• Proceedings of the Materials Research Society of Korea Conference
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• 2008.05a
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• pp.11.2-11.2
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• 2008

• Proceedings of the Materials Research Society of Korea Conference
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• 2012.05a
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• pp.57.2-57.2
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• 2012

산소 이온 전도성 세라믹을 이용한 고체 산화물 연료전지의 전극은 원활한 전기화학반응을 위해, 이온 전도도, 전자 전도도 및 전기화학적 활성을 동시에 가지고 있어야 한다. 이를 위해 복합체 전극을 사용하며, 특히 음극의 경우 니켈(Nickel)과 Yttria-stabilized zirconia (YSZ)로 이루어진 복합체 전극을 혼합 및 소결을 통해 제조하여 사용하였다. 하지만, 니켈의 경우 탄화 수소 연료에서의 탄소 침적 문제와 열악한 산화환원 안정성(redox stability)등의 문제점을 가지고 있다. 따라서 니켈대신 전도성 세라믹을 사용한 세라믹 복합체 음극 개발이 활발히 이루어지고 있으며, 그 중 침투법(infiltration method)을 이용한 복합체 전극 제조 방법을 소개한다. 실제로 니켈 금속과 유사한 높은 전기 전도도를 갖는 Sr-doped Lanthanum Vanadate (LSV)을 이용해, YSZ-LSV 복합체 전극을 침투법을 이용해 제조하고, 소량의 촉매을 첨가하여, 이온전도도, 전자 전도도 및 촉매 활성을 갖는 복합체 음극을 제조하였다. 이 복합체 음극의 탄화수소에서의 연료전지 성능 및 redox stability을 측정하였다.

• Journal of the Korean Applied Science and Technology
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• v.35 no.1
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• pp.151-156
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• 2018

As industry and medicine developed, many people became interested in the quality of life. As the concern for health became higher, vegetarian or vegetable oils became more popular than meat. With the development of processes primarily using nickel catalysts today, the shelf life of vegetable oils has increased and mobility has become more convenient. Currently nickel catalysts for the curing of oil are dominated by foreign companies in the world market. On the other hand, the mass production technology of domestic nickel catalyst is backward, and the entire amount is imported from foreign countries. Therefore, there is a need for active research and development of a catalyst that can be commercialized in korea. In this study, nickel as a main active catalyst was used as a base for hydrogen curing reaction, and the effect of rare earth on catalytic activity was investigated. A certain amount of rare earths could induce the dispersion of nickel to increase efficiency and use as co-catalyst.

• Resources Recycling
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• v.27 no.1
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• pp.22-30
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• 2018

In order to industrially recycle nickel, cobalt and rare earth elements included in waste NiMH batteries, electrode powder scraps were recovered by dismantle, crushing and classification from automobile waste battery module. As a result of leaching recovered electrode powder scrap with sulfuric acid solution, 99% of nickel, cobalt and rare earth elements were leached under reaction conditions of 1.0 M sulfuric acid solution, pulp density 25 g/L and reaction temperature $90^{\circ}C$ for 4 hours. In addition, the rare earth elements were able to separate from nickel / cobalt solution as cerium, lanthanum and neodymium precipitated under pH 2.0 using 10 M NaOH.

• Applied Chemistry for Engineering
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• v.5 no.6
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• pp.925-934
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• 1994

Nickel recovered from the spent oil-hydrogenation catalysts was used in hydrogenation catalyst preparation. The spent catalyst contains approximately 21.8% Ni, 0.7% Mg, and small quantities of Al, Fe, and Zn. Nickel recovery was obtained by inorganic acid digestion in the order of HCI>$NHO_3$>$H_2SO_4$. For $HNO_3$, 3hour extraction with 3N solution was satisfactory. In the PH range of 6.5~9.0, Ni recovery was higher, but metallic impurities were found to be coprecipitated. The PH in the range of 7.0~9.0 seems to be the optimum condition for separation to obtain acceptable Ni precipitates without the decrease of purity. The catalysts prepared with reclaimed nickel by wet reduction methods showed catalytic activities close to those prepared using reagent nickel in the oil hydrogenation reaction. The surface areas of the support do not seem to affect the catalytic activity.

