• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2232-2237
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• 2007

Steam reforming and catalytic reforming of $CH_4$ conversion to produce synthesis gas require both high temperatures and high pressure. Non-thermal plasma is considered to be a promising technology for the hydrogen rich gas production from methane. In this study, three phase AC GlidArc plasma system was employed to investigate the effects of gas composition, gas flow rate, catalyst reactor temperature and applied electric power on the $CH_4$ and $H_2$ yield and the product distribution. The studied system consisted of three electrode and it connected AC generate power system different voltages. In this study, air was used for the partial oxidation of methane. The results showed that increasing gas flow rate, catalyst reactor temperature, or electric power enhanced $CH_4$ conversion and $H_2$ concentration. The reference conditions were found at a $O_2$/C molar ratio of 0.45, a feed flow rate of 4.9 ${\ell}$/min, and input power of 1kW for the maximum conversions of $CH_4$ with a high selectivity of $H_2$ and a low reactor energy density.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2009년도 춘계학술대회 논문집
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• pp.731-734
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• 2009

KIER has been developed a compact and highly efficient fuel processor which is one of the key component of the residential PEM fuel cells system. The fuel processor uses methane steam reforming to convert natural gas to a mixture of water, hydrogen, carbon dioxide, carbon monoxide and unreacted methane. Then carbon monoxide is converted to carbon dioxide in water-gas-shift reactor and preferential oxidation reactor. A start-up time of the fuel processor is about 1h and CO concentration among the final product is maintained less than 5 vol. ppm. To achieve high thermal efficiency of 80% on a LHV basis, an optimal thermal network was designed. Internal heat exchange of the fuel processor is so efficient that the temperature of the reformed gas and the flue gas at the exit of the fuel processor remains less than $100^{\circ}C$. A compact design considering a mixing and distribution of the feed was applied to reduce the reactor volume. The current volume of the fuel processor is 17L with insulation.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2006년도 제32회 KOSCO SYMPOSIUM 논문집
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• pp.149-156
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• 2006

Structure of edge flame established in a mixing layer, formed between two uniformly flowing pure $CH_4$ and pure $O_2$ streams, is numerically investigated by employing a detailed methane-oxidation mechanism. The numerical results exhibited the most outstanding distinction of using pure oxygen in the fuel-rich premixed-flame front, through which the carbon-containing compound is found to leak mainly in the form of CO instead of HC compounds, contrary to the rich $CH_4-air$ premixed flames in which $CH_4$ as well as $C_2H_m$ leakage can occur. Moreover, while passing through the rich premixed flame, a major route for CO production, in addition to the direct $CH_4$ decomposition, is found to be $C_2H_m$ compound formation followed by their decomposition into CO. Beyond the rich premixed flame front, CO is further oxidized into $CO_2$ in a broad diffusion-flame-like reaction zone located around moderately fuel-rich side of the stoichiometric mixture by the OH radical from the fuel-lean premixed-flame front. Since the secondary CO production through $C_2H_m$ decomposition has a relatively strong reaction intensity, an additional heat-release branch appears and the resulting heat-release profile can no longer be seen as a tribrachial structure.

• 한국연소학회지
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• 제11권1호
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• pp.19-26
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• 2006

Structure of edge flame established in a mixing layer, formed between two uniformly flowing pure $CH_4$ and pure $O_2$ streams, is numerically investigated by employing a detailed methane-oxidation mechanism. The numerical results exhibited the most outstanding distinction of using pure oxygen in the fuel-rich premixed-flame front, through which the carbon-containing compound is found to leak mainly in the form of CO instead of HC compounds, contrary to the rich $CH_4-air$ premixed flames in which $CH_4$ as well as $C_2H_m$ leakage can occur. Moreover, while passing through the rich premixed flame, a major route for CO production, in addition to the direct $CH_4$ decomposition, is found to be $C_2H_m$ compound formation followed by their decomposition into CO. Beyond the rich premixed flame front, CO is further oxidized into $CO_2$ in a broad diffusion-flame-like reaction zone located around moderately fuel-rich side of the stoichiometric mixture by the OH radical from the fuel-lean premixed-flame front. Since the secondary CO production through $C_2H_m$ decomposition has a relatively strong reaction intensity, an additional heat-release branch appears and the resulting heat-release profile can no longer be seen as a tribrachial structure.

• 한국미생물·생명공학회지
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• 제45권3호
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• pp.185-199
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• 2017

메탄은 자연적인 발생원과 인위적인 발생원에 의해 배출되며 지구온난화를 야기하는 대표적인 온실가스이다. 메탄을 탄소원과 에너지원으로 이용하는 메탄산화세균은 메탄의 생물학적 산화에 중요한 역할을 한다. 메탄산화세균의 서식지는 매우 다양하며 메탄산화반응의 핵심 효소인 methane monooxygenases (MMOs)는 메탄뿐 아니라 다른 기질을 산화할 수 있는 기질특이성을 가지고 있다. 이러한 메탄산화세균의 특성으로 인해 생물학적 메탄 저감 기술과 생물정화기술 분야에서 메탄산화세균의 활용에 대한 연구가 활발히 진행되고 있다. 본 총설 논문에서는 메탄산화세균의 종류, MMOs의 특성과 메탄산화세균의 고농도 배양 기술에 관한 최근 정보를 정리하였다. 또한 메탄산화세균을 이용한 생물학적 메탄 저감 관련 실험실 규모와 매립지 현장에서의 기술 개발 현황 및 적용 결과를 소개하였다. 이러한 생물학적 메탄 저감 시스템에서 메탄산화세균의 군집 거동 특성도 고찰하였다. 마지막으로, 메탄산화세균을 활용한 생물공학기술의 혁신을 위해 필요한 과제로 대사활성이 우수하거나 신규 대사능력을 가진 메탄산화세균의 지속적인 탐색 연구, 고농도 세포 대량배양기술 개발 및 미생물 컨소시움(메탄산화세균과 비메탄산화세균의 컨소시움) 디자인 및 관리 기술 등이 필요함을 제안하였다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2008년도 춘계학술대회 논문집
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• pp.499-502
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• 2008

