• 한국분말재료학회지
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• 제11권1호
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• pp.28-33
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• 2004

In the present study, the focus is on the analysis of carbothermal reduction of the titanium-cobalt-oxygen based oxide powder by solid carbon for the optimizing synthesis process of ultra fined TiC/Co composite powder. The titanium-cobalt-oxygen based oxide powder was prepared by the combination of the spray drying and desalting processes using the titanium dioxide powder and cobalt nitrate as the raw materials. The titanium-cobalt-oxygen based oxide powder was mixed with carbon black, and then this mixture was carbothermally reduced under a flowing argon atmosphere. The changes in the phase structure and thermal gravity of the mixture during carbothermal reduction were analysed using XRD and TGA. The synthesized titanium-cobalt-oxygen based oxide powder has a mixture of $TiO_2$ and $CoTiO_3$. This oxide powder was transformed to a mixed state of titanium car-bide and cobalt by solid carbon through four steps of carbothermal reduction steps with increasing temperature; reduction of $CoTiO_3$ to $TiO_2$ and Co, reduction of $TiO_2$, to the magneli phase($Ti_nO_{2n-1}$, n>3), reduction of the mag-neli phase($Ti_nO_{2n-1}$, n>3) to the $Ti_nO_{2n-1}$(2$\leq$n$\leq$3) phases, and reduction and carburization of the $Ti_nO_{2n-1}$(2$\leq$n$\leq$3) phases to titanium carbide.

• 한국환경과학회지
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• 제12권9호
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• pp.997-1004
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• 2003

The objective of this research was to test whether, under controlled laboratory conditions, hybrid SNCR/SCR process improves N $O_{x}$ removal efficiency in comparison with the SNCR only. The hybrid process is a combination of a redesigned existing SNCR with a new downstream SCR. N $O_{x}$ reduction experiments using a hybrid SNCR/SCR process have been conducted in simple NO/N $H_3$/ $O_2$ gas mixtures. Total gas flow rate was kept constant 4 liter/min throughout the SNCR and SCR reactors, where initial N $O_{x}$ concentration was 500 ppm in the presence of 5% or 15% $O_2$. Commercial catalysts, $V_2$ $O_{5}$ -W $O_3$-S $O_4$/Ti $O_2$, were used for SCR N $O_{x}$ reduction. The residence time and space velocity were around 1.67 seconds and 2,400 $h^{-1}$ or 6000 $h^{-1}$ in SNCR and SCR reactors, respectively. N $O_{x}$ reduction of the hybrid system was always higher than could be achieved by SNCR alone at a given value of N $H_{3SLIP}$. Optimization of the hybrid system performance requires maximizing N $O_{x}$ removal in the SNCR process. An analysis based on the hybrid system performance in this lab-scale work indicates that a equipment with N $O_{xi}$ =500 ppm will achieve a total N $O_{x}$ removal of about 90 percent with N $H_{3SLIP}$ $\leq$ 5 ppm only if the SNCR N $O_{x}$ reduction is at least 60 percent. A hybrid SNCR/SCR process has shown about 26∼37% more N $O_{x}$ reduction than a SNCR unit process in which a lower temperature of 85$0^{\circ}C$ turned out to be more effective.be more effective.

• 한국환경과학회지
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• 제22권1호
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• pp.73-81
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• 2013

The present work has been devoted to the catalytic reduction of $N_2O$ by $H_2$ with $Pt/SiO_2$ catalysts at very low temperatures, such as $110^{\circ}C$, and their nanoparticle sizes have been determined by using $H_2-N_2O$ titration, X-ray diffraction(XRD) and high-resolution transmission electron microscopy(HRTEM) measurements. A sample of 1.72% $Pt/SiO_2$, which had been prepared by an ion exchange method, consisted of almost atomic levels of Pt nanoparticles with 1.16 nm that are very consistent with the HRTEM measurements, while a $Pt/SiO_2$ catalyst possessing the same Pt amount via an incipient wetness technique did 13.5 nm particles as determined by the XRD measurements. These two catalysts showed a noticeable difference in the on-stream $deN_2O$ activity maintenance profiles at $110^{\circ}C$. This discrepancy was associated with the nanoparticle sizes, i.e., the $Pt/SiO_2$ catalyst with the smaller particle size was much more active for the $N_2O$ reduction. When repeated measurements of the $N_2O$ reduction with the 1.16 nm Pt catalyst at $110^{\circ}C$ were allowed, the catalyst deactivation occurred, depending somewhat on regeneration excursions.

• 한국분무공학회지
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• 제25권3호
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• pp.132-138
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• 2020

N₂O is hazardous atmosphere pollution matter which can damage the ozone layer and cause green house effect. There are many other nitrogen oxide emission control but N₂O has no its particular method. Preventing further environmental pollution and global warming, it is essential to control N₂O emission from industrial machines. In this study, the thermal decomposition experiment of N₂O gas mixture is conducted by using cylindrical reactor to figure out N₂O reduction and NO formation. And CHEMKIN calculation is conducted to figure out reaction rate and mechanism. Residence time of the N₂O gas in the reactor is set as experimental variable to imitate real SNCR system. As a result, most of the nitrogen components are converted into N2. Reaction rate of the N₂O gas decreases with N₂O emitted concentration. At 800℃ and 900℃, N₂O reduction variance and NO concentration are increased with residence time and temperature. However, at 1000℃, N₂O reduction variance and NO concentration are deceased in 40s due to forward reaction rate diminished and reverse reaction rate appeared.

