• 한국대기환경학회지
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• 제15권3호
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• pp.249-255
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• 1999

We sdudied effect of additives on catalytic activity in thermal catalytic de-NOx process which was composed of thermal reduction, catalytic reduction and catalytic oxidation stage. Pd-Pt/${\gamma}$-$Al_2O_3$ catalysts with the addition of transition metals(Co, Cu, Fe, Ni, W, Zn, Zr) and rare earth metals(Ce, Sr) were prepared by the conventional washcoating method. Those catalysts were characterized by CO pulse chemisorption, ICP, $N_2$ adsorption, SEM and XRD. The effect of catalyst additives on NOx removal for diesel emission was studied in thermal catalytic de-NOx process at reduction temperature(350~50$0^{\circ}C$), space velocity(5,000~20,000 $hr^{-1}$) and the engine load(0~120kW). The concentraton of CO, $CO_2$, NO and $NO_2$ in the exhaust gas increased with the engine load. On the other hand the concentration of $O_2$ decreased. The de-NOx activityof all prepared catalysts increased with respect to high CO and low $O_2$ level in the thermal reduction stage of the process. Insertion of Ce to Pt-Pd/${\gamma}$-$Al_2O_3$ catalyst showed the best activity of all the catalysts under these experimental conditions. De-NOx catalysts are effective to remove CO in addition to NOx in the catalytic reduction stage.

• 한국수소및신에너지학회논문집
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• 제25권2호
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• pp.105-113
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• 2014

Performance tests on $Ni/Ce-ZrO_2/Al_2O_3$ catalysts with additives (MgO, $La_2O_3$) were investigated in the combined reforming processes (SCR, ATR, TRM) in order to produce hydrogen and carbon monoxide (it is called "syngas".). The catalyst characterization was conducted using the BET surface analyzer, X-ray diffraction (XRD), SEM, TPR and TGA. The combined reforming process was developed to adjust the syngas ratio depending on the synthetic fuel (methanol, DME and GTL) manufacturing processes. Ni-based catalysts supported on alumina has been generally recommended as a combined reforming reaction catalyst. It was found that both free NiO and complexed NiO species were responsible for the catalytic activity in the combined reforming of methane conversion, and the $Ce-ZrO_2$ binary support employed had improved the oxygen storage capacity and thermal stability. The additives, MgO and $La_2O_3$, also seemed to play an important role to prevent the formation of the carbon deposition over the catalysts. The experimental results were compared with the equilibrium data using a commercial simulation tool (PRO/II).

• 한국수소및신에너지학회논문집
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• 제25권6호
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• pp.570-576
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• 2014

LFG (Land-Fill Gas) includes components of $CH_4$, $CO_2$, $O_2$, $N_2$, and water. The preparation of synthesis gas from LFG as a DME (Dimethyl Ether) feedstock was studied by methane reforming of $CO_2$, $O_2$ and steam over NiO-MgO-$CeO_2$/$Al_2O_3$ catalyst. Our experiments were performed to investigate the effects of methane conversion and syngas ratio on the amount of LFG components over NiO-MgO-$CeO_2$/$Al_2O_3$ catalyst. Results were obtained through the activity reaction experiments at the temperature of $900^{\circ}C$ and GHSV of 4,000. The results were as following; it has generally shown that methane conversion rate increased with the increase of oxygen and carbon dioxide amounts. Highly methane conversion of 92~93% and syngas ratio of approximately 1.0 were obtained in the feed of gas composition flow-rate of 243ml/min of $CH_4$, 241ml/min of $CO_2$, 195ml/min of $O_2$, 48ml/min of $N_2$, and 360ml/min of water, respectively, under reactor pressure of 15 bar for 50 hrs of reaction time. Also, it was shown that catalyst deactivation by coke formation was reduced by excessively adding oxygen and steam as an oxidizer of the methane reforming.

