• 한국대기환경학회지
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• 제16권4호
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• pp.373-380
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• 2000

A new type of photocatalyst plasma air purification filter for decomposition of some VOCs has been developed. The photocatalyst plasma air purification filter employs the pulsed discharge plasma as an energy source of TiO2. photocatalyst instead of UV light. In closed room(2m3) test removal efficiency of some VOCs was 80∼100% in 15∼24 hours. In the initial step of phptocatalyst plasma reaction. Acetone and Nitromethane etc were detected. But they were completely oxidized to CO2 and H2O.

• 한국산학기술학회논문지
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• 제12권11호
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• pp.5357-5364
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• 2011

본 연구에서는 연소 배기가스로부터 포집된 이산화탄소를 다시 일산화탄소 또는 탄소로 전환하여 산업에 다시 활용하고자 하는 탄소순환형 기술개발이 목적이다. 그러나 이산화탄소는 안정한 화합물로 쉽게 분해되지 않기 때문에 적합한 금속계 산화물(활성화제)이 필요하며, 가능한 낮은 온도에서 분해되어야 한다. 따라서 본 연구에서는 바륨페라이트 분말을 사용하여 $CO_2$를 CO나 C로 전환하고자 하였다. 바륨페라이트는 산업계에서 사용되고 있는 고상법을 이용하여 제조된 분말과 수열합성을 이용해 제조된 분말을 사용하여 각각 이산화탄소 분해특성 연구를 수행하였다. 이산화탄소의 분해 특성을 관찰하기 위해 TPR/TPO와 TGA 장치를 사용하였다. TPR/TPO를 이용한 수소에 의한 환원곡선 면적과 $CO_2$에 의한 흡착분해 곡선면적을 측정한 결과 수열합성을 이용해 제조된 바륨페라이트 분말이 우수한 성능을 나타내었다. 그러나 TGA를 이용한 실험결과에서는 $500^{\circ}C$에서 고상법에 의해 제조된 시료가 수소에 의한 흡착환원이 21.96wt% 발생하였고, $CO_2$에 의한 산화량도 21.24wt%로 가장 높게 나타났다. 그리고 이산화탄소의 분해 효율이 96.72wt%로 우수한 산화 환원 특성을 나타내었다.

• 청정기술
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• 제24권1호
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• pp.35-40
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• 2018

$N_2O$ 촉매 분해 반응을 위한 $Co_3O_4$ 촉매는 공침법을 이용하여 제조하였으며, 조촉매로서 Ce 및 Zr의 양을 (Ce 또는 Zr)/Co = 0.05의 몰비로 고정하여 제조하였다. 또한 K가 촉매에 미치는 영향을 조사하기 위해 1 wt%의 $K_2CO_3$를 함침하여 촉매를 제조하였다. 제조된 촉매의 특성은 BET, SEM, XRD, $H_2-TPR$, XPS를 통해 분석하였다. $Co_3O_4$ 촉매는 스피넬 결정상을 나타냈으며, 조촉매의 첨가는 입자 크기와 결정 크기를 감소시켜 비표면적을 증가시키는 것으로 나타났다. K의 도핑은 촉매 활성 물질인 Co의 활성 종인 $Co^{2+}$의 농도를 증가시켜 촉매 활성을 향상시키는 것으로 확인되었다. $N_2O$ 분해 반응 테스트는 $GHSV=45,000h^{-1}$, $250{\sim}375^{\circ}C$에서 수행되었으며 $Co_3O_4$ 촉매에 조촉매를 첨가하였을 때도 반응성이 증가하였지만, K를 함침하면 활성이 더욱 크게 증가하는 것으로 나타났다. K의 도핑이 활성 종인 $Co^{2+}$의 농도를 증가시키며, 환원온도를 낮춰 주어 활성에 큰 영향을 주는 것으로 확인하였다.

