• Applied Chemistry for Engineering
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• v.18 no.1
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• pp.84-89
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• 2007

Direct decomposition of hydrocarbon (methane, propane) was studied using a thermal plasma to produce high purity hydrogen and carbon black. Thermodynamic equilibrium compositions were calculated based on the minimization of Gibb's free energy, and decomposition experiments were performed on the basis of calculation results. The purity of hydrogen was found to be depended strongly on the flow rate of hydrocarbon. The decomposition conditions for high purity hydrogen were investigated. The purity of hydrogen produced from methane decomposition was higher than that from propane. In the case of propane, it was investigated that by products such as methane, acetylene, and ethane etc., by radical recombination under thermal plasma were produced more than that of methane. Produced carbon blacks were characterized by material analyses, such as XRD, Raman spectroscopy, SEM, and particle size analysis. In both methane and propane decompositions, well-crystallized carbon blacks were produced and showed uniform and sphere-like morphologies. The size of carbon black synthesized from methane was observed to be smaller than that from propane.

• Journal of the Korea Organic Resources Recycling Association
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• v.11 no.4
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• pp.97-104
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• 2003

Hydrogen fermentation of food waste and sewage sludge was performed in serum bottles under various volatile solids(VS) concentrations(0.5~5.0%) and mixing ratios of two substrates(0:100-100:0, VS basis). Full quadratic equations, optimal conditions, and 90% acceptable conditions for hydrogen production potential and rate were obtained using cumulative methane production data and response surface methodology. The specific hydrogen production potential of food waste was higher than that of sewage sludge. However, hydrogen production potential increased as sewage sludge composition increased up to 13~19% at all the VS concentrations. The maximum specific hydrogen production potential of 122.9 mL/g $carbohydrate_{added}-COD$ was found at the waste composition of 87:13(food waste:sewage sludge) and the VS concentration of 3.0%. The relationship between carbohydrate concentration, protein concentration, and hydrogen production potential indicated that enriched protein by adding sewage sludge might enhance hydrogen production potential. The maximum specific hydrogen production rate was 111.2 mL $H_2/g$ VSS/h. Food waste and sewage sludge were, therefore, considered as a suitable main substrate and a useful auxiliary substrate, respectively, for hydrogen production.

• Korean Journal of Microbiology
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• v.21 no.3
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• pp.109-114
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• 1983

Physiological conditions for hydrogen evolution by Rhodopseudomonas sphaeroides K-7 are examined. Larger amount of molecular hydrogen was evolved at $30^{\circ}C$, pH6.8-7.0 under anaerobically illuminated condition of about 12, 000 lux by the organism. The heighest rates of hydrogen evolution were observed in the culture with the organic acids such as acetate, DL-lactate or DL-malate in media containing L-glutamate as a nitrogen source. Hydrogen was also evolved from glucose with the rate of $178.9\;{\mu}l/hr/mg$ cells (dry weight). When glucose was adopted a a sole carbon source, however, conside erable time lag of about 20hours was required for hydrogen evolution. The resting cells stored at $30^{\circ}C$ under argon maintained the rate of hydrogen evolution in nearly about 90% of initial one even 40 days of storation.

• Microbiology and Biotechnology Letters
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• v.20 no.4
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• pp.430-436
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• 1992

Hydrogen evolution by mixed fermentation of Clostn"dium butyn"cum and photosynthetic bacteria which were capable of consuming clostridial metabolites and evolving hydrogen was investigated. Acetate and butyrate formed from anaerobic clostridial fermentation were efficiently utilized by Rhodopseudomonas sPhaeroides K-7. For complete bioconversion of clostridial metabolites such as acetate and butyrate into hydrogen, mixed culture of both anaerobic organisms forming molecular hydrogen was performed. By the mixed culture, the yield of hydrogen production increased by 20 to 75% and the levels of clostridial metabolites such as acetate, butyrate decreased in the fermentation broth. Influence of cell mixing ratio. mixing time and inoculum level on hydrogen evolution by mixed culture were examined. And then cometabolic pattern compared with in pure culture was observed as time course.

• 전기의세계
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• v.29 no.11
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• pp.704-708
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• 1980

본고의 내용은 다음과 같다. 1. 연료로서의 수소 2. 수소의 생성법 3. 수소의 저장과 수송 4. 연구개발의 방향과 금후과제

• Journal of Radiation Protection and Research
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• v.22 no.2
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• pp.119-125
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• 1997

PHWR achieves high neutron economy by adopting heavy water as its moderator and coolant. On the other hand it permits much tritium generation, compared to LWR, due to the neutron capture reaction of deuterium in heavy water. Meanwhile in the reactor core, $^3He formed as the result of-decay of tritium, captures a thermal neutron and transforms to tritium again. The existing calculation models on tritium generation in PHWR neglect the contribution of $^3He$ in both moderator and coolant due to its relatively low solubility. However the neutron capture cross-section of $^3He$ is almost $1.6{\times}10^7$ times as large as that of deuterium. That means that the dissolved amount of 0.03 ppm of $^3He$ in heavy water is enough to generate the same amount of tritium as that generated by the deuterium of total heavy water in the system. This study dealt with the contribution of $^3He$ to tritium generation. As a sample case, the contribution of $^3He$ to the tritium generation in Wolsong #1 was evaluated and compared to the measured values. According to the result of this study, it is concluded that $^3He$ in coolant contributes very much to the tritium generation but that in moderator shows negligible effects due to the low solubility and $^4He$ cover gas. At the beginning of the plant operation, the contribution of $^3He$ is slightly greater than the measured value but agrees well with the measured as the operating time increases.

