• 한국신재생에너지학회:학술대회논문집
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• 2009.11a
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• pp.232-232
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• 2009

최근 WGS반응용 Pt 촉매의 성능 향상을 위한 다양한 담체 및 조촉매(Promotor) 개발에 대한 연구가 활발하게 진행되고 있다. 선행 연구결과, 입방(Cubic)구조를 가지는 $Ce_{0.8}Zr_{0.2}O_2$ 담체는 정방 입계(Tetragonal)구조를 가지는 $Ce_{0.2}Zr_{0.8}O_2$ 담체 또는 혼합산화물(Mixed oxide)구조를 가지는 $Ce_{0.5}Zr_{0.5}O_2$ 담체 보다 높은 활성과 안전성을 가진다. 이것은 촉매의 성능 향상이 Ce-$ZrO_2$의 결정구조에 의존한다는 것을 나타낸다. 따라서 WGS 반응에서 Ce/Zr 비에 따라 변화된 담체 특성이 Pt 촉매의 활성에 영향이 있을 것으로 예상되며 실험결과 1% Pt/$CeO_2$ 촉매가 가장 높은 활성을 나타내었다. 따라서 Pt/Ce-$ZrO_2$ 촉매의 성능 향상을 위해 Ce-$ZrO_2$ 담체에 조촉매인 Ni을 첨가하여 촉매적 활성을 비교하여 보았다. 촉매는 2%의 Pt과 15%의 Ni로 고정하였고 Ce/Zr 비를 제조변수로 하였다. 제조된 모든 담체는 공침법(Co-precipitation)을 사용하여 제조하였으며 $500^{\circ}C$에서 6시간 소성하였다. Pt 촉매는 함침법 (Incipient wetness impregnation)으로 담지 시켰다. 2% Pt/Ce-$ZrO_2$ 촉매와 2% Pt/15% Ni-Ce-$ZrO_2$ 촉매는 저온영역($200^{\circ}{\sim}320^{\circ}C$)에서 비슷한 CO 전환율을 나타내었으나 고온영역($360^{\circ}C{\sim}400^{\circ}C$)에서는 2% Pt/15% Ni-Ce-$ZrO_2$ 촉매가 더 높은 CO의 전환율을 나타내었다. 이것은 Ni의 영향으로 고온에서 부반응인 메탄화 반응(Methanation reaction)이 생긴 것으로 판단되어 메탄($CH_4$)의 선택도를 살펴본 결과 2% Pt/15% Ni-Ce-$ZrO_2$ 촉매가 고온영역($360^{\circ}{\sim}400^{\circ}C$)에서 급격하게 증가하는 것으로 나타나 메탄화 반응이 일어난 사실을 증명한다.

• Applied Chemistry for Engineering
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• v.10 no.3
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• pp.407-414
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• 1999

We have studied the reduction of NO by CO over perovskite-type oxides prepared by malic and method. The catalysts were modified to enhance the activity by substitution of metal into A or B site of perovskite oxides. In the $LaCoO_3$ type catalyst, the partial substitution of Sr into A site enhanced the catalytic activity on the conversion of NO at less than $350^{\circ}C$. In the $La_{0.6}Sr_{0.4}Co_{1-x}Fe_xO_3$ catalyst, the partial substitution of Fe or Mn into B site enhanced the conversion of NO, but excess amount of Fe decreased the conversion of NO. In addition, $La_{0.6}Sr_{0.4}Co_{0.8}Fe_{0.2}O_3$ mixed with $SnO_2$ or $MnO_2$ showed the synergy effect on the reduction of NO. The introduction of water into reactants feed decreased the catalytic activity but the deactivation was shown to be reversible. The introduction of $SO_2$ into reactants feed also decreased the catalytic activity.

