• 제목/요약/키워드: Hydrogen Yield

검색결과 478건 처리시간 0.022초

탑형 생물반응기에서 과산화수소 또는 유동화 입자를 이용만 Xanthan 발효의 산소공급 향상 (Inhanced Oxygen Supply of Xanthan Fermentations Using either Hydrogen Peroxide or Fluidized Particles in Tower Bioreators)

  • 서일순
    • KSBB Journal
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    • 제17권2호
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    • pp.142-147
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    • 2002
  • 기포탑 회분식 xanthan 발효에서 xanthan 생성속도와 분자량에 영향을 미치는 산소전달제한을 피하기 위하여 과산화수소수를 산소공금 보조수단으로 사용하였다. 과산화수소수 주 입은 xanthin 생성을 가역적으로 저해하였다. 반면이 직경 8 mm 유리구슬 유동화 입자는 기-액 산소전달속도를 증가시켜서 기-액-고 삼상유동충 생물반응기에서의 xanthan 발효는 기포탑 발효에 비하여 높은 단위균체량 당 xanthan 생성속도 및 점도수윤 그리고 반응기 공간-시간 수윤(space-time yield)을 보였다.

Reforming Tar from Biomass Gasification using Limonite and Dolomite as Catalysts

  • Kim, Hee-Joon;Kunii, Hiroo;Li, Liuyun;Shimizu, Tadaaki;Kim, Lae-Hyun
    • 에너지공학
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    • 제20권4호
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    • pp.298-302
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    • 2011
  • In this study, Catalytic reforming with vapor and biomass gasification was simultaneously performed in a same fixed bed reactor at $600-800^{\circ}C$. Light gases were produced from reformation of the tar (fuel gases) in biomass gasification by using limonite and dolomite, as catalysts. Hydrogen and carbon dioxide are main components in light gases. Hydrogen yields increased with temperature increasing in the range of $650-800^{\circ}C$, because the water shift reaction was promoted by catalyst. The yield of hydrogen gas was increased about 160% under catalyst with the mixture of limonite and dolomite comparing to limonite only.

일메나이트 상에서 물의 광분해에 의한 수소의 생성 (Hydrogen Formation by Photo-splitting of Water on Ilmenite)

  • 최임규;하백현
    • 태양에너지
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    • 제8권1호
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    • pp.49-56
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    • 1988
  • Thermally treated Korean ilmenite was characterized and used for water splitting to obtain hydrogen by photo-catalytic reaction. Experiments on specific surface area, X-ray diffraction and EDS showed that the formation of FeO, $Fe_2O_3$ and $TiO_2$ ilmenite crystal surface increased the specific surface area with maximum value, phase change of $TiO_2$ at $600^{\circ}C$ and hetrogeneity. The hydrogen evolved in caustic soda solution on these ilmenites indicated that there was a maximum yield point at about $600^{\circ}C$. This point was explained with the change of the surface area due to sintering of newly formed FeO, $Fe_2O_3$ and $TiO_2$, as well as crystal phase change of anatase to rutile at $600^{\circ}C$. Produced hydrogen increased also as the concentration of caustic soda, but become constant at the near 1N solution.

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HYDROGEN EMISSION SPECTRA OF QUIESCENT PROMINENCES

  • Kim, Kap-Sung
    • 천문학회지
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    • 제23권1호
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    • pp.71-82
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    • 1990
  • Theoretical calculations of the combined radiative transfer and statistical equilibrium equation including the charge-particle conservations have been earned out for a multilevel hydrogen atom in quiescent prominences. Cool and dense models show the steep changes of population and radiation field in the vicinity of the surface, while these physical quantities remain unchanged for models with temperature of 7,300K, regardless of total densities. Ionization rate of hydrogen atom related with metallic line formation varies in considerable amounts from the surface to the center of model prominences cooler than 6,300K. However, such cool models cannot release enough hydrogen line emissions to explain observed intensities. Prominence models with a temperature higher than 8,000K can yield the centrally reversed Lyman line profiles confirmed by satellite EUV observations. We find that queiscent prominence with a density between $2{\times}10^{11}$ and $10^{12}cm^{-3}$ should be in temperature range between 6,300K and 8,300K, in order to explain consistently observed H alpha, beta line emissions and $n_p/n_l$ ratio.

