• 제목/요약/키워드: Decomposition of Efficiency

검색결과 664건 처리시간 0.038초

방전 플라스마에 의한 CFC-12($CCl_2F_2$)의 분해 (Decomposition of CFC-12($CCl_2F_2$) by Discharge Plasma)

  • 강현춘;우인성;황명환;안형환;이한섭;조정국;강안수
    • 한국안전학회지
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    • 제14권3호
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    • pp.93-100
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    • 1999
  • Decomposition efficiency, power consumption, and applied voltage of CFC(Chlorofluorocatbon) were investigated by SPCP(surface induced discharge plasma chemical processing) reactor to obtain optimum process variables and maximum decomposition efficiencies. Decomposition efficiency of CFC-12 with various electric frequencies(5~50kHz). flow rates (100~1,000mL/min), initial concentrations(100~1,000ppm), electrode materials(W, Cu, Al). electrode thickness(1, 2, 3mm) and reference gases($N_2$, $O_2$, air) were measured and the products were analyzed with FT-IR. Experimental results showed that at the frequency of 10kHz, the highest decomposition efficiency of 92.7% for CFC-12 were observed at the power consumptions of 29.6W. respectively, and that decomposition efficiency decreased with increasing frequency above 20kHz and decomposition efficiency per unit power were 3.13%/W for CFC-12. Decomposition efficiency was increased with increasing residence times and with decreasing initial concentration of pollutants. Decomposition efficiency was increased with increasing thickness of discharge electrode and the highest decomposition efficiency was obtained for the electrode diameter of 3m. As the electrode material, decomposition efficiency was in order that tungsten(W), copper(Cu), aluminum (Al). Decomposition of CFC-12 in the reference gas of $N_2$ showed the highest efficiency among three reference gases, and then the effect of reference gas on the decomposition efficiency decreased in order of air and $O_2$. The optimum power for the maximum decomposition efficiency was 25.3W for CFC.

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EFFICIENCY ANALYSIS OF A DOMAIN DECOMPOSITION METHOD FOR THE TWO-DIMENSIONAL TELEGRAPH EQUATIONS

  • Jun, Younbae
    • East Asian mathematical journal
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    • 제37권3호
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    • pp.295-305
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    • 2021
  • In this paper, we analyze the efficiency of a domain decomposition method for the two-dimensional telegraph equations. We formulate the theoretical spectral radius of the iteration matrix generated by the domain decomposition method, because the rate of convergence of an iterative algorithm depends on the spectral radius of the iteration matrix. The theoretical spectral radius is confirmed by the experimental one using MATLAB. Speedup and operation ratio of the domain decomposition method are also compared as the two measurements of the efficiency of the method. Numerical results support the high efficiency of the domain decomposition method.

연면방전에 의한 질소산화물의 분해시 전극 공정변수에 대한 영향 (Effect of Electrode Process Variables in case of Decomposition of $NO_{x}$ by SPCP)

  • 안형환;강현춘
    • 대한안전경영과학회지
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    • 제1권1호
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    • pp.241-258
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    • 1999
  • For hazardous air pollutants(HAP) such as NO and $NO_{2}$ decomposition efficiency, power consumption, and applied voltage were investigated by SPCP(surface induced discharge plasma chemical processing) reactor to obtain optimum process variables and maximum decomposition efficiencies. Decomposition efficiency of HAP with various electric frequencies(5~50 kHz), flow rates(100~1,000 mL/min), initial concentrations(100~1,000 ppm), electrode materials(W, Cu, Al), electrode thickness(1, 2, 3 mm) and number of electrode windings(7, 9, 11) were measured. Experimental results showed that for the frequency of 10 kHz, the highest decomposition efficiency of 94.3 % for NO and 84.7 % for $NO_{2}$ were observed at the power consumptions of 19.8 and 20W respectively and that decomposition efficiency decreased with increasing frequency above 20 kHz. Decomposition efficiency was increased with increasing residence times and with decreasing initial concentration of pollutants. Decomposition efficiency was increased with increasing thickness of discharge electrode and the highest decomposition efficiency was obtained for the electrode diameter of 3 mm in this experiment. As the electrode material, decomposition efficiency was in order : tungsten(W), copper(Cu), aluminum(Al).