• Applied Chemistry for Engineering
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• v.20 no.2
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• pp.201-207
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• 2009

The hydrogenation reaction of methyl dodecanoate for the synthesis of 1-dodecanol has been carried out in the presence of a copper chromite catalyst. The catalysts were synthesized by ceramic method, co-precipitation, and improved co-precipitation method and the particles were characterized by SEM and XRD. Also, the products of the reaction were assigned by GC, GC/MSD and NMR. The particles synthesized by each method showed (1) a spherical shape with the size of 3.2 to $7.0{\mu}m$, (2) an agglomerated spherical shape with the size of 50 to 500 nm and (3) a spherical shape with smaller particle size, respectively. Especially, in order to control the size of particles, the particles were synthesized in various dispersant solutions as Span 80, polyacrylate, and polyethyleneglycols (PEGs). The particles synthesized in PEG (Mw = 4000) solution showed the smallest particle size of 30 to 50 nm and the regularity of the particle size distribution. Our experimental results elucidated that the activity of catalyst for hydrogenation increases with decreasing the size of catalyst particle. The highest yield of dodecanol in the hydrogenation reaction was 95.5% when copper chromite synthesized in the PEG solution was used as a catalyst in the optimized reaction condition.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2004.05a
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• pp.119-124
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• 2004

최근 소형 다기능, 고기능 전자장비의 개발로 인하여 고밀도 전원이 필요성이 대두되고 있다. 연료전지는 높은 전력 밀도를 가짐으로 인하여 소형 전원 장비에 가능성을 가지는 것으로 여겨지고 있다. 연료전지 중 특히 고분자 전해질 연료전지는 높은 전력밀도와 낮은 작동온도 등으로 인하여 이차전지의 자리를 대체할 수 있을 것으로 보여지지만 현재까지 연료 공급장치의 문제로 인하여 실용화되지 못하고 있다. 본 연구에서는 여러 가지 수소저장 물질 중에서 알칼리 붕소 수소화물을 이용하여 연료전지에 수소를 공급하고자 하며, 수소발생에 사용되는 촉매에 대한 연구를 진행하였다. 알칼리 붕소 수소화물의 수소발생 반응에 사용되는 촉매로는 Pt, Ru, Co, Ni 등이 사용되어질 수 있다. 이중에서 가장 수소발생 능력이 높은 촉매는 Ru이며, 비귀금속 촉매 중에는 Co가 높은 활성을 나타내었다. 본 연구에서는 Ru 촉매와 Co 촉매의 특성을 비교하였으며 연료전지에 수소를 공급할 수 있는 가능성을 확인하였다. Ru와 Co 촉매의 공통적인 특징은 알칼리 붕소화물인 NaBH$_4$의 농도가 높아질수록, 온도가 높아질수록 수소의 발생속도를 높이는 현상을 보였다. 또한 안정화제인 NaOH에 대하여, Ru의 경우는 농도가 높아질수록 수소발생 속도가 낮아졌으며, Co는 그 반대의 결과를 보였다. NaBH$_4$의 분해 반응으로 발생된 수소를 연료전지에 공급하여 2W급의 휴대폰용 연료전지를 구동할 수 있었다. 이로써 알칼리 붕소수소화물로부터 발생된 수소를 이용하여 안정적으로 연료전지를 구동할 수 있는 가능성을 확인하였다. 유류 분해정도를 파악하는 지시자로써 특정 무기 오염물질을 이용할 수 있을 가능성이 있으므로 좀더 이들 관계성에 대한 연구가 진행될 필요성이 있다고 판단된다.고 과학적으로 분석할 수 있는 방법이 될 수 있을 것으로 기대된다. 의미를 되새기는 것으로 짧은 연구를 시작하겠다. 등은 활성 값이 70% 이상으로 퇴적물 독성이 상대적으로 낮았다. 이중나선 DNA 함량은 28.4 % - 49%로 대조군에 비해서 감소가 크다. 대부분의 정점이 대조군의 30% 내외로 정점 간의 차이는 크지는 않다. 그러나 다른 측정자료와 같이 정점 22에서 18%로 최소치를 나타내고, 정점 2, 12에서 20% 내외의 값을 보인다. 종합적으로 볼 때 오염물질의 유입이 크고, 광양제철 인근 정점 들이 모두 다른 정점에 비해서 낮아서, 퇴적물 독성이 높은 정점으로 조사되었다.hiwo의 광합성 능력은 낮은 농도들에서는 대조구와 유사하였으나, 5 $\mu\textrm{g}$/l의 높은 농도에서는 초기에 매우 낮은 광합성 능력을 보이다가 시간이 경과하면서 대조군보다 더 높은 경향을 나타냈다. 이러한 결과는 식물플랑크톤이 benso[a]pyrene의 낮은 농도에서 노출될 때는 이 물질을 탄소원으로 사용할 가능성이 있음을 시사한다. 본 연구의 결과들은 연안해역에 benso[a]pyrene과 같은 지속성 유기오염물질이 유입되었을 때 내정여부에 따라 식물플랑크톤 군집내 종 천이와 일차생산력에 크게 영향을 미칠 수 있음을 시사한다.TEX>5.2개)였으며, 등급별 회수율은 각각 GI(8.5%), GII(13.4%), GIII(43.9%), GIV(34.2%)로 나타

