• 대한화학회지
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• 제32권3호
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• pp.267-275
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• 1988

$Al(OC_3H_7)_3$ 및 $Si(OC_2H_5)_4$, 알콕사이드를 합성하고 그 물질을 각각 또는 혼합가수분해하여 $Al_2O_3,\;SiO_2,\;Al_2O_3-SiO_2$계의 물질을 얻고 $Al_2O_3-SiO_2$계에 환원제로서 carbon black을 혼합하여 $N_2$분위기에서 환원질화반응시켜 고순도의 ${\beta}-sialon$ 초미분말을 합성하였다. 가수분해 과정에서는 반응조건이 가수분해반응에 미치는 영향을 알아보았고, 환원질화반응 과정에서는 중간생성물을 분석하여 반응경로를 추정하고 ${\beta}-sialon$의 생성반응에 대한 동력학적 고찰을 하였다.

• 한국세라믹학회지
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• 제24권1호
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• pp.23-32
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• 1987

Synthesis of high purity ultrafine Si3N4 and ${\beta}$-Sialon powders was investigated via the simultaneous reduction and nitriding of amorphous SiO2, SiO2-Al2O3 system prepaerd by hydrolysis of alkoxides, using carbonablack as a reducing agent. In Si(OC2H5)4-C2H5 OH-H2 O-NH4OH system, hydrolysis rate increased with increasing reaction temperature and pH. Pure ${\alpha}$-Si3N4 was formed at 1350$^{\circ}C$ for 5 hrs in N2 atmosphere. In Si(OC2H5)4-Al(OC3H7)3-C6H6-H2 O-NH4OH system, weight loss increased as Si/Al ratio decreased. Single phase ${\beta}$-Sialon consisted of Si/Al=2 was formed at 1350$^{\circ}C$ in N2 and minor phases of ${\alpha}$-Si3N4, AIN, and X-phase were existed besides theSialon phase at other Si/Al ratios. The Si3N4 and Sialon powders synthesized from alkoxides consisted of uniform find particles of 0.05-0.2$\mu\textrm{m}$ in diameter, respectively.

• 한국수소및신에너지학회논문집
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• 제22권3호
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• pp.340-348
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• 2011

Effects of various inorganic-metal oxide (Zr, Zn, Si, Al and Ca as promoters and stabilizers) additive on the reduction rate of iron oxide and the composition of forming hydrogen using the steam-iron cycle operation was investigated. The reduction rate of redox agent with additive was determined from weight change by TGA. The changes of weight loss and reduction rate according to redox agent with various additive affected the hydrogen purity and cycle stability of the process. The cyclic micro reactor showed that hydrogen purity exceeding 95% could be obtained by the water splitting with Si/Fe, Zn/Fe, Zr/Fe redox agents. The redox agents with these elements had an affect on redox cycle stability as a good stabilizer for forming hydrogen by the steam-iron process.

• 한국콘크리트학회:학술대회논문집
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• 한국콘크리트학회 2008년도 추계 학술발표회 제20권2호
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• pp.613-616
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• 2008

최근 결합재로 시멘트를 사용하지 않은 알칼리 활성 콘크리트에 대한 연구가 활발히 진행되고 있다. 이 알칼리 활성 콘크리트는 시멘트 대신에 실리콘(Si)과 알루미늄(Al)이 풍부한 플라이애시와 고로슬래그등을 사용하여 알칼리 용액으로 활성화시킨 시멘트 ZERO 콘크리트로서 CO$_2$ 가스를 저감하는데 효과적이다. 본 연구에서는 시멘트를 전혀 사용하지 않고 결합재로서 고로슬래그를 100% 사용한 알칼리 활성 콘크리트를 개발할 목적으로 감수제, 알칼리 활성화제 및 양생조건이 모르타르의 시공성 및 압축강도에 미치는 영향에 대해 검토하였다. 그 결과, NaOH의 몰 농도가 증가함에 따라 유동성은 저하되나, 9M까지는 유동성 저하가 크지 않고, 대부분의 감수제는 유동성 향상에 기여하지 못하는 것으로 나타났다. 그리고 압축강도는 NaOH의 몰 농도가 증가함에 따라 향상되나, 9M이 가장 효율적인 것으로 나타났다. 또한 양생온도 및 양생조건은 고로슬래그 알칼리 활성 모르타르의 강도에는 큰 영향이 없는 것으로 나타났다.