• Bulletin of the Korean Chemical Society
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• 제15권1호
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• pp.53-57
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• 1994

A comparison study on asymmetric borane reduction of ketoxime ethers and N-substituted ketimines possesing C = N double bond mediated by the selected chiral oxazaborolidines (1-6) was investigated. Thus, an aromatic ketoxime O-alkyl ether acetophenone oxime O-methyl ether was reduced to the corresponding amine (1-phenylethylamine 8a) with optical yields, such as 58% ee with 1, 86% ee with 2, 3% ee with 3, 99% ee with 4, 60% ee with 5, and 73% ee with 6. However, the reduction of an aliphatic ketoxime derivative 2-heptanone oxime O-methyl ether provided low optical inductions (7-13% ee). For ketoxime O-trimethylsilyl ethers, the reduction of acetophenone O-trimethylsilyl ether afforded 8a with optical yields which were 90% ee with 1, 40% ee with 2, 2% ee with 3, 62% ee with 4, 5% ee with 5, and 60% ee with 6. The reduction of 2-heptanone O-trimethylsilyl ether also gave the product amine with low optical yields (10-40% ee). In the case of N-substituted ketimines, the reduction of acetophenone N-phenylimine afforded the corresponding amine with 79% ee, 78% ee, 9% ee, 73% ee, 78% ee and 67% ee using 1, 2, 3, 4, 5, and 6, respectively, whereas low optical inductions (5-18% ee) for 2-heptanone N-phenylimine were achieved.

• Korean Chemical Engineering Research
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• 제47권1호
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• pp.96-104
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• 2009

혼합금속산화물에 담지된 Pd-Rh 허니컴 촉매 상에서 NO와 $N_2O$를 동시에 저감하기 위한 반응 온도를 낮추면서 각각의 반응물에 대한 전환율을 높이기 위하여, 환원제로 수소 또는 일산화탄소 사용에 대해 조사하였다. 각각의 환원제 사용 시, NO와 $N_2O$의 전환율에 대한 반응 조건의 영향을 조사하기 위해 반응온도, 각 환원제와 산소의 농도, NO와 $N_2O$ 간의 농도 비율 등을 변화시켰다. 먼저 수소를 환원제로 사용하는 경우, 산소의 부재시 $200^{\circ}C$ 미만의 저온에서 50% 이상의 NO와 $N_2O$ 전환율을 얻을 수 있었다. 한편, 일산화탄소를 환원제로 사용하는 경우에는 NO와 $N_2O$ 전환율이 각각 $200^{\circ}C$와 $300^{\circ}C$ 이상에서 증가하기 시작하였다. 그러나, 두 가지 환원제 모두의 경우에서, 반응 가스내에 산소 농도가 증가함에 따라 $N_2O$와 NO 전환율에 감소하였다. 결과적으로 일산화탄소 환원제에 비해, 수소 환원제가 상대적으로 저온에서 NO와 $N_2O$를 동시에 저감할 수 있으며, 산소 농도에 의한 영향을 덜 받는 것으로 나타났다. 반면, 반응물내 $N_2O$와 NO 농도비에 의한 NO와 $N_2O$ 전환율의 영향은 환원제의 종류에 크게 영향을 받지 않는 것으로 관찰되었다. 저온에서 NO와 $N_2O$를 동시에 저감시키기 위해서는 산소 분위기보다는 수소 분위기에서 촉매를 전처리하는 것이 보다 효과적인 것으로 나타났다.

• 한국대기환경학회지
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• 제33권6호
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• pp.605-615
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• 2017

Efficient simultaneous reduction conditions for $NO_x$ and $NH_3$-slip was investigated in SCR (Selective Catalytic Reduction) process with load variation by applying dual catalysts (SCR catalyst, $NH_3$ decomposition catalyst) system. $N_2O$ formation characteristics were analyzed to look into possible undesirable reaction pathways. In the experiments of catalyst characteristics, various operational variables were tested for the combined catalytic system, such as $NH_3/NO_x$ ratio, temperature, oxygen concentration and $H_2O$. The reaction characteristics of $NO_x$, $NH_3$ and $N_2O$ were analyzed and optimal conditions could be evaluated for the combustion facility with varied load. In terms of $NO_x/NH_3$ simultaneous reduction and $N_2O$ formation suppression, optimal condition was considered NSR 1.2 and temperature $300^{\circ}C$. At this operational condition, $NO_x$ conversion was 98%, $NH_3$ reduction efficiency was 95%, generated $N_2O$ concentration 9.5 ppm with inlet $NO_x$ concentration of 100 ppm. In $NH_3-SCR$ process with $NH_3$ decomposition catalyst, $NO_x$ and $NH_3$ can be considered to be reduced simultaneously at limited conditions. The results of this study may be utilized as basic data at facilities requiring simultaneous $NO_x$ and $NH_3$ reduction for facilities with load variation.