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Ca(OH)2촉매를 이용한 플라즈마 반응에 의한 황산화물(유해가스)의 제거에 관한 연구 (A study of decomposition of sulfur oxides(harmful gas) using calcium dihydroxide catalyst by plasma reactions)

  • 김다영;황명환;우인성
    • 대한안전경영과학회지
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    • 제16권2호
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    • pp.237-246
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    • 2014
  • Researches on the elimination of sulfur and nitrogen oxides with catalysts and absorbents reported many problems related with elimination efficiency and complex devices. In this study, decomposition efficiency of harmful gases was investigated. It was found that the efficiency rate can be increased by moving the harmful gases together with SPCP reactor and the catalysis reactor. Calcium hydroxide($Ca(OH)_2$), CaO, and $TiO_2$ were used as catalysts. Harmful air polluting gases such as $SO_2$ were measured for the analysis of decomposition efficiency, power consumption, and voltage according to changes to the process variables including frequency, concentration, electrode material, thickness of electrode, number of electrode winding, and additives to obtain optimal process conditions and the highest decomposition efficiency. The standard sample was sulfur oxide($SO_2$). Harmful gases were eliminated by moving them through the plasma generated in the SPCP reactor and the $Ca(OH)_2$ catalysis reactor. The elimination rate and products were analyzed with the gas analyzer (Ecom-AC,Germany), FT-IR(Nicolet, Magna-IR560), and GC-(Shimazu). The results of the experiment conducted to decompose and eliminate the harmful gas $SO_2$ with the $Ca(OH)_2$ catalysis reactor and SPCP reactor show 96% decomposition efficiency at the frequency of 10 kHz. The conductivity of the standard gas increased at the frequencies higher than 20 kHz. There was a partial flow of current along the surface. As a result, the decomposition efficiency decreased. The decomposition efficiency of harmful gas $SO_2$ by the $Ca(OH)_2$ catalysis reactor and SPCP reactor was 96.0% under 300 ppm concentration, 10 kHz frequency, and decomposition power of 20 W. It was 4% higher than the application of the SPCP reactor alone. The highest decomposition efficiency, 98.0% was achieved at the concentration of 100 ppm.

방전플라스마에 의한 NOx, SOx 분해시 메탄첨가의 영향 (Effect of CH4 Addition in Case of Decomposition of NOx, SOx by Discharge Plasma)

  • 강현춘;우인성;강안수
    • 한국안전학회지
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    • 제15권2호
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    • pp.70-77
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    • 2000
  • For hazardous air pollutants(HAP) such as NO, $NO_2$ and $SO_2$ decomposition efficiency, power consumption, and applied voltage were investigated by SPCP(Surface induced discharge Plasma Chemical Processing) reactor to obtain optimum process variables and maximum decomposition efficiencies. Decomposition efficiency of HAP with various electric frequencies(5~50 kHz), flow rates(100~1,000 mL/min), initial concentrations(100~1,000 ppm) and additive($CH_4$) were measured and the products were analyzed with FT-IR. Experimental results showed that for the frequency of 10 kHz, the highest decomposition efficiency of 94.3 % for NO, 84.7 % for $NO_2$ and 99 % far $SO_2$ were observed at the power consumptions of 19.8, 20 and 19W, respectively, and that decomposition efficiency decreased with increasing frequency above 20 kHz. And decomposition efficiency per unit power were 5.21 %/W for $SO_2$, 4.76 %/W for NO and 4.24 %/W for $NO_2$ and the highest decomposition efficiency was observed with $SO_2$. Decomposition efficiency was increased with increasing residence times and with decreasing initial concentration of pollutants. When the additive of $CH_4$ was used, decomposition efficiency was increased with increasing $CH_4$ content, and NO, $NO_2$ and $SO_2$ were almost completely decomposed with the efficiency of 99 %, 98 % and 99 %, respectively and therefore $CH_4$ was a good additive material. The optimum power for the maximum decomposition efficiency were 7.5 W for $SO_2$, 9.5 W for NO and 15.5 W for $NO_2$, respectively. Optimum power with the maximum decomposition efficiency were 9.5 W at 1,000 ppm of NO, 7~8 W at 100~500 ppm of NO and 15.5 W at all concentration range of $NO_2$ and 11.5 W at 1,000 ppm, 4.9 W at 500 ppm, 3.7 W at 100~300 ppm of $SO_2$ and power efficiency was best in these case.