• Journal of the Korean Electrochemical Society
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• v.11 no.2
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• pp.115-119
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• 2008

Single particle of nickel hydroxide and the surface-treated one with cobalt element were performed to review the effect of LiOH additive in alkaline electrolyte for Ni-MH batteries using microelectrode test system. As a result of cyclic voltammetry, the electrochemical behaviors such as the oxidation/reduction and oxygen evolution reaction are clearly observed for a single particle of nickel hydroxide, respectively. Furthermore, the reduction current peak of nickel hydroxide added with LiOH in electrolyte was very low and broad compared with the normal nickel hydroxide without an additive LiOH, which had a bad effect to the crystallization structure of nickel hydroxide. However, it was found that capacity and cycle properties of the nickel hydroxide treated with cobalt greatly increased by the addition of LiOH.

• Korean Journal of Materials Research
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• v.3 no.5
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• pp.521-528
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• 1993

Ni-graphi~e composite powders were prepared by reduct ion of $Ni^{++}$ from arnmoniacal nickel sulfate solution on graphite core by hydrogen gas at elevated temperature and pressure. Effect of coating catalyst. Anthraquinone $(C_6H_4COC_6H_4 CO)$, on the reduction rate and the properties of nickel layer were investigated by SEM, X-ray, size and chemical analysis. 1nduct.ion period, a time lag between the ~njection of hydrogen gas and the start of the reduction, was 22 to 70 mins and was affected by the size and amount of Anthraquinone. Kickel layer deposited on the surface of graphite core material was composed of nickel nodules whose sizes were different with vari~ ous reduction conditions. Minimum diameter of nickel nodules was about 2-3$\mu \textrm m$.

• Journal of the Korean Electrochemical Society
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• v.9 no.2
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• pp.95-99
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• 2006

Electrochemical properties were studied for a single particle of active material of hydrogen storage alloy $(MmNi_{3.55}Co_{0.75}Mn_{0.4}Al_{0.3})$ and nickel hydroxides $(NiOH)_2$ for the secondary Nickel Metal Hydride (Ni-MH) batteries using the microelectrode, which was manipulated to make electrical contact with an active material particle for cyclic voltammograms (CV) and potential-step experiments. As a result of CV test, it was found that three kinds of hydrogen oxidation peaks at -0.9, -0.75 and -0.65 V and hydrogen evolution peak at -0.98 V for hydrogen storage alloy were separately observed and two kinds of peaks of proton oxidation/reduction at 0.45 and 0.32 V and oxygen evolution reaction (OER) at 0.6 V for nickel hydroxides were also more clearly observed. Furthermore hydrogen diffusion coefficient within a single particle was also found to vary the order between $10^{-9}\;and\;10^{-10}cm^2/s$ over the course of hydrogenation and dehydrogenation process for potential-step experiments.

• Korean Chemical Engineering Research
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• v.48 no.6
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• pp.776-783
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• 2010

Co and Ni catalysts supported on $Al_2O_3$ for partial oxidation of methane producing hydrogen were synthesized using impregnation to incipient wetness. The activities of these catalysts for the partial oxidation of methane was investigated at 1 atm and $CH_4/O_2=2.0$ in the temperature range of $450{\sim}650^{\circ}C$. The reaction activity of $Ni/Al_2O_3$ and $Co/Al_2O_3$ catalysts with different loading was investigated. And the beneficial effects of Ni addition to $Co/Al_2O_3$ and the promotional effects of Ce and La addition to $Ni/Al_2O_3$ and $Co/Al_2O_3$ were investigated. These catalysts were characterized by XRD and SEM/EDX. Comparing catalyst loadings, 10 wt% Co and 10 wt% Ni were found to be optimal at the experimental conditions. The 10 wt% $Ni/Al_2O_3$ and 10 wt% $Co/Al_2O_3$ catalysts in partial oxidation of methane showed $CH_4$ conversions and CO selectivity close to the thermodynamic equilibrium levels, but showed lower $H_2$ selectivity than equilibrium level. The addition of Ni to $Co/Al_2O_3$ exhibited higher $H_2$ selectivity but beneficial effect was not observed in the $CH_4$ conversion. Addition of Ce to $Co/Al_2O_3$ and addition of La to $Ni/Al_2O_3$ a improved the $CH_4$ conversion level and $H_2$ selectivity.

