• 한국수소및신에너지학회논문집
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• 제14권1호
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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.

• 한국통신학회논문지
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• 제17권1호
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• pp.90-97
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• 1992

이 논문은 전송선로의 진폭과 위상응답을 선로의 입력측에서 추정하는 방법에 대해서 논의하고 협대역 ISDN 가입자 선로의 경우에 적용한 것이다. 활성과 비활성 상태의 표준 단말 임피던스와 선로의 입력측에서 추정할 수 있는 입력 임피던스로부터 선로의 ABCD 파라메터를 구할 수 있는 계산식을 유도한다. 입력 임피던스함수 추정을 위해 "chirp" 신호를 입자 전압신호로 사용하며, 이때 잡음의 영향은 앙상블 평균을 취하여 감소 시킨다. 이러한 ABCD 파라메터 추정 방법은 균일선로와 복합선로에 동일하게 적용될 수 있으며, 추정된 결과로부터 진폭 및 위상응답을 구할 수 있다. 협대역 ISDN 가입자 선로의 모델을 결정하여 모의실험한 결과를 제시하며 단말 임피던스의 편차에 의한 추정오차를 분석하였다.

• Bulletin of the Korean Chemical Society
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• 제24권1호
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• pp.86-90
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• 2003

Reverse-Water-Gas-Shift reaction (RWGSR) was carried out over the ZnO, $Al_2O_3,\;and\;ZnO/Al_2O_3$ catalysts at the temperature range from 400 to 700 ℃. The ZnO showed good specific reaction activity but this catalyst was deactivated. All the catalysts except the $ZnO/Al_2O_3$ catalyst (850 ℃) showed low stability for the RWGSR and was deactivated at the reaction temperature of 600 ℃. The $ZnO/Al_2O_3$ catalyst calcined at 850 ℃ was stable during 210 hrs under the reaction conditions of 600 ℃ and 150,000 GHSV, showing CO selectivity of 100% even at the pressure of 5 atm. The high stability of the $ZnO/Al_2O_3$ catalyst (850 ℃) was attributed to the prevention of ZnO reduction by the formation of $ZnAl_2O_4$ spinel structure. The spinel structure of $ZnAl_2O_4$ phase in the $ZnO/Al_2O_3$ catalyst calcined at 850 ℃ was confirmed by XRD and electron diffraction.

• 대한환경공학회지
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• 제34권10호
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• pp.664-670
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• 2012

상용 중유 발전소 배가스에 장기간 노출되어 활성이 현저히 저하된 탈질 SCR 폐촉매를 대상으로 현장 시스템을 모사하여 증류수 및 산성용액에 의한 세척과정을 거쳐 모사된 현장 조건으로 촉매를 재생하였다. 산성용액의 제조조건 및 처리조건에 따른 촉매의 물성변화를 확인하였고 질소산화물($NO_x$) 전환 촉매 활성 실험을 수행하여 촉매성능 변화를 고찰하였다. 촉매의 특성분석은 BET, Porosimeter, EDX (Energy Dispersive X-ray spectrometer), ICP (Inductively Coupled Plasma) 등을 이용하여 수행하였고, $NO_x$ 전환 반응실험은 중유 발전소 배가스를 모사하여 마이크로 반응기에서 SCR 반응을 수행하였다. 촉매특성 분석결과 재생된 촉매의 경우 비표면적은 신품 촉매 대비 95% 이상 회복되었고, $NO_x$ 전환활성은 산성용액 농도 3~6 M 범위에서 신품 촉매 대비 90% 이상을 회복한 것으로 나타났다. 이러한 촉매활성의 향상은 산성용액에 의한 촉매표면의 불순물들이 제거되면서 일어난 결과로 밝혀졌다.

• Bulletin of the Korean Chemical Society
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• 제23권6호
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• pp.803-807
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• 2002

The conversion of dimethyl ether(DME) has been carried out over $\gamma-alumina$, silica-alumina, and modified $\gamma-aluminal$ catalysts. Especially, the water effect has been investigated on purpose to develop a suitable catalyst for one-step synthesis of DME from $CO_2$ hydrgenation, The $\gamma-Al_2O_3$ modified with 1 wt% silica is more active and less deactivated by water than unmodified one. $CO_2has$ no effect on catalytic dehydration of methanol to DME.

• 공업화학
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• 제21권1호
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• pp.104-110
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• 2010

국내에서 가동 중인 석탄, 오리멀젼, LNG 등의 화력발전소에서 선택적 촉매 환원(SCR) 공정에 사용되고 있는 촉매의 재생을 연구하기 위하여 이들 촉매의 활성 저하를 고찰하였다. XRD, ICP-AES, BET, SEM 분석 등으로 촉매의 특성분석을 수행하였고 이들 촉매에 대하여 암모니아 SCR을 행하였다. 석탄 화력발전소의 SCR 촉매는 연료 성분과 관련된 황산염과 분진의 침적에 의한 기공 폐색에 기인하여 활성저하가 발생하였다. 오리멀젼 화력발전소의 SCR 촉매는 연료에 함유된 바나듐과 황 성분 그리고 연료에 첨가된 마그네슘 화합물의 침적에 의한 기공 폐색에 기인하여 촉매 표면적이 크게 감소하였다. 그러나 촉매의 암모니아 SCR 활성은 약간 감소하였다. LNG 화력발전소의 SCR 촉매는 사용 기간이 2년 이상임에도 불구하고 활성저하는 거의 일어나지 않았다.