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Structural Properties of Dielectric Barrier Reactor with Hole (DBH) for CF4 Decomposition

  • Jung Jung Gun;Kim Jong Suk;Park Jae Yoon;Kim Kwang Soo;Rim Geun Hie
    • Transactions on Electrical and Electronic Materials
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    • 제4권4호
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    • pp.30-35
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    • 2003
  • In this paper, the $CF_4$ decomposition efficiency is investigated for three simulated plasma reactors that are needle plate reactor, metal particle reactor, and dielectric barrier reactor with hole (DBH). The$CF_4$ decomposition efficiency by DBH is much better than that by needle plate reactor or metal particle reactor. When applied voltage is increased up to the critical voltage for spark formation in the all reactors, the $CF_4$ decomposition efficiency is increased. The $CF_4$ decomposition efficiency in needle plate reactor and metal particle reactor is about $12\%$ and $22\%$ respectively at applied voltage of 23 kV (consumption power: 110 W) and $CF_4$ concentration of 500 ppm, however, the $CF_4$ decomposition efficiency is more than $95\%$ in case of DBH. DBH should be much better than two reactors investigated for $CF_4$ decomposition.

고밀도스트리머를 이용한 $CF_{4}$ 분해특성 (The characteristic of $CF_{4}$ decomposition for High density streamer)

  • 송원섭;박재윤;정장근;김종석;김태용
    • 한국전기전자재료학회:학술대회논문집
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    • 한국전기전자재료학회 2002년도 제4회 영호남학술대회 논문집
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    • pp.133-137
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    • 2002
  • In this paper, the $CF_{4}$ decomposition rate are investigated for a simulated three plasma reactors which are metal particle reactor, spiral wire reactor and reactor with porous dielectric as applied voltage. The $CF_{4}$ decomposition rate by plasma reactor with porous dielectric had a gain of 20~25[%] over that by plasma reactor with spiral wire or metal particle electrode. The $CF_{4}$ decomposition efficiency increases with increasing applied voltage up to the critical voltage for spark formation. The $CF_{4}$ decomposition efficiency of metal particle reactor was about 80[%] at AC 24[kV]. However, decomposition efficiency is more than 90% in case of the reactor with porous dielectric. we think, the reactor with porous dielectric should be much better than other reactors for $CF_{4}$ decomposition.

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플라즈마 광촉매 복합 긍정을 이용한 악취물질 중 TEA, MEK의 분해처리 (Treatment of Odorous air pollutants by Plasma and Photocatalytic Process.)