• 공업화학
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• 제19권6호
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• pp.624-628
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• 2008

$N_2O$는 주요 온실가스 성분의 하나로서 광화학 스모그의 유발, 산성비의 전구체 등 온실효과에 상당한 기여를 하고 있는 물질이다. 이러한 $N_2O$ 및 질소산화물을 제거하기 위하여 환원제를 이용한 Selective Catalytic Reduction (SCR) 반응 공정이 널리 사용되고 있다. 본 연구에서는 Hydrotalcite 형태의 전구체로부터 Mixed Metal Oxide 촉매를 제조하고 그를 사용하여 $N_2O$ 분해를 위한 메탄 SCR 반응 및 CO의 생성효과를 비교 연구하였다. 실험결과 $CH_4$ 환원제의 첨가는 $N_2O$의 분해 반응에 긍정적인 영향을 미치며, 최적화된 $O_2/CH_4$ 비율의 조건에서 메탄의 부분산화에 의한 SCR 반응이 가장 높은 효율을 나타내는 것을 확인할 수 있었다.

• Korean Chemical Engineering Research
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• 제51권3호
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• pp.313-318
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• 2013

$V_2O_5-WO_3/TiO_2$ 촉매의 질소산화물 환원반응에 있어서 $V_2O_5$ 함량이 NO 환원 및 $N_2O$ 생성에 미치는 영향을 조사하기 위하여 분말촉매를 사용한 미분반응기에서 실험 연구를 수행하였다. 고정된 비율의 $WO_3$와 $TiO_2$에 $V_2O_5$ 함량을 1에서 8 wt%까지 변화시킨 촉매에서 NO 환원반응과 암모니아 산화반응 특성이 조사되었다. $V_2O_5-WO_3/TiO_2$ 촉매에서 NO 환원 반응은 $200^{\circ}C$ 이하에서도 상당량 진행되지만, $V_2O_5$ 함량을 1 wt% 촉매의 경우 700 ppm의 NO를 99.9%이상 전환시키는 최저 반응온도가 $340^{\circ}C$에서 아주 좁은 활성 온도창으로 일어났다. 그리고 이 활성온도는 촉매의 $V_2O_5$ 함량이 증가됨에 따라 점점 저온 쪽으로 이동하여, 6 wt% 촉매의 경우 $220{\sim}340^{\circ}C$에서 높은 활성을 보였다. $V_2O_5$ 함량이 8 wt% 촉매의 경우 전 온도 구간에서 6 wt% 촉매보다 낮은 NO 환원율을 보였다. 그러나 반응온도 $340^{\circ}C$ 이상에서는 촉매의 $V_2O_5$ 함량이 증가함에 따라 NO 전환율이 감소하였다. 이는 $V_2O_5-WO_3/TiO_2$ 촉매의 NO 환원을 위한 촉매 활성점 상당 크기 이상의 $V_2O_5$ 입자와 관계되는 것으로 판단되며 촉매 입자가 클수록 $320^{\circ}C$ 이상에서 암모니아 산화에 의해 발생되는 $N_2O$ 생성을 고려하여야 한다. $V_2O_5-WO_3/TiO_2$ 촉매는 배기가스 중의 질소산화물 제거를 위하여 현재 통상적으로 $350{\sim}450^{\circ}C$의 영역에서 운전되고 있으나, 고온 영역에선 2차 오염물인 $N_2O$의 발생을 피할 수 없고 에너지 소비량이 많으므로, $250{\sim}320^{\circ}C$의 저온 영역에서 적합한 촉매로써 $V_2O_5$ 함량이 높은 $V_2O_5-WO_3/TiO_2$ 촉매의 사용이 권장되었다.

• Environmental Engineering Research
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• 제10권5호
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• pp.239-246
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• 2005

The effect of Pt addition over $V_2O_5-WO_3/TiO_2$ catalyst supported on PRO-66 was investigated for NO reduction in order to develop the catalytic filter working at low temperature. Catalytic filters, $Pt-V_2O_5-WO_3/TiO_2/PRD$, were prepared by co-impregnation of Pt, V, and W precursors on $TiO_2$-coated ceramic filter named PRD (PRD-66). Titania was coated onto the pore surface of the ceramic filter using a vacuum aided-dip coating method. The Pt-loaded catalytic filter shifted the optimum working temperature from $260-320^{\circ}C$(for the catalytic filter without Pt addition) to $190-240^{\circ}C$, reducing 700 ppm NO to achieve the $N_x$ slip concentration($N_x\;=\;NO+N_2O+NO_2+NH_3$) less than 20 ppm at the face velocity of 2 cm/s. $Pt-V_2O_5-WO_3/TiO_2$ supported on PRD showed the similar catalytic activity for NO reduction with that supported on SiC filter as reported in a previous study, which implies the ceramic filter itself has no considerable interaction for the catalytic activity.