• 제목/요약/키워드: No decomposition

검색결과 681건 처리시간 0.022초

마이크로 에멀젼 상태에서 전기분해법을 이용한 독성물질 분해 연구 (Decomposition of Toxic Chemicals in Microemulsion by Electrolytic Oxidation Method)

  • 심성현;전병철;정용찬
    • 청정기술
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    • 제14권3호
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    • pp.218-223
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    • 2008
  • 마이크로 에멀젼 수용액에 분산된 반응성 유기화합물을 전기분해를 통하여 얻을 수 있는 수산화이온 및 수소이온을 이용하여 가수분해시키고, 분해속도를 비교하는 실험을 수행하였다. 반응물질로 사용된 p-nitrophenylacetate (PNPA)의 가수분해로부터 발생하는 p-nitrophenoxide 농도 변화에 따른 흡광도 변화를 이용하여 분해속도를 얻을 수 있었다. 자체 조립한 전기분해 장치를 이용하여 전압, 반응온도, 반응물질 양에 따른 분해속도 변화를 관찰하였다. 마이크로 에멀젼 사용으로 인하여 반응물질 용해도를 증가시킬 수 있으며, 전기분해법 사용으로 인하여 반응속도 조절이 용이하며, 유지비용이 저렴하고, 기존 화학물질 투여방법에 비해 소모되는 시약 보충 및 반응 후 부산물 처리 등의 과정이 수월하다. 유기물질 분해에 대한 메커니즘 및 수처리 분야 응용에 대하여 토의하였다.

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질산매질에서 UV 조사에 의한 옥살산 분해 (Decomposition of Oxalic Acid in Nitric Acid by UV Radiation)

  • 김응호;김영환;정동용;유재형
    • 공업화학
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    • 제8권1호
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    • pp.108-113
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    • 1997
  • 본 연구에서는 질산매질에서 UV 광조사에 의한 옥살산 분해연구가 수행되었다. UV 광원은 $2537{\AA}$의 파장을 방출하는 수은램프가 사용되었다. UV 광조사에도 불구하고 옥살산 자체는 분해되지 않았다. 그러나 질산매질하에서 UV 광조사에 의해 옥살산은 쉽게 분해되었다. UV광조사에 의해 $NO_3{^-}$으로부터 발생되는 산소라디칼이 옥살산을 분해시키는 것으로 조사되었다. 옥살산 분해율은 질산 0.5M 부근에서 최대를 이루다가 질산농도 증가에 따라 점차 감소하였다. 이것 역시 산소라디칼과 $NO_3{^-}$ 사이에서 반응으로 쉽게 설명될 수 있다.

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$TiO_2$ 촉매를 이용한 플라즈마반응에 의한 NOx의 분해 (Reduction and Decomposition of Hazardous NOx by Discharge Plasma with $TiO_2$)

  • 박성국;우인성;황명환
    • 한국안전학회지
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    • 제23권5호
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    • pp.54-60
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    • 2008
  • The objective of this study is to obtain the optimal process condition and the maximum decomposition efficiency by measuring the decomposition efficiency, electricity consumption, and voltage in accordance with the change of the process variables such as the frequency, maintaining time period, concentration, electrode material, thickness of the electrode, the number of windings of the electrode, and added materials etc. of the harmful atmospheric contamination gases such as NO, $NO_2$, and $SO_2$ etc. with the plasma which is generated by the discharging of the specially designed and manufactured $TiO_2$ catalysis reactor and SPCP reactor. The decomposition efficiency of the NO, the standard samples, is obtained with the plasma which is being generated by the discharge of the combination effect of the $TiO_2$ catalysis reactor and SPCP reactor with the variation of those process variables such as the frequency of the high voltage generator($5{\sim}50kHz$), maintaining time of the harmful gases($1{\sim}10.5sec$), initial concentration($100{\sim}1,000ppm$), the material of the electrode(W, Cu, Al), the thickness of the electrode(1, 2, 3mm), the number of the windings of the electrode(7, 9, 11turns), basic gases($N_2$, $O_2$, air), and the simulated gas($CO_2$) and the resulting substances are analyzed by utilizing FT-IR & GC.

카본블랙 촉매 상에서 프로판-부탄 혼합가스 분해에 의한 수소 생산 (Hydrogen Production by Decomposition of Propane-Butane Mixture Gas Over Carbon Black Catalyst)

  • 윤석훈;박노국;이태진
    • 한국수소및신에너지학회논문집
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    • 제20권5호
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    • pp.397-403
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    • 2009
  • The catalysis of carbon black was investigated for the production of hydrogen by the catalytic decomposition of propane-butane mixture gas in this study. The thermal and the catalytic decompositions of hydrocarbons were performed at the temperature range of 500 - $1100^{\circ}C$, respectively. The conversions of hydrocarbons and the mole traction of hydrogen increased with increasing the reaction temperature and the conversion of hydrocarbons in the catalytic decomposition process was approximately liked with that obtained by the thermal decomposition. However, the mole traction of hydrogen produced in the catalytic decomposition process was higher than that obtained from the thermal decomposition. Therefore, it was concluded that the catalysis for the decomposition of hydrocarbons is occurred over carbon black used as catalyst. The mole traction of hydrogen produced by the catalytic decomposition of hydrocarbons also increased with increasing the mole ratio of $C_3H_8/C_4H_{10}$ in propane and butane mixture gas at $700^{\circ}C$. Therefore, it was concluded that the catalytic decomposition of the high propane mixture gas is more effectively for the production of hydrogen.