• KSII Transactions on Internet and Information Systems (TIIS)
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• 제7권1호
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• pp.81-98
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• 2013

Since Probabilistic Latent Semantic Analysis (PLSA) and Latent Dirichlet Allocation (LDA) were introduced, many revised or extended topic models have appeared. Due to the intractable likelihood of these models, training any topic model requires to use some approximation algorithm such as variational approximation, Laplace approximation, or Markov chain Monte Carlo (MCMC). Although these approximation algorithms perform well, training a topic model is still computationally expensive given the large amount of data it requires. In this paper, we propose a new method, called non-simultaneous sampling deactivation, for efficient approximation of parameters in a topic model. While each random variable is normally sampled or obtained by a single predefined burn-in period in the traditional approximation algorithms, our new method is based on the observation that the random variable nodes in one topic model have all different periods of convergence. During the iterative approximation process, the proposed method allows each random variable node to be terminated or deactivated when it is converged. Therefore, compared to the traditional approximation ways in which usually every node is deactivated concurrently, the proposed method achieves the inference efficiency in terms of time and memory. We do not propose a new approximation algorithm, but a new process applicable to the existing approximation algorithms. Through experiments, we show the time and memory efficiency of the method, and discuss about the tradeoff between the efficiency of the approximation process and the parameter consistency.

• 공업화학
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• 제9권1호
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• pp.121-128
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• 1998

삼중수소를 함유하는 수소동위원소 시설의 운용이나 취급 또는 핵융합소재의 관리기술분야에서는 기체크로마토그래피 분리법이 중요한 분석 및 농축기술중의 하나로 활용되고 있다. 수소, 중수소 및 삼중수소의 수소동위원소 혼합기체시료를 상용 기체크로마토그래피를 사용하여 분리하였다. 기체시료는 특별히 제작된 진공-시료주입장치를 통해 액체질소온도의 분위기로 유지된 분리컬럼을 통과하는 비활성 캐리어 기체의 흐름을 주입하였다. 10% 함량의 염화망간으로 부분-비활성화한 산화알루미늄 고정상에서 수소동위원소들이 완전히 분리됨을 확인할 수 있었다. 그리고 이성질체피크의 억제와 분리 용리시간이 단축되어 실제 수소동위원소의 분리 및 농축기술에 유용하게 적용할 수 있는 비교적 우수한 분리조건을 얻었다.

• BMB Reports
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• 제28권3호
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• pp.254-260
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• 1995

Cytochrome oxidase was purified from bovine-heart mitochondria and its enzymatic properties were examined. The purified cytochrome oxidase was identified by its absorption spectrum and chromatogram through gel filtration. The specific activity, purification degree and yield of purified cytochrome oxidase were 18 nmol/mg/ml/min, 24.83 fold and 0.93%, respectively. The activity of the enzyme assayed by a ferrocytochrome $c-O_2$ system was optimized at $25^{\circ}C$ and pH 6.5. Examining the effect of nonionic detergents established that cytochrome oxidase was deactivated by Triton X-100. The oxidase was activated by Tween 80 and deactivated by Tween 20. The Michaelis constant and maximum velocity of the oxidase for ferrocytochrome c were 0.032~0.044 mM and 0.019~0.021 mM/min, respectively. After adaption to basal diet for a week, experimental diets containing 6 mg Cu/kg, or zero mg Cu/kg, or 12 mg Cu/kg were fed to a control group, a copper-free group and a copper-rich group of Sprague-Dawley rats, respectively, for 4 weeks. The specific activities assayed for the ferrocytochrome $c-O_2$ system of isolated cytochrome oxidase from the rat liver of control, copper-free, and copper-rich group were 1.00, 1.19, and 0.878 nmol/mg/ml/min, respectively. Their degrees of purification were 11.38, 10.82 and 8.78 fold, respectively. The specific activities for liver and heart mitochondrial cytochrome oxidase of copper-free/copper-rich groups assayed using the ferrocytochrome $c-O_2$ system were 81.4% and 96.4%/64.1% and 61.1%, respectively, compared with those of the control.

• 한국수소및신에너지학회논문집
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• 제1권1호
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• pp.15-23
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• 1989

The selective separation of hydrogen from gas mixture containing hydrogen was experimentally studied using $LaNi_5$. The capacity and the rate of hydrogen separation, the purity of recovered hydrogen and the optimum condition of the regeneration of deactivated $LaNi_5$ were investigated. The separation rate and the recovery ratio of hydrogen were slowly decreased with the increase of the number of hydrogen absorption cycle. It was found that this result comes from the deactivation of $LaNi_5$ partly because of the blocking of hydrocarbon compounds in the $LaNi_5$ lattice and partly because of the poisoning of $LaNi_5$ surface by carbon monoxide contained in the gas mixture. The optimum condition for the regeneration of deactivated $LaNi_5$ was obtained by heating in a vacuum to about 637 K. The recovery ratio of hydrogen at the optimum condition was observed to be about 80%. The rates of hydrogen separation were measured in the ${\alpha}$-phase and two phase regions. The rate equations could be expressed as follows ; ${\alpha}$ - phase : $$-\frac{dP{_{H_2}}}{dt}=9.836{\times}10^{-3}(P{_{H_2}}_{-P_{eq}})$$ two phase region : $$-\frac{dP_{H{_2}}}{dt}=1.6909{\times}10^2\exp(-17560/RT)(P{_{H_2}}_{-P_{eq}})$$.