• 한국재료학회지
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• 제12권1호
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• pp.48-53
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• 2002

$Al_2O_3-SiC$ and $Al_2O_3-SiC$-TiC composite powders were prepared by SHS process using $SiO_2,\;TiO_2$, Al and C as raw materials. Aluminum powder was used as reducing agent of $SiO_2,\;TiO_2$ and activated charcoal was used as carbon source. In the preparations of $Al_2O_3-SiC$, the effect of the molar ratio in raw materials, compaction pressure, preheating temperature and atmosphere were investigated. The most important variable affecting the synthesis of $Al_2O_3-SiC$ was the molar ratio of carbon. Unreactants remained in the product among all conditions without compaction. The optimum condition in this reaction was $SiO_2$: Al: C=3: 5: 5.5, 80MPa compaction pressure under Preheating of $400^{\circ}C$ with Ar atmosphere. However there remains cabon in the optimum condition. The effect of $TiO_2$ as additive was investigated in the preparations of $Al_2O_3-SiC$. As a result of $TiO_2$ addition, $Al_2O_3-SiC$-TiC composite powder was prepared. The $Al_2O_3$ powder showed an angular type with 8 to $15{\mu}m$, and the particle size of SiC powder were 5~$10{\mu}m$ and TiC powder were 2 to $5{\mu}m$.

• 한국건설순환자원학회논문집
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• 제1권2호
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• pp.101-106
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• 2013

본 연구에서는 CA계 슬래그와 무수석고를 사용하여 수축저감제를 제조하였으며, 모르타르의 압축강도와 건조수축 특성을 향상시키기 위해서 상기 수축저감제를 첨가하였다. 모르타르의 응결시간, 길이변화율 및 압축강도는 수축저감제의 배합비율에 따라 변화하였다. 슬래그가 0~7%까지 첨가된 모르타르는 슬래그 첨가량 증가에 따라 응결시간이 짧아졌으며, 7일까지의 길이변화율은 유사하였다. 7일 양생조건의 압축강도는 $C_{12}A_7$계 슬래그 첨가량 증가에 따라 증가되었다. $C_{12}A_7$계 슬래그가 6% 첨가된 모르타르의 28일 강도는 약 36 MPa이었으며, 35일에서의 건조수축율은 가장 낮은 값을 나타내었다. 그러므로 $C_{12}A_7$계 슬래그가 6% 첨가된 모르타르에서 우수한 물리적 특성을 발현하는 것으로 판단할 수 있었다.

• 한국재료학회지
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• 제16권5호
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• pp.285-291
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• 2006

Copper powders have been widely used in electrically conductive coatings, electrode materials et al. and are very prospective since they are cheaper than noble metal powders such as silver or palladium. In this study, copper powders for metal filler of EMI shielding have been prepared using a solvothermal process from $CuSO_4$, NaOH, Glucose, mixed solvent ($H_2O$: Ethanol) and hydrazine which was used as a reducing agent at various reaction conditions. The prepared copper powders showed finely dispersed spherical shape without agglomerate, uniform morphology, narrow size distribution, high purity and were about 400-700 nm in size. The prepared powders were characterized using XRD, SEM, TGA, XPS, particle size measurement and EMI shielding efficiency.