2,4,6-Trinitrotoluene (TNT)의 광분해 특성 (Photo-decomposition Characteristics of 2,4,6-Trinitrotoluene in a UV/$H_2O_2$ Process)

  • 권범근;최원용;윤제용
    • 상하수도학회지
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    • 제24권6호
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    • pp.775-788
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    • 2010
  • The decomposition of 2,4,6-trinitrotoluene (TNT) and the mass balance of nitrogen (N) species as products were investigated in a UV/H2O2system by varying pH, concentrations of $H_2O_2$, and $O_2$. All experiments were conducted in a semi-batch system employing a 50 mL reaction vessel and a coil-type quartz-tube reactor. In contrast with previous studies employing batch mode, TNT decomposition in the semi-batch mode was proportionally enhanced by increasing $H_2O_2$ concentration to 10 mM (0.034%), indicatingthat an inhibitory effect of excess $H_2O_2$on hydroxyl radical (${\cdot}OH$) can be negligible. N compounds are released as $NO_2^-$ in the early stages of the reaction, but $NO_2^-$ is rapidly oxidized to $NO_3^-$ by means of ${\cdot}OH$. $NH_4^+$ was also detected in this study and showed gradually the increase with increasing reaction time. In this study, $NH_4^+$ production can involve the reduction of nitro group of TNT concurrent with the production of $NO_3^-$. Of the N species originating from TNT decomposition, 12 ~ 72% were inorganic forms (i.e. [$NO_3^-$] + [$NO_2^-$] + [$NH_4^+$]). This result suggests that the large remaining N portions indicate that unidentified N compounds can exist.

고온 불활성 기체 분위기에서 아산화질소 열분해 및 반응속도에 관한 연구 (A Study of Nitrous Oxide Thermal Decomposition and Reaction Rate in High Temperature Inert Gas)

  • 이한민;윤재근;홍정구
    • 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.

Thr Adsorption and Decomposition of NO on a Stepped Pt(111) Surface

  • Lee, S. B.;Kang, D. H.;Park, C. Y.;Kwak, H. T.
    • Bulletin of the Korean Chemical Society
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    • 제16권2호
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    • pp.157-163
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    • 1995
  • The adsorption and decomposition of NO on a stepped Pt(111) surface have been studied using thermal desorption spectroscopy and Auger electron spectroscopy. NO adsorbs molecularly in two different states of the terrace and the step, which are distinguishable in thermal desorption spectra. NO dissociates via a bent species at the step sites on the basis of vibrational spectrum data reported previously. The dissociation of NO is an activation process : the activation energy is estimated to be about 2 kcal/mol. Increase in the NO dissociation with adsorption temperature is explained by a process controlled by diffusion of the dissociated atomic nitrogen from the step to the terrace of the surface. In addition to NO and N2, the desorption peak of N2O is observed. We conclude that the formation of N2O is attributed to surface reaction of NO and N adsorbed on the surface.

연변방전에 의한 유해물질의 분해제거 (Decomposition of Harmful Materials by SPCP Discharge)

  • 우인성;황명환
    • 한국전기전자재료학회논문지
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    • 제11권11호
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    • pp.1043-1048
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    • 1998
  • The decomposition performance of the Surface induced Plasma Chemical Processing(SPCP) for benzene, toluene, xylene and $NO_2$ were experimentally examined. Discharge exciting frequency range was 5kHz and 10kHz, and low frequency discharge requires high voltage to inject high electric power in gas and to decompose contaminants. The decomposition rate of dioxide nitrogen for 5kHz power in gas and to decompose contaminants. The decomposition rate of dioxide nitrogen for 5kHz power supply is only 85%, but it’s rate for 10kHz power supply is very high, more than 96% when peak voltage is 12kv. Aromatic hydrocarbon vapor of up to 1000ppm is almost throughly decomposed at the flow rate of 1000$\ell$/min or lower rate under the discharge with electric power of several hundred watts. High decomposition rate is shown in every case, that is, for SPCP reactor is necessary to obtain the decomposition rate of more than 80~98%. The decomposition rate of benzene, toluene and xylene were 90~98% and dioxide nitrogen was 45~96%.

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모호수 연산을 적용한 네트워크 신뢰도 (Reliability Approach to Network Reliability Using Arithmetic of Fuzzy Numbers)

  • 김국
    • 한국신뢰성학회지:신뢰성응용연구
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    • 제14권2호
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    • pp.103-107
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    • 2014
  • An algorithm to get network reliability, where each link has probability of fuzzy number, is proposed. Decomposition method and fuzzy numbers arithmetic are applied to the algorithm. Pivot link is chosen one by one from start node recursively at time of decomposition, and arithmetic of fuzzy complementary numbers is included at the same time. No criteria of pivot link selection and the recursive calculation make the algorithm simple.

Generalized Multicommodity Distribution System Design

  • Chen, Ju-Long;Morris, James-G.;Son, Ki-Hyoung
    • Management Science and Financial Engineering
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    • 제5권2호
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    • pp.25-41
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    • 1999
  • This paper generalizes the classic two-stage multicommodity distribution system design problem to the one that includes plant locations as well as distribution center locations. Accommodating plant location leads to subproblems which are mixed are mixed integer. Hence. no LP-type subproblems are avail-able, and therefore standard Benders decomposition no longer applies. We develop new solution method which combines an integer L-shaped method with Benders decomposition to suit the purpose, and pre-sent the test results.

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