• Transactions of the Korean hydrogen and new energy society
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• v.23 no.4
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• pp.337-345
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• 2012

To check effects of operating variables on reaction characteristics of WGS catalyst for SEWGS process, water gas shift reaction tests were carried out in a pressurized fluidized bed reactor using commercial WGS catalyst and sand(as a substitute for $CO_2$ absorbent) as bed materials. Simulated syngas(mixed with $N_2$) was used as a reactant gas. Operating temperature was $210^{\circ}C$ and operating pressure was 20 bar. WGS catalyst content, steam/CO ratio, gas velocity, and syngas concentration were considered as experimental variables. CO conversion increased as the catalyst content and steam/CO ratio increased. CO conversion at fluidized bed condition was higher than that of fixed bed condition. However, CO conversion were maintained almost same value within the fluidized bed condition. CO conversion decreased as the syngas concentration increased. The optimum operation condition was confirmed and long time water gas shift reaction test up to 24 hours at the optimum operating conditions was carried out.

• Applied Chemistry for Engineering
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• v.31 no.6
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• pp.668-673
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• 2020

In this work, ultrathin and two-dimensional (2D) cobalt hydroxide [Co(OH)2] nanosheets were synthesized by a sonication assisted liquid-phase exfoliation of bulk Co(OH)2. The resulting exfoliated Co(OH)2 is a hexagonal mono-layered nanosheet with a high specific surface area of 27.5 ㎡ g-1. The depolymerization of polyethylene terephthalate (PET) based on glycolysis reaction was also performed using an exfoliated Co(OH)2 catalyst. Excellent catalytic reaction performances were demonstrated; a high PET conversion and bis(2-hydroxyethyl) terephthalate (BHET) yield of both 100% using the nanosheet catalyst were achieved within a reaction time and temperature of 30 min and 200 ℃, respectively. The long-term stability of exfoliated Co(OH)2 catalysts was also demonstrated by recyclability tests of the catalyzed glycolysis reaction of PET over four cycles, showing both 100% of high PET conversion and BHET yield.

• Proceedings of the KAIS Fall Conference
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• 2011.12b
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• pp.379-381
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• 2011

본 논문에서는 피복아크용접(SMAW)을 자동용접으로(GMAW) 전환시키기 위한 기초 연구로서 GMA용접가스가 기공율에 미치는 영향을 보고자 한다. 기공율 평가를 위해 반자동 소방용 분기배관실험장치를 제작하였다. 분기배관의 기공율을 평가하기 위해 보호가스 3종(Ar, $CO_2$, 8:2 혼합가스), 전압을 변수로 설정하여 GMA용접을 실시하였다. 용접을 실시한 시편을 용접방향으로 절단하여 기공율 평가를 실시하였다.

• Korean Chemical Engineering Research
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• v.44 no.4
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• pp.356-362
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• 2006

The $SO_2$ reduction using CO and $H_2$ over Sn-Zr based catalysts was performed in this study. Sn-Zr based catalysts with Sn/Zr molar ratio (0/1, 1/4, 1/1, 2/1, 3/1, 1/0) were prepared by the precipitation and co-precipitation method. The effect of the temperature on the reaction characteristics of the $SO_2$ reduction with a reducing agent such as $H_2$ and CO was investigated under the conditions of space velocity of $10,000ml/g_{-cat.}h$, $([CO(or\;H_2)]/[SO_2])$ of 2.0. As a result, the activity of Sn-Zr based catalysts were higher than $SnO_2$ and $ZrO_2$. The reactivity for the $SO_2$ reduction with CO was higher than that with $H_2$, and sulfur yield in the $SO_2$ reduction by $H_2$ was higher than that by CO. The reactivity for the $SO_2$ reduction with $H_2$ was increased with the reaction temperature regardless of Sn-Zr based catalyst with a Sn/Zr molar ratio. $SnO_2-ZrO_2$ (Sn/Zr=1/4) had highest activity at $550^{\circ}C$, in the $SO_2$ reduction with $H_2$ and $SO_2$ conversion of 94.4％ and sulfur yield of 66.4％ were obtained at $550^{\circ}C$. On the other hand, in the $SO_2$ reduction by CO, the reactivity was decreased with the increase over $325^{\circ}C$. At the optimal temperature of $325^{\circ}C$, $SO_2$ conversion and sulfur yield were about 100％ and 99.5％, respectively, in the $SO_2$ reduction over $SnO_2-ZrO_2$ (Sn/Zr=3/1). Also, the $SO_2$ reduction using syngas with $CO/H_2$ ratio over $SnO_2-ZrO_2$ (Sn/Zr=2/1) was performed in order to investigate the application possibility of the simulated coal gas as the reductant in DSRP. As a result, the reactivity of the $SO_2$ reduction using syngas with $CO/H_2$ ratio was increased with increasing the CO content of syngas. Therefore, it could be known that DSRP using the simulated coal gas over Sn-Zr based catalyst is possible to be realized in IGCC system