• 대한환경공학회지
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• 제22권1호
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• pp.169-178
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• 2000

알루미나 상에 페롭스카이트 산화물 촉매를 구연산 용액에서 제조하였다. 고온 배가스 처리에 페롭스카이트 촉매의 적용가능성을 평가하기 위해 충진 촉매 반응기내에서 조업온도와 $CO/NO_x$ 몰비를 변화시키면서 CO에 의한 $NO_x$의 환원특성을 실험하였다. 본 연구에서 제조한 촉매를 분석한 결과 알루미나 상에 $La_{0.5}Sr_{0.5}CoO_3$, $SrAl_{12}O_{19}$, $LaAl_{11}O_{18}$의 복합산화물이 균일하게 분포되어 있음을 확인하였다. $CO/NO_x$ 몰비가 1보다 높은 조건에서 $NO_x$의 전환율은 온도가 높아짐에 따라 $700^{\circ}C$ 근방까지는 급격히 증가하였고, 그 이상에서는 100%에 근접하였다. 또한 조업온도 $800^{\circ}C$, 공간속도 $10700hr^{-1}$에서 23시간 연속조업한 결과 $NO_x$의 전환율은 98% 이상으로 유지됨을 확인할 수 있었다.

• 한국물환경학회지
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• 제34권6호
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• pp.621-631
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• 2018

In this study, catalyst was made through incipient wetness method using palladium (Pd) as noble metal, indium (In) as secondary metal, and montmorillonite (MK10) and Al pillared montmorillonite (Al-MK10) as supporters. The nitrate reduction rate of the catalysts was measured by batch experiments where H2 gas was used as reducing agent and formic acid as pH controller. Transmission electron microscopy (TEM) equipped with energy dispersive spectroscopy (EDS) and X-ray photoelectron spectroscopy (XPS) were all used to determine the elemental distribution of Pd, In, Al, and Si on catalysts. It was observed that Al pillaring increased the Al/Si elemental composition ratio and point of zero charge of MK10, but decreased its BET specific surface area and pore volume. The nitrate reduction rate of Al-MK10 Pd/In was 2.0 ~ 2.5 times higher than that of MK10 Pd/In using artificial groundwater (GW) in ambient temperature and pressure. Nitrate reduction rates in GW were 1.2 ~ 1.7 times lower than those in distilled deionized water (DDW). Nitrate reduction rates in acidic conditions were higher than those in neutral condition in both GW and DDW. The amount of produced NH3-N over degraded NO3- at acid conditions was lower than that of neutral condition. Even though the leaching of Pd after reaction was measured in DDW it was not detected when both Al-MK10 Pd/In and MK10 Pd/In were used in GW. The modification of montmorillonite as a supporter significantly increased the reductive catalytic activities of nitrates. However, the ratio of producing ammonia by-products to degraded nitrates in ambient temperature and pressure was similar.

• 한국세라믹학회지
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• 제24권5호
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• pp.453-460
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• 1987

β'-sialon(Z=2.7) specimens with <30%wt. graphite as a reducing agent were decomposed at 1350°up to 1,450℃ under the atmosphere of 90% N2-10%H2. The decomposition of β'-sialon was calculated from the change in Z-value, and the formation of new minerals was identified from X-ray diffraction patterns. The decomposition reactions of sialon were considered to yield a stable sialon close to β-silicon nitride and some aluminum compounds according to the following equations; β'-sialon(s)＋C(s)＋N2(g)→β2-sialon(metastable)＋β3-sialon(stalbe phase) β2-sialon(s)＋C(s)＋N2(g)→β3-sialon(s)＋AlN(s)＋α-Al2O3(s)＋15R(s)＋SiO(g)＋Al2O(g)＋CO(g) Z-value; β2( 3.5)>β'( 2.7)>β3( 0.5) The decomposition rate of sialon was controlled by two mechanisms ; One was characterized by the interface area of contact, corresponding to an apparent activation energy of 50.5Kcal/mol in the initial stage, and the other by the diffusion, corresponding to that of 104.3Kcal/mol in the final stage of the decomposition.