• 한국세라믹학회지
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• 제38권12호
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• pp.1110-1114
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• 2001

열화학기상증착법으로 탄소나노튜브를 합성할 때, 촉배전구체로 사용하는 Fe(NO$_3$)$_3$.9$H_2O$-Al(OH)$_3$혼합물을 믹서밀을 이용하여 혼합분쇄한 후, 이 혼합물을 사용하영 합성에 미치는 메카노케미컬 효과를 조사하였다. SEM과 TEM 관찰 결과, 분쇄된 촉매 위에서 합성된 탄소생성물이 미분쇄 촉매위에서 성장한 생성물에 비해 훨씬 균일했으며, 대부분의 생성물이 탄소나노튜브로서 존재하였다. 또한, 전류-전압 측정을 통해서, 분쇄 촉매에서의 생성물의 전계 방출 특성이 미분쇄 촉매에서보다 우수함을 확인하였다.

• 한국수소및신에너지학회논문집
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• 제23권6호
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• pp.647-653
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• 2012

We have investigated the kinetics and activity of waste catalysts for steam-lignite gasification. Waste catalysts I, II, III and reference $K_2CO_3$ were used and physical mixed with a coal. The gasification experiments were carried out with the low rank coal loaded with 1 wt% and 5 wt% catalyst at the temperature range from 700 to $900^{\circ}C$ using thermobalance reactor. It was observed that the carbon conversion reached almost 100% regardless of the kinds of catalysts at $900^{\circ}C$. The shortest time to reach the designated conversion was obtained for 1 wt% waste catalyst II and 5 wt% $K_2CO_3$ at $900^{\circ}C$. The gasification reaction rate constant increased with increasing the temperature. Highest rate constant was obtained with $K_2CO_3$ at $900^{\circ}C$. The lowest activation energy was 69.42 kJ/mol for 5 wt% waste catalyst II. The waste catalyst had an influence on the reduction of activation energy.

• 방사성폐기물학회지
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• 제5권3호
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• pp.221-227
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• 2007

음이온교환수지인 IRN-78및 IRN-77과의 혼합 수지를 액체 상태로 직접 분해 처리하기 위하여 Fenton 시약을 이용하였다. 개선된 분해방법의 특징은 수지를 먼저 건조시키고 $FeSO_4$ 용액을 수지에 완전히 흡수시킨 후 일정량의 $H_2O_2$를 첨가하여 분해반응을 유도하는 방법을 적용하였다. 촉매로서 $CuSO_4,\;Cu(NO_3)_2$ 및 IRN-77 수지의 분해시 사용한 $FeSO_4$를 각각 사용하여 각 이온교환수지의 단독 및 혼합수지의 분해에 필요한 적절한 촉매와 그의 농도 및 $H_2O_2$의 소요량을 측정하였다. IRN-78 수지에 대해 $CuSO_4$ 촉매를 사용한 경우, 초기 분해반응을 유도하기 위해 $40^{\circ}C$까지 가열이 필요하였으며, 반응유도시간은 촉매의 적정온도에서 약 20분 이내 개시되는 것으로 나타났다. 동 수지에 $FeSO_4$를 사용한 경우에는 가열 없이 즉시 분해반응이 진행되었으며 분해율도 수% 높게 나타났다. 결론적으로 IRN-78 및 IRN-77과의 혼합수지의 분해를 위한 최적 촉매는 $FeSO_4$로 나타났으며 가열하지 않고 상온에서 반응유도시간 없이 각 수지를 단독으로 분해한 경우보다 적은 양의 $H_2O_2$로 완전히 액상으로 분해시킬 수 있는 좋은 결과를 얻었다. 또한 이들 각각의 수지 및 혼합수지에 대한 적절한 촉매 및 적정 농도와 완전분해에 필요한 $H_2O_2$의 양을 제시하였다.

• 한국산업융합학회 논문집
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• 제1권2호
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• pp.49-54
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• 1998

In the catalytic combustor, combustion characteristic and deterioration of catalysts were affected by non-uniformity of pre-mixed gas, Therefore, formation of uniform pre-mixed gas is one of important subjects. In this study, the effect of uniformity and non-uniformity of pre-mixed gas supplied to the catalyst was examined to clarify reaction acceleration and combustion characteristic of the catalytic combustion. It was clarified that static mixer or vaporizer tube length of about 150mm and weak swirl to a combustion air were effictive expedient to make uniform pre-mixed gas. And catalystic inlet temperature needs more than $600^{\circ}C$ with rich pre-mixed gas to active reaction.