• Journal of Sensor Science and Technology
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• v.9 no.1
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• pp.36-43
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• 2000

In oder to enhance the selectivity of TMA(trimethylamine) gas, the ZnO-based films which were doped with $Al_2O_3$, $TiO_2, $In_2O_3$ and $V_2O_5$ catalysts with various weight percents were deposited in oxygen by RF magnetron sputtering method. To improve electrical stability of sensors, the ZnO-based films were annealed in oxygen at $700^{\circ}C$ for 1 hour. The TMA selectivity of sensors was defined by the magnitude($S_{TMA}/S_{DMA}$ and $S_{TMA}/S_{NH3}$) of TMA sensitivity relative to DMA and sensitivity ammonia($NH_3$) sensitivity, respectively. The $ZnO+Al_2O_3(4\;wt.%)+TiO_2(1\;wt.%)+In_2O_3(1\;wt.%)$ sensor showed high $S_{TMA}/S_{DMA}$ of 5.9 and $S_{TMA}/S_{NH3}$ of 26 to 160 ppm at the working temperature of $300^{\circ}C$ respectively.

• Applied Chemistry for Engineering
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• v.17 no.3
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• pp.321-326
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• 2006

Thermal degradation of styrene dimer fraction (SDF, main compound: 47 wt% of 1,3-diphenylpropane), 5~15% of total products produced during decomposition of waste expanded polystyrene (WEPS) was investigated. Reaction condition of $360^{\circ}C$, and 152 kPa to 202 kPa was an optimum for high pressure degradation. Under this operating condition, the yield of oil was 73.8% and the selectivities to Ben, Tol, EB, SM, and AMS were 0.4, 30.9, 15.0, 19.6, and 4.2%, respectively. Non-catalytic fixed bed continuous degradation was conducted at reaction temperatures of $510{\sim}610^{\circ}C$ and contact time ranges of 2~24 min, where the yield was increased by increasing of reaction temperature and contact time. A $Cr_2O_3$ catalyst showed the highest activity and SM yield among acid, base, and redox catalysts. The conversion of 74.6% and the yield of Ben, Tol, EB, SM, and AMS were 0.4, 21.6, 9.7, 17.9, and 3.5%, respectively at $560^{\circ}C$ and contact time of 24 min. It is thought that styrene is converted to EB and other secondary products throughout the formation of diradicals of styrene.