• Korean Chemical Engineering Research
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• 제51권1호
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• pp.47-52
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• 2013

본 연구는 $Ni/Ce_xZr_{1-x}O_2$ 촉매를 이용하여 프로판의 자열개질반응을 통한 수소제조에 관한 것이다. $Ni/Ce_xZr_{1-x}O_2$ 촉매는 용매로서 물을 사용한 방법(CZ-W), 우레아와 물을 사용한 방법(CZ-UW), 우레아, 에탄올 및 물을 사용한 방법(CZ-UWA)으로 각각 제조하였다. 반응물질의 조성은 $Steam/C_3H_8$=3, $C_3H_8/O_2$=2.70 이었고, 반응은 상압 고정층 유통식 반응기에서 $300{\sim}700^{\circ}C$ 온도범위에서 진행하였다. 촉매제조시 용매에 우레아 및 에탄올을 첨가할 경우 촉매의 활성이 증가하였다. CZ-UW 촉매의 경우 클러스터형태의 탄소생성에 기인한 활성점 피막으로 인해 쉽게 비활성화가 초래됐다. 하지만 CZ-UWA 촉매의 경우 반응 후 탄소가 활성에 영향을 미치지 않는 나노파이버형태로 존재하여 활성저하가 발생되지 않음을 SEM을 통해 확인했다. 또한 $Ni/Ce_{0.75}Zr_{0.25}O_2$ 촉매의 전환율 및 수율이 더 좋게 나타났으며 또한 소량의 Cobalt를 첨가했을 때 탄소에 대한 저항성이 크게 향상됨을 TGA로 확인하였다.

• Bulletin of the Korean Chemical Society
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• 제17권9호
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• pp.790-793
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• 1996

The azacrown compound, 1,7-dioxa-4,10,13-triazacyclopentadecane-N,N',N"-tri(methyl-acetic acid)(N3O2-tri(methylacetic acid)) was synthesized by modified procedure of Krespan. Potentiometric method has been used to determine the protonation constants of N3O2-tri(methylacetic acid) and stability constants of complexes on the divalent transition metal ions (Co2+, Ni2+, Cu2+, and Zn2+) and trivalent metal ions (Ce3+, Eu3+, Gd3+, and Yb3+) with N3O2-tri(methylacetic acid). The stability constants for the complexes of the divalent transition metal ions studied in the present work with N3O2-tri(methylacetic acid) were 11.4 for Co2+, 11.63 for Ni2+, 13.51 for Cu2+, and 11.65 for Zn2+, respectively. Thus, the order of the stability constants for complexes on the transition metal ions with N3O2-tri(methylacetic acid) was shown Co2+ < Ni2+ < Cu2+ > Zn2+ as same as the order of Irving-Williams series. The stability constants of Ce3+, Eu3+, Gd3+, and Yb3+ trivalent lanthanide metal ion complexes of N3O2-tri(methylacetic acid) were, respectively, 11.26 for Ce3+, 11.56 for Eu3+, 11.49 for Gd3+, and 11.80 for Yb3+. The values of the stability constants on trivalent metal ions with the ligand are increasing according to increase atomic number, due to increase acidity. But the value of stability constant of Gd3+ ion is less than the value of Eu3+ ion. This disordered behavior is also reported by Moeller.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2010년도 하계학술대회 논문집
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• pp.214-214
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• 2010

The 0.65Pb($Mg_{1/3}Nb_{2/3})O_3-0.35PbTiO_3$ (PMN-PT) thin films with $La_{0.5}Sr_{0.5}CoO_{3-\delta}$ (LSCO) bottom electrodes were grown on $CeO_2$/YSZ/Si(001), Pt/$TiO_2$/Si and $SrTiO_3$ (STO) substrates using conventional pulsed laser deposition (PLD) at a substrate temperature of $550^{\circ}C$. Since generally the crystallographic orientation of the bottom electrode induces the orientation of the films deposited on it, it allows us to observe the influence of the PMN-PT film orientation on the electrical properties. Phi scan done on PMN-PT/LSCO thin films shows epitaxial behavior of the films grown on sto substrates and $CeO_2$/YSZ buffered Si(001) substrates, and (110) texture on Pt/$TiO_2$/Si substrates. Polarization-electricfield (P-E) measurement shows good hysteresis behavior of PMN-PT films with remnant polarization of 18.2, 8.8, and $4.4{\mu}C/cm^2$ on $CeO_2$/YSZ/Si, Pt/TiO2/Si and STO substrates respectively.

• 한국수소및신에너지학회논문집
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• 제26권3호
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• pp.221-226
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• 2015

Ru catalysts supported on $CeO_2$ were synthesized by an impregnation method and characterized by numerous analytical techniques including X-ray diffraction (XRD), Brunauer-Emmett-Teller (BET), transmission electron microscopy (TEM), and scanning electron microscopy-energy dispersive X-ray spectroscopy (SEM-EDS). Upon utilization of these catalysts for methane dry reforming with a $CH_4/CO_2$ ratio of 1:1 at different temperatures ranging from 550 to $750^{\circ}C$, the $Ru/CeO_2$ catalysts have shown to be active. In particular, Ru(0.55wt%) supported on $CeO_2$ (1) prepared by a hydrothermal method exhibited excellent activity with the conversion of > 75% at $750^{\circ}C$. In addition, the catalyst also proved to be highly stable for at least 47 h without catalyst deactivation under the dry reforming conditions.