• Proceedings of the Korean Vacuum Society Conference
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• 2010.02a
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• pp.234-234
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• 2010

최근 CMOS 소자 크기가 축소됨에 따라 소스와 드레인 영역에서의 접촉저항을 줄이기 위하여, 실리사이드 공정이 많이 연구되고 있다. 실리사이드 물질로서 NiSi는 낮은 저항률과 낮은 실리콘 소모, 낮은 공정온도, 등의 장점을 가지고 있다. 그러나, 실리사이드 형성으로 인한 나노소자의 소오스/드레인에서정션(junction) 누설전류의 증가는 큰 문제가 되므로 실리콘과 실리사이드 계면의 특성이 중요하다. 본 연구에서는 니켈을 이용한 실리사이드 형성시 계면 활성제인 에틸 요오드를 이용하여 실험을 진행하였다. 금속 유기 전구체인 MABONi을 사용하여 ALD 방식으로 증착 한 니켈 박막과 니켈 핵 형성시 계면활성제인 에틸요오드의 처리 방법에 따른 Ni-silicide 박막의 특성을 비교, 분석하였다. 먼저 자연산화막을 건식식각으로 제거한 뒤, 첫 번째 샘플에서는 10회의 주기로 초기 니켈을 증착한 뒤, 에틸요오드로 니켈의 표면 위를 처리하고, 다시 200회의 주기로 니켈을 증착하였으며, 두 번째는 첫 번째 방식에서 에틸요오드 주입 시 동시에 수소도 함께 주입하였다. 세 번째는 비교를 위해 에틸요오드 처리를 하지 않고 니켈 박막만을 증착 하였다. 이어서, 각 샘플을 급속 열처리 장비에서 $400^{\circ}C$부터 $900^{\circ}C$까지 각각 30sec간 열처리를 진행후, 반응하지 않은 잔여 니켈을 제거한 후, XRD(x-ray diffraction), AES(auger), 그리고 4-point probe 등을 이용하여 형성된 실리사이드의 특성을 분석하였다. 에틸요오드와 함께 수소를 주입한 경우 계면에서의 산소 불순물과 카본 성분이 효과적으로 제거되어 $400^{\circ}C$에서 $2.9{\Omega}/{\Box}$ 의 낮은 면저항을 가지는 NiSi가 형성되었고 모든 온도구간에서 다른 샘플에 비하여 가장 낮은 면저항 분포를 보였다. 이는 분해 흡착된 요오드에 의한 계면 특성 향상과 카본 성분이 포함된 잔여물들이 수소처리에 의해 효율적으로 제거되어 실리사이드의 특성이 향상되었기 때문이다. 계면활성제를 사용하지 않은 경우에는 $500^{\circ}C$에서 NiSi가 형성되었다. 반면에 에틸요오드로만 표면을 처리한 경우에는 니켈과 실리콘 계면에서의 카본 성분에 의하여 silicidation 이 충분히 일어나지 않았다. 이러한 결과는 향후 45nm 이하의 CMOS 공정상에서 소스와 드레인의 낮은 누설전류를 가지고, 접촉저항을 줄이기 위한 니켈 실리사이드 형성에 큰 도움을 줄 것으로 기대된다.