• Applied Chemistry for Engineering
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• v.10 no.2
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• pp.247-251
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• 1999

Tungsten oxide supported on zirconia was prepared by drying powdered $Zr(OH)_4$ with ammonium metatungstate aqueous solution, followed by calcining in air at high temperature. Upon the addition of only small amount of tungsten oxide (1 wt % $WO_3$) to $ZrO_2$, both the acidity and acid strength of catalyst increased remarkably, showing the presence of $Br{\ddot{o}}nsted$ and Lewis acid sites on the surface of $WO_3$/$ZrO_2$. The high acid strength and large amount of acid sites on $WO_3$/$ZrO_2$ were due to the presence of the W=O bond nature of complex formed by the interaction between $WO_3$ and $ZrO_2$. The catalyst containing 20 wt % $WO_3$, calcined at 973 K, showed the highest catalytic activity for the 2-propanol dehydration, while the catalyst containing 15 wt % $WO_3$, calcined at 1023 K, exhibited the highest catalytic activity for the cumene dealkylation. For the 2-propanol dehydration the catalytic activities of $WO_3$/$ZrO_2$ catalysts were roughly correlated with their acidities.

• Applied Chemistry for Engineering
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• v.5 no.2
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• pp.327-336
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• 1994

The synergistic effects in mechanical mixture catalysts of Mo-V-O and metal oxide were investigated for the selective oxidation of acrolein. The metal oxides used are $SnO_2$, ${\alpha}-Sb_2O_4$, $WO_3$, ${\alpha}-Al_2O_3$, CuO, $MnO_2$, $Cu_2O$, MgO, CoO, and ZnO. Mechanical mixtures of Mo-V-O plus $SnO_2$ or ${\alpha}-Sb_2O_4$ had resulted in higher conversion of acrolein and higher yield of acrylic acid than Mo-V-O. The origin of the synergy is attributed to the cooperation of Mo-V-O and $SnO_2$ or ${\alpha}-Sb_2O_4$, in which $SnO_2$ or ${\alpha}-Sb_2O_4$ forms dissociated oxygens at their oxygen vacancies and transports them to Mo-V-O. $Cu_2O$, MgO, CuO, and $MnO_2$, increased conversion of acrolein but decreased yield of acrylic acid. CoO and ZnO inhibited the catalytic performance of Mo-V-O. The different role of these metal oxides is explained in terms of their oxidation-reduction properties.

• Applied Chemistry for Engineering
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• v.19 no.5
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• pp.466-470
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• 2008

The objective of this study is to convert methane into hydrogen using a nanoporous catalyst in the $CO_2$ containing syngas generated from the gasified waste. For the purpose, $Ni/Al_2O_3$ catalyst was prepared with the one-pot method. According to analyses of the catalyst, three dimensionally linked sponge shaped particles were created and the prepared nanoporous catalysts had larger surface area and smaller particle size and more uniform pores compared to the sphere shaped commercial catalyst. The catalyst for reforming reaction gave the highest $CH_4$ conversion of 91%, and $CO_2$ conversion of 92% when impregnated with 16 wt% of Ni at the reaction temperature of $750^{\circ}C$. At that time, the prepared catalyst remarkably improved the $CH_4$ and $CO_2$ conversion up to 20% compared to the commercial one.

• Applied Chemistry for Engineering
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• v.18 no.5
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• pp.516-521
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• 2007

The copolymerization characteristics of a newly-synthesized catalyst, $rac-Me_2Si(2-p-tolylindenyl)_2ZrCl_2$, and its analogue, $rac-Me_2Si(Ind)_2ZrCl_2$, were examined in the ethylene/1-octene copolymerization while varying the concentration of 1-octene in the reaction mixture. The activity of $rac-Me_2Si(2-p-tolylindenyl)_2ZrCl_2$ catalyst was decreased with increase of comonomer concentration, which is different from the usual comonomer effect of the metallocene catalysts with a bridge structure. The contents of 1-octene in the copolymer from the catalyst with 2-p-tolyl substituent were higher than those from the catalyst without that substituent. The melting point, crystallinity, and molecular weight decreased with comonomer content which was more apparent for $rac-Me_2Si(2-p-tolylindenyl)_2ZrCl_2$ catalyst.