• Journal of the Korean Chemical Society
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• v.29 no.2
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• pp.129-136
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• 1985

In the atomic absorption spectrometry using an air-acetylene flame, the interferences of Zr, Sn, Al, Sb, $SO_4^{2-},\;VO_3^-,\;and\;SiO_3^{2-}$, on the calcium absorption and the repression of this interference by the addition of cerium have been studied. The interference by Zr, Sn, Al, Sb, $SO_4^{2-},\;VO_3^-,\;and\;SiO_3^{2-}$ existed as the same concentration as calciurn ($3.0 {\times} 10^{-4}$M) in the sample solution are completely released by the addition of cerium twice as much as interfering cation. The interferences by the mixed interfering cations (Zr, Sn, Al and Sb) and by the mixed interfering anions ($SO_4^{2-},\;VO_3^-,\;and\;SiO_3^{2-}$) are larger than by each interfering cation and anion, and the releasing effect by cerium ($1.5 {\times} 10^{-2}$M) is effective up to some degree of the concentration of mixed interfering cations and of mixed interfering anions. The releasing effect by cerium to the mixed solution of interfering cations and anions is applicable to quite wide range of concentration.

• Proceedings of the Korean Radioactive Waste Society Conference
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• 2004.06a
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• pp.338-338
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• 2004

건식공정 (pyrochemical process 혹은 pyroprocessing)은장수명핵종의 소멸처리를 위해서는 장수명핵종을 분리한 뒤 연료로 제조하여야 하며, 분리 공정은 습식공정과 건식공정으로 크게 나누어진다. 용융염을 사용하는 습식공정에 비해 2차 방사성폐기물의 발생량이 적고 공정이 간단하고, 핵확산에 대한 저항성이 매우 크다는 장점 때문에 미래의 핵주기 기술로서 주목받고 있다. 소멸처리를 위해서는 사용 후 핵연료 내에 존재하는 장수명 핵종군 원소들을 분리하고 소멸처리용 연료에 적합한 형태의 물리 화학적 형태로 전환시켜야 한다.(중략)

• Proceedings of the Korean Institute of Resources Recycling Conference
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• 2005.10a
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• pp.266-270
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• 2005

본 연구는 Ta, Nb, Zr, 및 희토류 등을 복합적으로 함유한 복합광을 대상으로 사염화탄소에 의한 염화반응을 알아보기 위한 기초연구로서 각 산화물의 염화반응 특성을 알아보고 이를 토대로 복합광의 염화반응을 비교하여 보았다. 실험결과 산화물 상태의 Nb, Ta 및 Zr은 비교적 낮은 온도에서 염화반응이 일어나고 염화물이 휘발됨을 알 수 있었다. 복합광을 반응 온도 $400^{\circ}C,\;CCl_4$ 분압 0.28 일때 반응시간이 10분에서 60분으로 변함에 따라 니오븀 및 탄탈륨은 $91%{\sim}99%$의 높은 회수율을 나타내었으나 지르코늄은 각각 16.5%에서 27.5%로 약간 증가하는 경향을 나타내었다. 희토류의 경우 세륨은 반응율이 71.7에서 73% 정도였고 란타늄은 51%에서 54% 정도의 반응율을 나타내었다.

• Nuclear Engineering and Technology
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• v.13 no.4
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• pp.254-263
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• 1981

Paper electrophoretic separation of fission products has been carried out by using the specially designed migration apparatus. In general, the isolation of rubidium, strontium, zirconium, ruthenium, cesium, cerium, molybdenum, and some short-lived fission products is more efficient under 0.1M HCl electrolyte as compared with 0.1M NaOH electrolyte. In addition to Np-239, 1-131∼135 were, in particular, observed with different iodine chemical species obtained by the paper-electrophoretic separation of short, neutron-irradiated uranyl nitrate solution.

• Transactions of the Korean hydrogen and new energy society
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• v.14 no.1
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• pp.1-7
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• 2003

In this study, activity changes of $Ni/Ce-ZrO_2$ catalyst for steam reforming reaction in the various steam treatment condition were investigated and BET, XRD and XPS analysis were introduced to characterize the catalyst before and after treatment. Activity test showed that $Ni/Ce-ZrO_2$ catalyst had good activity after reduction in steam reforming reaction but deactivated rapidly after steam treatment at high temperature. Activities of deactivated catalyst by steam was recovered to die previous activity level after reduction using hydrogen rich gas. It was observed that catalytic activity was preserved after repeated steam treatment, too. It showed that change of catalytic activity due to steam treatment is perfectly reversible. From the BET, XRD and XPS analysis, deactivation of $Ni/Ce-ZrO_2$ catalyst was due to the transition from Ni, that is activity site for steam reforming reaction, to $NiAl_2O_4$ in steam treatment at high temperature.

• Transactions of the Korean hydrogen and new energy society
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• v.22 no.4
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• pp.415-423
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• 2011

HI decomposition step certainly demand catalytic reaction for efficient production of hydrogen in SI process. Platinum catalyst can apply to HI decomposition reaction as well as hydrogenation or dehydrogenation. Generally, noble metal is used as catalyst which is loaded form for getting high dispersion and wide active area. In this study, Pt was loaded onto zirconia, ceria, alumina, and silica by impregnation method. HI decomposition reaction was carried out under the condition of $450^{\circ}C$, 1atm, and $167.76h^{-1}$ (WHSV) in a fixed bed reactor for measuring catalytic activity. And property of a catalyst was observed by BET, TEM, XRD and chemisoption analysis. On the basis of experimental results, we discussed about conversion of HI according to physical properties of the loaded Pt catalyst onto each support.