• Journal of Environmental Health Sciences
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• v.26 no.2
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• pp.1-5
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• 2000

연속형 혐기성처리 반응조에서 배양된 수소발생 슬러지를 이용하여 증온 조건에서 회분식 혐기성 처리방법으로 유기성 폐수로부터 전환되는 수소가스 및 대사산물들에 대한 연구를 수행하였다. 수소발생에 대한 기질로는 sucrose를 이용하였다. 처리과정에서 발생된 누적수소가스, 휘발성지방산(VFAs) 및 solvents는 Gompertz equation을 이용한 비선형회귀분석을 통하여 계산하였다. 처리과정 중 수소가스는 반응초기에 발생하였고, 발생된 가스내 수소가스가 차지하는 비율은 약 20%이었다. 반응 전과정에서 메탄가스는 발생하지 않았다. 비수소가스발생율은 sucrose 농도가 40 g/l일 때 0.956 ml/g VSs/h이었으며, sucrose 농도가 300g/l의 경우는 0.011 ml/g VSS/h이었다. 수소가 발생하는 기간 동안 VFAs의 생성은 acetate, butyrate의 순으로 높게 생성되었으나, propionate로의 전환은 발견되지 않았다. solvents의 경우 butanol이 가장 높게 발생하였다.

• Microbiology and Biotechnology Letters
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• v.18 no.1
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• pp.6-11
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• 1990

Hydrogen evolution from biomass-derived carbohydrates by some Clostridia and optimal culture conditions for hydrogen evolution were investigated. Among the organisms tested, Clostridium butyricum was efficient hydrogen producer with starch, xylan, pectin, cellobiose and xylose. In batch fermentation of Cl. butyricum, optimal conditions for hydrogen evolution were achieved at pH 7.0-8.5, 10-50 mM phosphate, and 2% (w/v) glucose. Total amount of molecular hydrogen evolved by the organism slightly increased at the presence of acetate (<150 mM) or butyrate (<20 mM) in the initial fermentation medium. Especially, in case of more than the above concentration of butyrate, growth and hydrogen evolution were dramatically inhibited. In the conditions were described here, 70 mmole of molecular hydrogen per mg of DCW was produced with 1%(w/v) glucose by the organism.

• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 2002.09a
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• pp.71-74
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• 2002

다고리방향족 탄화수소를 페놀에 적응된 미생물을 이용하여 분해하고자 하였다. 분리된 Stenotrophomons maltophilia는 나프탈렌과 페난스렌을 탄소원 및 에너지원으로 이용하였으며 10mg/$\ell$의 나프탈렌과 0.9mg/$\ell$의 페난스렌이 완전히 분해되는데 지체기후 약 2일과 3일이 소요되었다. 나프탈렌, 페난스렌의 분해시 중간생성물로 chromatography 상에 새로운 피크들이 생성되었으며, 이러한 중간생성물을 파악하여 다고리 방향족 탄화수소의 분해경로를 모색하고자 하였다.

• 한국신재생에너지학회:학술대회논문집
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• 2006.11a
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• pp.380-383
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• 2006

수소는 미래의 청정에너지원이다. 수소를 생산하는 효과적인 방법으로는 탄소계촉매를 이용하여 부탄을 분해하는 것이다. 촉매는 카본블랙이 사용되었으며, $500{\sim}1100^{\circ}C$의 온도 범위에서 열분해 반응과 촉매분해반응이 수행되었다. 열분해의 경우 온도가 증가함에 따라 전화율이 증가하여 $800^{\circ}C$에서 98.9%로 부탄이 거의 분해되었으며, $900^{\circ}C$ 이상의 온도에서는 전화율이 100%까지 도달하였다. 부탄 분해반응에서 기대되는 생성물은 메탄, 에틸렌, 에탄, 프로필렌, 프로판 등이다. $1000^{\circ}C$이상의 온도에서는 부탄 촉매 분해반응에서 거의 대부분 수소와 메탄만이 관찰되었다. 특히 $500-1100^{\circ}C$까지 온도가 증가하였을 때 수소의 생성율은 꾸준히 증가하는 것으로 확인되었고 촉매분해반응이 촉매를 사용하지 않은 열분해반응보다 온도가 증가함에 따라 수소의 선택도를 더욱 향상시켜 보다 많은 수소가 생성되었으며, 반응성 실험이 진행되는 동안 촉매의 비활성화는 관찰되지 않았다. 반응전후의 촉매의 특성을 분석하기 위해 TEM 및 SEM 분석을 하였다. 반응전의 촉매는 매끈한 모양이었으나 $1000-1100^{\circ}C$에서 반응후에는 표면에 돌기모양을 형성하는 것을 관찰할 수 있었다.