• E2M - 전기 전자와 첨단 소재
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• 제7권6호
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• pp.496-503
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• 1994

In recent years Sol-Gel processing provides an interesting alternative method for the fabrication of ferroelectric thin layers and powder. PZT powder was prepared from an alkoxide-based solution by a Sol-Gel method. Gelation of synthesized complex solutions, microstructure, thermal analysis and crystallization behaviors of the calcined powder were studied in accordance with a water content and a catalyst. Especially gelation and crystallization behavior were analysed with the change of pH. The gelation time decreased as the pH of the mixed solution increased. For PZT powder with 650.deg. C heat treatment, 100% perovskite phase was formed by using either acidic or basic catalyst. By using either acidic or basic catalyst, we were able to get very fine powders of uniform shape with an average particle size of 0.8-1.mu.m.

• 한국수소및신에너지학회논문집
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• 제1권1호
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• pp.9-14
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• 1989

Mixed photocatalyst containing cadmium sulfide and zinc sulfide was prepared on silica gel powder and Nafion film. Photo-irradiation of aqueous mixture containing the photocatalysis generated hydrogen by water cleavage reaction. Use of sodium sulfide as sacrificial reagent help the photo-reaction. Evolution of the hydrogen was measured by gas chromatographic analysis. Composition of the catalyst was determined by atomic absorption spectrophotometer. 0.2 mL of of hydrogen was generated per hour. The maximun catalytic activity was obtained after 8-12 hours later. Hydrogen generation efficiency by the two different catalytic system was compared and showed that the Nafion-based catalyst is more efficient than the silicagel-based catalyst for the photoreaction.

• 한국대기환경학회지
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• 제6권1호
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• pp.57-72
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• 1990

The oxidation of carbon monoxide on a catalyst, $LaSrNiCoO_3$ was investigatigated with a plug flow system. Kinetic quantities such as reaction-rate, reaction order and Arhenius-parameters at various reactor temperature from 200$^\circ$C to 300$^\circ$C were determined. Also, the optimum condition for the oxidation of carbon monoxide with this catalyst was determined and are as follows. Partial pressure of oxigen ; 428mmHg Partial pressure of carbon monoxide ; 332mmHg Mixed moral ratio of oxigen and Carbon monoxide ; 1.3 : 1 Total gas flow ; 224ml/min Reaction temperature ; 340$^\circ$C The reaction kinetic equation at the optimum condition, temperature range from 200$^\circ$C to 340$^\circ$C, are as follow. $$ $v = Ae^{6.5Kcal/RT} [CO]^{0.93 \sim 0.98} [O_2]^{0.42 \sim 0.50}$ $$ In addition to this, numerical calculation were performed to evaluate the mass and heat transfer effect on this system.

• 전기학회논문지
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• 제62권6호
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• pp.782-785
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• 2013

Multi-walled carbon nanotubes were synthesized on Ni catalyst using thermal chemical vapor deposition. By introducing ammonia gas during the CNT synthesis process, clean and vertically aligned CNTs without impurities could be prepared. As the ammonia gas increased a partial pressure of hydrogen in the mixed gas during the CNT synthesis process, we could control the CNT synthesis rate appropriately. As the ammonia gas has an etching ability, amorphous carbon species covering the catalyst particles were effectively removed. Therefore catalyst particles could maintain their catalytic state actively during the synthesis process. Finally, we could obtain clean and vertically aligned CNTs by introducing $NH_3$ gas during the CNT synthesis process.

• Environmental Engineering Research
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• 제10권2호
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• pp.54-61
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• 2005

Liquid-phase catalytic degradation of waste high-density polyethylene (HDPE) over ZSM-5 (powder type (PW)) and ZSM-5+binder (granule type (GR)) has been investigated with a stirred semi-batch operation at 400°C. Two ZSM-5 catalysts with a different crystal size were synthesized and also each ZSM-5 (25%) Catalyst was mixed with a same binder (kaolin: silica sol: alumina = 55%:10%:10%). The performance of prepared catalysts that has different physicochemical properties was discussed with the cumulative amount distribution, molecular weight distribution and also paraffin, olefin, naphthene and aromatic (PONA) distribution in liquid product. These liquid product quality and distributions were changed depending on the physicochemical properties of the catalyst. Moreover, the characteristic of ZSM-5 in the catalyst was strongly influenced on the activity and PONA distribution in liquid product.

• Korean Journal of Chemical Engineering
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• 제36권2호
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• pp.191-196
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• 2019

The phase of Cu,Zn,Al precursors strongly affects the activity of their final catalysts. Herein, the Cu,Zn,Al precursor was prepared by precipitation of $Al^{3+}$ onto primitive, amorphous Cu,Zn precipitate. This precursor turned out to be a phase mixture of zincian malachite and hydrotalcite in which the latter phase was less abundant compared to the co-precipitated precursor. The final catalyst derived from this precursor exhibited a little higher copper surface area and methanol synthesis activity than the co-precipitated counterpart. Therefore, the two precursor phases need to be mixed in an adequate proportion for the preparation of active $Cu/ZnO/Al_2O_3$ catalyst.