• 한국신재생에너지학회:학술대회논문집
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• 2011.05a
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• pp.146.1-146.1
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• 2011

석탄가스화복합발전(IGCC)공정에서 가스화기를 거쳐 생성된 합성가스로부터 $CO_2$를 효과적으로 분리/회수하기 위해 가스 고형화법을 제안하였다. 가스 하이드레이트 형성과정에서의 반응특성을 살펴보기 위하여 반응시간에 따른 가스소모량과 기상의 $CO_2$ 조성 변화를 측정하였다. 순수계와 촉진제 첨가계 (TBAB (10, 40 wt%), TBAF (10, 34 wt%), THF (4, 19 wt%))에 대하여 하이드레이트 생성 후의 기상과 하이드레이트상의 $CO_2$ 조성을 측정하였으며, 그 결과 하이드레이트 형성법에 의해 고농도의 $CO_2$가 하이드레이트상에 포집되는 것을 확인하였다. 가스 소모량 측정실험에서는 THF 19.1 wt%를 첨가하였을 때 가장 큰 소모량을 보였으며, TBAF 10 wt%를 첨가하였을 때 가장 적은 가스소모량을 보였다. $CO_2$ 조성 변화 실험에서는 가스 소모량 실험과 마찬가지로 THF 19.1 wt%를 첨가하였을 때 가장 큰 조성변화를 보였다. 이는 THF의 첨가로 인하여 가스 하이드레이트로의 전환율 증가로 많은 양의 $CO_2$ 기체가 하이드레이트 상에 포집되었음을 나타낸다. 속도론적인 측면에서는 모든 실험조건에서 하이드레이트 형성반응이 1시간 이내에 대부분 종결되는 것을 볼 수 있었다. 또한 $^1H$-NMR을 통하여 혼합가스 하이드레이트의 구조적인 분석을 진행하였다. 본 실험에서 얻어진 결과는 가스 하이드레이트 형성법을 이용한 합성가스 분리 공정 개발에 중요한 기초자료가 될 것으로 사료된다.

• 한국신재생에너지학회:학술대회논문집
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• 2011.11a
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• pp.121.2-121.2
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• 2011

석탄가스화복합발전과 연계하여 사용할 수 있는 $CO_2$분리법으로 연소 전 탈탄소화는 연료가 연소되기 전에 $CO_2$를 회수하는 방법으로 현재 여러가지 분리법이 사용되고 있다. 본 연구에서는 가스 하이드레이트의 다양한 응용 분야 중 이산화탄소 격리분야에서 합성가스로부터 $CO_2$롤 효과적으로 분리/회수하기 위하여 가스 고형화법에 관한 연구를 진행하였다. 가스 하이드레이트 형성과정에서의 반응 특성을 살펴보기 위하여 순수계와 촉진제 첨가계(TBAB, TBAF, THF)에 대하여 반응시간에 따른 가스소모량 및 기상의 $CO_2$ 조성 변화를 측정하였다. 그 결과 하이드레이트 상에 고농도의 $CO_2$가 포집되는 것을 확인 할 수 있었다. 순수계와 THF 첨가계의 경우 가스 소모량이 다른 계에 비하여 높게 나타났다. 이는 순수계의 경우 구조-I의 큰 동공과 작은 동공에 모두 기체가 점유되기 때문이며, THF 첨가계의 경우 구조-II의 큰 동공에만 기체가 점유되지만 THF의 첨가로 인해 전환율이 증가되기 때문이다. 반면, TBAF와 TBAB 첨가계의 경우에는 상재적으로 낮은 가스 소모량을 보였다. 기체 소모량이 큰 경우 최종 기상의 $CO_2$ 조성이 낮게 나타났다. 그리고 모든 실험조건에서 1시간 이내에 하이드레이트 형성반응이 종결되는 것을 확인할 수 있었다. 또한, 촉진제 첨가에 의한 하이드레이트의 구조적인 변화를 확인하기 위하여 Raman 분광법과 $^1H$-NMR을 이용하여 혼합가스 하이드레이트를 분석하였다. 본 실험으로 얻어진 결과는 가스 고형화법을 이용한 합성가스 분리 공정 설계 및 개발에 중요한 기초자료가 될 것으로 사료된다.