• Bulletin of the Korean Chemical Society
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• 제24권7호
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• pp.971-974
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• 2003

By utilizing singular value decomposition (SVD) and shift averaged Harr wavelet transform (WT) with a set of Daubechies wavelet coefficients (1/2, -1/2), a method that can simultaneously eliminate an unwanted large solvent peak and noise peaks from NMR data has been developed. Noise elimination was accomplished by shift-averaging the time domain NMR data after a large solvent peak was suppressed by SVD. The algorithms took advantage of the WT, giving excellent results for the noise elimination in the Gaussian type NMR spectral lines of NMR data pretreated with SVD, providing superb results in the adjustment of phase and magnitude of the spectrum. SVD and shift averaged Haar wavelet methods were quantitatively evaluated in terms of threshold values and signal to noise (S/N) ratio values.

• 청정기술
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• 제24권3호
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• pp.198-205
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• 2018

본 연구는 $Co-CeO_2$ 촉매의 $N_2O$ 분해 반응에서 촉매의 제조 방법이 활성에 미치는 영향을 고찰하였다. $Co-CeO_2$ 촉매는 공침법(Co-precipitation)과 함침법(Incipient wetness impregnation)으로 제조하였다. 제조된 촉매의 성능을 평가하기 위하여 $N_2O$ 직접 촉매 분해(Direct catalytic $N_2O$ decomposition) 반응을 $250{\sim}375^{\circ}C$에서 실시하였다. 그 결과 공침법으로 제조된 촉매(CoCe-CP)는 $O_2$ 및/또는 $H_2O$의 존재 하에서도 $N_2O$ 분해 반응에서 향상된 성능을 보인 반면에 함침법으로 제조된 촉매(CoCe-IM)는 그렇지 못하였다. 이러한 촉매 활성의 차이를 조사하기 위하여 XRD, BET, TEM, $H_2-TPR$, $O_2-TPD$ 그리고 XPS와 같은 촉매 특성 분석들을 진행하였다. 촉매의 제조 방법에 따라서 입자의 크기 및 표면적이 변화하는 것을 확인하였고 합성 과정이 촉매의 물리적 특성에 영향을 미치는 것을 알 수 있었다. 공침법으로 제조된 촉매의 활성 증가는 $Co^{3+}{\rightarrow}Co^{2+}$의 향상된 환원 특성 및 산소 탈착 속도 향상에 기인한 것으로 여겨진다. 하지만, $N_2O$ 분해와 관련이 있는 촉매의 표면 전하 상태 및 결합에너지는 제조 방법에 따라서 변하지 않는 것을 확인하였다.

• 한국세라믹학회지
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• 제24권5호
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• pp.453-460
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• 1987

β'-sialon(Z=2.7) specimens with <30%wt. graphite as a reducing agent were decomposed at 1350°up to 1,450℃ under the atmosphere of 90% N2-10%H2. The decomposition of β'-sialon was calculated from the change in Z-value, and the formation of new minerals was identified from X-ray diffraction patterns. The decomposition reactions of sialon were considered to yield a stable sialon close to β-silicon nitride and some aluminum compounds according to the following equations; β'-sialon(s)＋C(s)＋N2(g)→β2-sialon(metastable)＋β3-sialon(stalbe phase) β2-sialon(s)＋C(s)＋N2(g)→β3-sialon(s)＋AlN(s)＋α-Al2O3(s)＋15R(s)＋SiO(g)＋Al2O(g)＋CO(g) Z-value; β2( 3.5)>β'( 2.7)>β3( 0.5) The decomposition rate of sialon was controlled by two mechanisms ; One was characterized by the interface area of contact, corresponding to an apparent activation energy of 50.5Kcal/mol in the initial stage, and the other by the diffusion, corresponding to that of 104.3Kcal/mol in the final stage of the decomposition.