  • 최금찬;정창훈
    • 한국환경과학회지
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    • 제12권12호
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    • pp.1255-1260
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    • 2003
  • Plasma-photocatalytic oxidation process was applied in the decomposition of Triethylamine(TEA) and Methyl ethyl ketone(MEK). Plasma reactor was made entirely of pyrex glass and consists of 24mm inner diameter, 1,800mm length and discharge electrode of 0.4mm stainless steel. And initial concentrations of TEA and MEK for plasma-photocatalytic oxidation are 100 ppm. Odor gas samples were taken by gas-tight syringe from a glass sampling bulb which was located at reactor inlet and outlet, and TEA and MEK were determined by GC-FID. For plasma process, the decomposition efficiency of TEA and MEK were evaluated by varying different flowrates and decomposition efficiency of TEA and MEK increased considerably with decreasing treatment flowrates. For photocatalytic oxidation process, also the decomposition efficiency of TEA and MEK increased considerably with decreasing treatment flowrates. The decomposition efficiency of MEK was 57.8%, 34.2%, 18.8% respectively and the decomposition efficiency of TEA was reached all 100%. This result is higher than that of plasma process only, From this study, the results indicate that plasma-photocatalytic oxidation process is ideal for treatment of TEA and MEK.

Removal Characteristics of Benzene in Dielectric Barrier Discharge Process

  • Chung, Jae-Woo
    • Journal of Korean Society for Atmospheric Environment
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    • 제18권E1호
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    • pp.13-20
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    • 2002
  • The electrical and chemical properties of the dielectric barrier discharge (DBD) process for the benzene removal were investigated. The benzene removal was initiated with the applied voltage higher than the discharge onset value. The removal efficiency over 95 % was obtained at approximately 1.6 kJ lite $r^{r-1}$ of the electrical energy density. The increase of the inlet concentration decreased the removal efficiency. However, the benzene decomposition rate increased with the inlet concentration . While the increase of the gas retention time enhanced the removal efficiency, the decomposition rate decreased. Identification of the optimum condition between the decomposition rate and the removal efficiency is required for field applications of the DBD process.s.

연면방전에 의한 질소산화물의 분해시 전극 공정변수에 대한 영향 (Effect of Electrode Process Variables in case of Decomposition of $NO_x$ by SPCP)

  • 안형환;강현춘
    • 대한안전경영과학회:학술대회논문집
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    • 대한안전경영과학회 1999년도 추계학술대회
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    • pp.543-563
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    • 1999
  • 본 연구에서는 특수 설계된 연면방전(Surface discharge induced Plasma Chemical Process, SPCP) 반응기로부터 발생하는 플라스마에 의하여 일산화질소(NO)와 이산화질소($NO_2$)등 유해 환경오염 가스를 주파수, 유량, 농도, 전극재질 및 감은 횟수 등의 공정변수 변화에 따른 분해율, 소비전력 및 소비전압 등을 측정하여 최적의 공정조건과 최대의 분해효율을 얻고자 하였다. 표준시료로서 일산화질소와 이산화질소를 고전압발생기의 주파수(5~50kHz), 유해가스의 체류시간(1~10.5 초)과 초기농도(100~1000 ppm), 전극의 재질(W, Cu, Al), 전극의 굵기(1, 2, 3 mm)및 감은횟수(7회, 9회, 11회)에 대하여 플라스마 연면방전 반응기를 이용하여 분해효율을 구하였다. 유해가스(NO, $NO_2$)의 분해제거 실험결과, 10 kHz의 주파수와 각각 19.8와 20 W의 소비전력에서 각각 94.3, 84.7 %로 가장 높은 분해제거율을 나타내었고, 20 kHz이상에서는 주파수가 커질수록 분해율이 감소하였다. 또한 연면방전 반응기에서 유해가스의 체류시간이 길수록, 그리고 초기농도가 작을수록 분해율은 증가하였다. 방전전극에 대한 영향은 전극의 굵기가 굵을수록 분해율이 증가하여 본 실험의 경우 3 mm의 전극을 사용하였을 때 가장 높은 분해율을 나타내었고, 전극의 재질은 텅스텐을 사용하여 방전한 경우에 가장 높은 분해율을 보였으며 구리, 알루미늄의 순으로 낮아졌다. 방전전극의 감은 횟수에 대한 영향은 7회, 9회, 11회의 순으로 감은 횟수가 많을수록 분해율이 높아짐을 알 수 있었다.

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