• Applied Chemistry for Engineering
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• v.8 no.4
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• pp.685-693
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• 1997

We have studied the reforming of carbon dioxide with methane over various supported nickel catalysts. The nickel supported on natural zeolite showed the highest activity and the nickel on acidic support showed higher activity and slow deactivation compared to nickel on basic support. The activity of nickel on natural zeolite increased with increasing loading ratio and showed almost constant activity above 10wt.% loading of nickel. The conversion and yield of products were affected by the mole ratio of reactants and the highest yields of CO and $H_2$ were obtained at $CH_4/CO_2=1$. The deactivation of catalyst was caused by deposition of coke which was formed by the decomposition of methane. The shape of coke was shown to be whisker tripe carbon, and it brought out the slow deactivation of catalyst.

• Clean Technology
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• v.17 no.2
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• pp.166-174
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• 2011

The xAl-yCe oxide catalysts with different mol ratios of Al/(Al+Ce) were prepared by a co-precipitation method and Pt supported on xAl-yCe oxide catalysts were synthesized by an incipient wetness impregnation method. The catalysts were characterized by X-ray Diffraction (XRD), $N_2$ sorption, and $H_2$/CO-temperature programmed reduction ($H_2$/CO-TPR) to correlate with catalytic activities in co oxidation. Among the catalysts studied here, Pt/1Al-9Ce oxide catalyst showed the highest activity in dry and wet reaction conditions and the catalytic activity showed a typical volcano-shape curve with respect to Al/(Al+Ce) mol ratio. When the presence of 5% water vapor in the feed, the temperature of $T_{50%}$ was shifted ca. $30^{\circ}C$ to lower temperature region than that in dry condition. From CO-TPR, the desorption peak of $CO_2$ on Pt/1Al-9Ce oxide catalyst showed the highest value and well correlated the catalytic performance. It indicates that the Pt/1Al-9Ce oxide catalyst has a large amount of active sites which can be adsorbed by co and easy to supplies the needed oxygen. In addition, the amount of pentacoordinated $Al^{3+}$ sites obtained through $^{27}Al$ NMR analysis is well correlated the catalytic performance.

• Korean Journal of Plant Tissue Culture
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• v.22 no.6
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• pp.329-334
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• 1995

Transformation system of rolC gene, dwarf gene in Lycium chinenese Mill. established by using system. Pin-punctured leaves induced numerous adventious buds in abaxial side when cultured on 3/2 MS medium containing 2.0 mg/L zeatin. Survival rate and shoot regeneration frequency of leaf explants decreased as kanamycin sulfate level increased. Shoot buds were not regenerated on 3/2 MS medium containing 10 mg/L kanamycin sulfate and 2.0 mg/L zeaein. Of the level tested, 10 mg/L of kanamycin sulfate was optimum in selection of kanamycin sulfate resistant plant. Co-culture time of bacteria and leaf explants was affected at the frequency of shoot regeneration and survival of leaf explants. Leaf explants co-cultivated during above 48hr severely decreased survival rate and shooting rate. Best result on survival rate and shooting rate were obtained when exposed for 24 h. 80 explants of 105 leaf explants survived on 3/2 MS medium containing 2.0 mg/L zeatin and 10 mg/L kanamycin sulfate, and 15 shoots was regenerated on the same medium. To select kanamycin sulfate resistant plant, regenerate as cultured on 3/2 MS medium containing 10 mg/L kanamycin sulfate, and obtained 5 kanamycin resistant plants. Southern blot analysis conformed that the rolC gene was incorporated into the genomic DNA of kanamycin resistant plants.

• Clean Technology
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• v.20 no.3
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• pp.218-225
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• 2014

Catalytic gasification of raw coals at mild condition is not realized yet mainly due to deactivation of catalysts via their irreversible interaction with mineral matters in coal. In this work, the gasification behavior of ash-free coal (AFC) was compared with that of the parent raw coal. In order to modify the gasification conditions, the raw coal gasified with fixed variables (water supply, space velocity, temperature, catalysts) in a fixed bed reactor. When catalysts are added by physical mixing method with coal, $K_2CO_3$ was the most effective additives for steam gasification of coal. However, the activity of ash-free coal (AFC) was much less reactive than raw coal due to high temperature extraction in a 1-methylnaphthalene under 30bar at $370^{\circ}C$ for 1 h, almost removed oxygen functional groups, and increased carbonization. The addition of $K_2CO_3$ in AFC achieved higher conversion rate at low temperature ($700^{\circ}C$). At that time, the molar ratio of gases ($H_2/CO$ and $CO_2/CO$) was increased because of water-gas shift reaction (WGSR) by addition of catalysts. This shows that catalytic steam gasification of AFCs is achievable for economic improvement of gasification process at mild temperature.