• 한국환경보건학회지
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• 제24권1호
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• pp.32-37
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• 1998

The Carbon Dioxide is the gas, which causes green house effects, unusual changes in the weather, destruction of the life. Almost every nation in the world is trying to search the countermeasure to this poisonous gas. I synthesized $Fe_3O_4$ and NaOH, in order to decompose the Carbon Dioxide. Among the particles synthesizing $Fe_3O_4$, I chose the equivalent ratio 1.00 which can decompose the Carbon Dioxide best, and fixed that equivalent ratio and added the 0.005-3.00 mole percentage of NiCl$_2$ and synthesized $Fe_3O_4$. I studied the decomposition of the Carbon Dioxide and methanized reaction, by measuring its crystal structure, thermochemistrical character and specific surface area. In decomposing the Carbon Dioxide, I used oxygen-deficit Magnetite which I produced by injecting the hydrogen gas into the synthesized sample. I observed the methanization reaction by raising the temperature of sample up to 650$\circ$C and having it reacted with the hydrogen gas. The decomposition of the Carbon Dioxide was added 0.005, 0.03, 0.05 mole percentage of NiCl$_2$ was more effective than pure $Fe_3O_4$. All sample in which the decomposition of the Carbon Dioxide took place produced the methane gas.

• 한국대기환경학회지
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• 제24권5호
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• pp.512-522
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• 2008

Ammonia is a major compound of odor in livestock house. To enhance the performance of ammonia oxidation (decomposition). the gas-liquid, two phase photocatalytic oxidation system was designed and prepared in this study. Commercial P-25 as $TiO_2$ catalyst was used for ammonia decomposition. V/P-25 catalyst prepared by sol gel method was also used for the removal of by-producted $NO_x$ in $NH_3$ oxidation reaction. When $TiO_2$ was used as a photocatalyst, the conversion to $N_2$ in ammonia decomposition reached above 90% until 200hr (The air flow rate of 4L/min with the ammonia concentration up to 25ppm.). However, considerable amounts of NO and $NO_2$ were formed as a result of $NH_3$ oxidation (as a by-product). Therefore, we added Vanadia impregnated $TiO_2$(P-25) catalyst for the removal of $NO_x$ at the end of reaction trail. The results of a pilot-scale operation were successful to achieve the simultaneous removal of $NH_3\;and\;NO_x$ about 81 and 87%, respectively.

• 센서학회지
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• 제22권3호
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• pp.197-201
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• 2013

This paper describes the fabrication and characterization of graphene based carbon dioxide ($CO_2$) gas sensors. Graphene was synthesized by thermal decomposition of SiC. The resistivity $CO_2$ gas sensors were fabricated by pure graphene and graphene decorated Au nanoparticles (NPs). The Au NPs with size of 10 nm were decorated on graphene. Au electrode deposited on the graphene showed Ohmic contact and the sensors resistance changed following to various $CO_2$ concentrations. Resulting in resistance sensor using pure graphene can detect minimum of 100 ppm $CO_2$ concentration at $50^{\circ}C$, whereas Au/graphene can detect minimum 2 ppm $CO_2$ concentration at same at $50^{\circ}C$. Moreover, Au NPs catalyst improved the sensitivity of the graphene based $CO_2$ sensors. The responses of pure graphene and Au/graphene are 0.04% and 0.24%, respectively, at $50^{\circ}C$ with 500 ppm $CO_2$ concentration. The optimum working temperature of $CO_2$ sensors is at $75^{\circ}C$.

• 한국응용과학기술학회지
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• 제18권3호
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• pp.174-179
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• 2001

The spinel $Fe_{3}O_{4}$ powders were synthesized using 0.2 $M-FeSO_4{\cdot}7H_{2}O$ and 0.5 M-NaOH by oxidation in air and the spinel $LiMn_{2}O_{4}$ powders were synthesized at 480 $^{\circ}C$ for 12 h in air by a sol-gel method using manganese acetate and lithium hydroxide as starting materials. The synthesized $LiMn_{2}O_{4}$ powders were mixed at portion of 5, 10, 15 and 20 wt% of $Fe_{3}O_{4}$ powders using a ball-mill. The mixed catalysts were dried at room temperature for 24 hrs. The mixed catalysts were reduced by hydrogen gas at 350 $^{\circ}C$ for 2 h. The carbon dioxide decomposition rates of the mixed catalysts were 90% in all the mixed catalysts but the decomposition rate of carbon dioxide was increased with adding $LiMn_{2}O_{4}$ powders to $Fe_{3}O_{4}$ powders.