고정층반응기에서 니켈이 치환된 하이드로탈사이트($Ni_3Mg_3Al_2(CO_3)(OH)_{{16}{\cdot}n}H_2O$ ; n=3$\sim$5)를 합성하고 여기에 세리아를 첨가 후 소성하여 얻은 촉매를 사용하여($Ce_xNi_3$-HTlc ; x=0.3$\sim$1.2) 메탄의 부분산화 반응실험을 수행하였다. 세리아가 첨가되지 않은 촉매는 반응 초기 활성이 세리가가 소량 첨가된 ($Ce_{0.3}Ni_3$-HTlc) 촉매보다 우수하였으나 장시간 반응에서는 차차 활성이 저하되었으나, $Ce_{0.3}Ni_3$-HTlc의 활성은 30시간까지 일정하게 유지 되었다. 세리아 함량이 많아 질수록 촉매 활성은 점차 저하되었으며, $Ce_{1.2}Ni_3$-HTlc 는 촉매활성이 매우 낮았다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 추계학술대회 논문집
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• pp.85-88
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• 2007

고정층반응기에서 여러 가지 전이금속으로 치환된 하이드로탈사이트($[M_xMg_{6-x}Al_2(OH)_{16}(CO_3)^{2-}]{\cdot}H_2O;$ M: 전이금속(Ni, Mn, Co, Cu, Zn) x: 전이금속 치환비($x=0.5{\sim}6$))를 합성하고 이를 소성한 후 메탄의 부분산화 반응에 사용하였다. 반응 시 도입되는 $CH_4/O_2$비는 2로 하고 $VHSV=120,000cm^3/g$ h, 온도를 $500^{\circ}C$ 부터 $50^{\circ}C$ 간격으로 하여 $800^{\circ}C$까지 수행하였다. 실험결과 다른 전이금속들 중에서 니켈로 치환된 촉매가 대체적으로 부분산화반응을 촉진시키는데 좋은 것으로 나타났으며, 실험 결과 니켈의 hydrotalcite 중의 치환비(x)에 따른 차이는 별로 없었다.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2006년도 제32회 KOSCO SYMPOSIUM 논문집
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• pp.144-148
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• 2006

Characteristics of a plasma reactor for partial oxidation of methane, especially focused on the role and effectiveness of plasma chemistry, is investigated. Partial oxidation of methane is investigated using a rotating arc which is a three dimensional version of a typical glidingarc. The rotating arc has both the characteristics of equilibrium and non-equilibrium plasma. Non-equilibrium characteristics of the rotating gliding arc can be increased by rotating an elongated arc string attached at both the tip of inner electrode and the edge of outer electrode. In this way, plasma chemistry can be enhanced and hydrogen selectivity can reach almost 100% that is much higher than thermal equilibrium condition. As a result, the present study enables the strategic approach of the plasma reforming process by means of appropriate reactor design to maximize plasma effect and resulting in maximized reaction efficiency.

• KSBB Journal
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• 제13권5호
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• pp.483-490
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• 1998

Two unidentified methanotrophic strains (MM-white and MM-red) secreting soluble methane monooxygenase (sMMO) involved in thrichloroethylene biodegradation have been isolated from mixed methanotrophic consortium (MM) around Taejon area. Subsequently four methanotrophic strains were isolated from MM and named according to their color; white (MS-white), yellow (MS-yellow), pink (MS-pink) and reddish brown (MS-rbrown). All strains except MS-yellow which can take glucose as well as methane, metabolized methane as a sole carbon source. They all showed symbiotic behavior when methane was used as the sole carbon source. Optimum conditions of cell growth for MM were pH of 6.8 - 7.2, temperature of 29 - 32$^{\circ}C$, and gas flow rate of 6 (for methane), 40 (for air), and 4 ml/min (for carbon dioxide). The sMMO activity was expressed as naphthalene oxidation rate (${\mu}$mol/ mg protein/ hr). The sMMO activity for MM grown in flask culture with 1 ${\mu}$M of CuSO4 was 36, while it was 61 without copper. The activity for MM grown in the fermentor without CuSO4 was 1077, but is was 197 after reaction with 5 ppm of TCE. The methanotrophs showed significantly high sMMO activity despite the presence of 1 ${\mu}$M of CuSO4, although most of other strains already known could not express sMMO activity under this condition.

• Bulletin of the Korean Chemical Society
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• 제30권6호
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• pp.1368-1372
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• 2009