxilla(p=0.612). This results may suggest that there are statistical significance between the hounsfield unit and the insertion torque values(r=0.494, p<0.05), the histomorphometric values and the insertion torque values(r=0.689, p<0.05). But there was no correlation between histomorphometric values and ISQ. There was no statistical significance in age and gender effect on parameters. Conclusions; There was significant correlations between bone density and implant stability parameters. The bone density measurements using preoperative CT may help clinicians to predict primary stability before implant insertion, which is associated with implant survival rates.

• 청정기술
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• 제25권1호
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• pp.81-90
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• 2019

프로페인($C_3H_8$)의 건식 개질($CO_2$ 개질)을 통한 합성 가스($H_2$와 CO 혼합물) 제조를 위해 $Ni-CeO_2/{\gamma}-Al_2O_3$ 촉매가 충진된 유전체 장벽 방전 플라즈마 반응기를 사용하였다. 열 또는 플라즈마에 의해 환원된 $Ni-CeO_2/{\gamma}-Al_2O_3$ 촉매를 사용하여 $C_3H_8/CO_2$ 비율 1/3, 총 유량 $300mL\;min^{-1}$에서 플라즈마-촉매 건식 개질을 수행하였다. 건식 개질에 대한 촉매 활성은 온도범위 $500{\sim}600^{\circ}C$에서 평가되었다. $Ni-CeO_2/{\gamma}-Al_2O_3$ 촉매 제조를 위해 전구물질 수용액(질산니켈, 질산세륨)으로 함침된 ${\gamma}-Al_2O_3$를 공기 분위기에서 소성시킨 후, $H_2/Ar$ 분위기에서 환원시켰다. 촉매 특성 조사에는 X-선 회절분석기(XRD), 투과전자현미경(TEM), 전계 방출 주사전자현미경(FE-SEM), 승온 탈착($H_2-TPD$, $CO_2-TPD$) 및 라만 분광기가 이용되었다. 열로 환원된 촉매와 비교하면 플라즈마 방전하에서 환원된 $Ni-CeO_2/{\gamma}-Al_2O_3$ 촉매가 개질 반응을 통한 합성 가스 생산에서 보다 우수한 촉매 활성을 나타내었다. 또한, 플라즈마로 환원된 $Ni-CeO_2/{\gamma}-Al_2O_3$가 개질 반응의 문제점인 탄소퇴적 관점에서 장기 촉매 안정성을 보여주었다.

• 한국수산과학회지
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• 제33권5호
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• pp.455-462
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• 2000

점증하는 적조로부터 수산피해를 줄이는 것은 시급한 문제이다. 황토를 살포하여 적조생물입자를 응집 제거하는 것이 하나의 방법이 되고 있다. 황토를 이용하여 적조생물입자에 대한 응집실험을 한 결과는 다음과 같다. 본 실험에 사용한 황토입자의 입도 분포는 정규분포를 보여주는 하나의 peak로 나타났으며, 입자의 평균 지름은 $25.0 {\mu}m$이고, 약$84.5{\%}$의 황토입자가 $9.8-55.0{\mu}m$의 범위에 속하며 변동계수는 $65.1{\%}$이었다. 황토의 금속성분을 분석한 결과는 규소 (Si)가 $48{\%}$, 알루미늄 (Al)이 $35{\%}$, 철 (Fe)이 $11{\%}$로서 $94{\%}$를 차지하며 나머지 $48{\%}$는 칼릅 (K), 구리 (Cu), 아연 (Zn), 티타늄 (Ti) 등으로 구성되어 있었다. 전자현미경 사진에 나타난 황토입자의 표면은 거칠고 다공질이며 부정형의 입자로 되어 있었다. 황토입자는 $10^(-3)M$ NaCl의 수용액 중에서 pH가 증가함에 따라 negative zeta potential 값이 증가하여 pH 9.36에서 -71.3mV를 나타내고 이후 거의 일정한 값을 나타내었으며, pH 1.98에서 +1.8 mV를 나타내어 amphoteric surface charge를 가지는 물질의 성질을 나타내었다. 전하결정이온은 $H^+, OH^-$ 이온이고, pH 2 부근에서 PZPC를 나타내었다. 용액의 전해질이 NaCl일 경우 $10^(-2)M (pNa=2)$ 이상의 농도에서는 $Na^+$ 이온의 농도가 증가함에 따라서 황토입자의 negative zeta potential 값은 일률적으로 감소하다가 $Na^+$ 이온의 농도가 1M (pNa=0)이 되었을 때 zeta potential은 0에 근접하였다. 용액의 전해질이 2 :l electrolyte ($CaCl_2$와 $MgCl_2$)의 경우 $Ca^(+2)$ 이온의 농도가 증가함에 따라서 황토입자의 negative zeta potential 값이 일률적으로 감소하다가 약 $10^(-3)M (pCa=3)$의 농도에서 등전점을 나타내고 전하역전이 일어났다. 해수중의 황토와 적조생물 입자는 비슷한 negative zeta potential을 나타내었고, 점토 중에서 해사가 가장 큰 negative zeta potential을 나타내었다. 해수중에서 황토입자와 적조생물입자의 EDL은 해수에 포함된 고농도의 염류 농도로 인하여 극히 얇게 압축되고, 이런 상태에서 두 입자가 상호 접근할 경우 모든 간격에서 LVDW attractive force의 절대값이 EDL repulsive force의 절대값보다 항상 큰 값을 나타낸다. 해수중에서 황토입자와 적조생물입자는 모든 간격에서 negative total interaction energy 값 (attractive force)을 나타내어 항상 용이하게 floe을 형성할 수밖에 없는 조건에 있다. 적조생물입자의 응집제거 효율은 황토의 농도가 증가함에 따라서 지수함수적 ($Y=36.04{\times}X^(0.11); R^2=0.9906$)으로 증가하였으며, 황토의 농도 800mg/l까지 급격한 증가를 보이다가 황토의 농도가 계속 증가함에 따라서 완만한 증가를 나타내었다. 적조생물은 황토 6,400mg/l에서 거의 $100{\%}$ 응집제거 되었다. 황토 800 mg/l을 사용하고 G-value를 $1, 6, 29, 139 sec^(-1)$로 단계적으로 증가시킴에 따라 응집제거 효율은 지수함수적으로 증가하였다. 이는 응집반응의 효율을 높이기 위해서는 황토입자와 적조생물입자 사이에 충분한 충돌이 일어날 수 있도록 교반하는 것이 매우 중요함을 나타내 주는 것이다. $800mg/l$의 농도에서 황토는 철을 함유하지 않은 다른 점토보다 $28.8{\~}60.3{\%}$ 더 높은 처리효율을 나타내었다. 황토에는 >SiOH의 음전하단과 수중의 phenolphthalein alkalinity를 소모하는 수화금속화합물의 양전하단이 공존하며, 이 수화금속화합물에 의하여 황토가 나머지 점토 특히 해사와 다른 응집특성을 보여주는 것으로 생각된다.