• 방사성폐기물학회지
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• 제8권3호
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• pp.181-188
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• 2010

레이저 용발법에 의한 금속 표면 제염특성을 평가하였다. 레이저로는 파장 532 nm, 펄스에너지 150 mJ, 펄스폭 5 ns의 큐스위치 Nd:YAG를 적용하였고, 금속 표면에 $CsNO_3$, $Co(NH_4)_2(SO_4)_2$, $Eu_2O_3$ 그리고 $CeO_2$를 오염시켜 이들의 제염 특성을 평가하였다. 제염 변수로는 레이저 적용횟수, 레이저 에너지 밀도 및 레이저 조사 각도 특성을 평가하였으며 각각 8, 13.3 J/$cm^2$ 및 $30^{\circ}$의 최적 조건을 확인하였다. 제염 효율은 오염성분의 비점과 관련이 있었으며 $CsNO_3>Co(NH_4)_2(SO_4)_2>Eu_2O_3>CeO_2$ 순이었다. 또한 여러 에너지 밀도 조건에서 스테인레스 스틸 재질의 식각 깊이 제어 특성을 규명하였다.

• 자원리싸이클링
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• 제17권6호
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• pp.10-16
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• 2008

본 연구는 염화세륨 수용액으로부터 중탄산암모늄의 첨가에 의한 탄산세륨 합성시, 반응 조건(염화세륨 농도: 0.5-2M, 반응온도: $20-60^{\circ}C$)에 따라 형성되는 탄산세륨 결정에 대하여 고찰하였다. 반응성 결정화 과정에서 반응물의 농도 및 반응온도에 따라 lanthanite 형태의 결정상[$Ce_2(CO_3)_3{\cdot}8H_2O$]과 tengerite 형태의 결정상[$Ce_2(CO_3)_3{\cdot}2.5H_2O$] 등 두 형태의 탄산세륨 결정을 얻을 수 있었다. 염화세륨의 농도와 반응온도가 증가함에 따라 탄산세륨의 결정상은 lanthanite에서 tengerite형태로 변하였으며, 함수의 탄산세륨은 건조 조건에 따라 무수의 수산기가 함유된 탄산세륨의 결정상 구조로 전이되었다. Lanthanite와 tengerite 구조의 탄산세륨은 판상의 결정립들이 서로 간에 응집된 상태로서 크기나 형태가 두 결정상 모두 같은 형상을 가지며, 결정립의 크기는 lanthanite구조가 약 $3{\mu}m$, tengerite구조가 약 $5{\mu}m$이었다. 그러나 수산기가 함유된 탄산세륨[$Ce(OH)(CO_3)$]은 침상의 결정립이 응집되어 있는 상태로서 결정립의 크기는 장축이 약 $7{\mu}m$이었으며, 결정수가 함유되어 있는 탄산세륨과 무수의 수산기 함유 탄산세륨의 형상은 서로 다른 형태를 갖고 있음을 알 수 있다.

• 한국수소및신에너지학회논문집
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• 제26권5호
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• pp.477-483
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• 2015

LFG (Land-Fill Gas) includes components of $CH_4$, $CO_2$, $O_2$, $N_2$, and water. The preparation of synthesis gas from LFG as a DME (Dimethyl Ether) feedstock was studied by methane reforming of $CO_2$, $O_2$ and steam over $NiO-MgO-CeO_2/Al_2O_3$ catalyst. Our experiments were performed to investigate the effects of methane conversion and syngas yield on the amount of LFG components over $NiO-MgO-CeO_2/Al_2O_3$ catalyst. Results were obtained through the methan reforming experiments at the temperature of $900^{\circ}C$ and GHSV of 8,800. The results were as following; it has generally shown that syngas yield increase with the increase of oxygen and steam amounts and then decrease. Highly methane conversion of above 98% and syngas yield of approximately 60% were obtained in the feed of gas composition flow-rate of 243ml/min of $CH_4$, 241ml/min of $CO_2$, 195ml/min of $O_2$, 48ml/min of $N_2$, and 450ml/min of steam, respectively, under reactor pressure of 1 bar for 200 hrs of reaction time. Also, it was shown that catalyst deactivation by coke formation was reduced by excessively adding oxygen and steam as an oxidizer of the methane reforming.