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SOFC 스택 적용 마이크로웨이브-매트릭스 개질기 개발 (Development of Microwave-Matrix Reformer for Applying SOFC Stack)

  • 안준;전영남
    • 한국수소및신에너지학회논문집
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    • 제32권6호
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    • pp.534-541
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    • 2021
  • In this study, a novel microwave-matrix reformer was proposed to convert CH4, which is a major component, to a high quality hydrogen energy. And to identify this performance, it was investigated for O2/C ratio, steam feed amount and reformed gas recirculation which are affected for methane conversion and product gas yield. Through the parametric screening studies, optimal operating conditions were that O2/C ratio, steam feed amount and recirculation rate were 1.1, 10 mL/min and 30 L/min. In this conditions, CH4 conversion was 68.1%, H2 selectivity 77.2 and H2/CO ratio 2.62 which are possible applying SOFC stack for RPG (residential power generator).

수소 생산을 위한 Cu/ZnO/Al2O3 촉매상에서 DME의 수증기 개질 반응 연구 (A Study on the Steam Reforming Reaction of DME on Cu/ZnO/Al2O3 Catalyst for Hydrogen Production)

  • 변현승;구윤지;오주희;반재성;나영진;이제설;조원준
    • 한국수소및신에너지학회논문집
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    • 제34권6호
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    • pp.581-586
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    • 2023
  • As the development of alternative energy is required due to the depletion of fossil fuels, interest in the use of hydrogen energy is increasing. Hydrogen is a promising clean energy source with high energy density and can lead to the application of environmentally friendly technologies. However, due to difficulties in production, storage, and transportation that prevent the application of hydrogen-based eco-friendly technology, research on reforming reactions using dimethyl ether (DME) is being conducted. Unlike other hydrocarbons, DME is attracting attention as a hydrogen carrier because it has excellent storage stability and transportability, and there is no C-C bond in the molecule. The reaction between DME and steam is one of the reforming processes with the highest hydrogen yield in theory at a temperature lower than that of other hydrocarbons. In this study, a hydrogen reforming device using DME was developed and a catalyst prepared by supporting Cu in alumina was put into a reactor to find optimal hydrogen production conditions for supplying hydrogen to fuel cells while changing reaction temperature (300-500℃), pressure (5-10 bar), and steam/carbon ratio (3:1 to 5:1).

아임계 및 초임계수를 이용한 Athabasca 오일샌드의 추출 (Extraction of Athabasca Oil Sand with Sub- and Supercritical Water)

  • 박정훈;손수환;백일현;남성찬
    • Korean Chemical Engineering Research
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    • 제47권3호
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    • pp.281-286
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    • 2009
  • 아임계 및 초임계 조건의 물을 이용하여 캐나다산 Athabasca 오일샌드로부터 역청 추출 및 황 제거 실험을 수행하였다. 0~120 min의 반응시간, 360, $380^{\circ}C$의 온도, 15~30 MPa의 압력 및 $0.074{\sim}0.61g/cm^3$의 물 밀도를 변화시키면서 micro reactor에서 역청 수율을 조사하였다. 역청 수율은 온도에 상관없이 압력이 증가할수록 증가하였으며, 특히 초임계 영역에서 수증기 개질반응에 의해 생성된 수소에 의해 역청의 수율이 급격히 증가하였다. 전체 기상 생성량은 압력 증가에 따라 감소하였으나 $380^{\circ}C$에서 황과 수소의 생성분율은 25 및 30 MPa로 압력 증가에 따라 소량 증가하였다. 이상의 결과는 초임계 조건이 수소의 생성과 황의 제거에 유리하다는 것을 보여준다. 초임계 조건$380^{\circ}C$, 25와 30 MPa)에서 역청 수율은 최대 약 22%였으며, 오일샌드에 함유된 황 제거율도 최대값 40%에 도달하였다.

산업공정의 폐수처리에서 발생된 폐활성슬러지 및 인공음식폐기물을 이용한 생물학적 수소생성에 관한 연구 (Study on Bio-H2 Production from Synthetic Food Waste and Activated Sludge from Industrial Waste Water Processes using Dark-fermentation)

  • 김태형;김미형;이명주;황선진;엄형춘
    • 상하수도학회지
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    • 제24권6호
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    • pp.703-712
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    • 2010
  • This study performed to extract operation factors of major organic wastes, which were food wastes and waste activated sludge generated in industries in order to use them as a substrate for bio-H2 production. According to the results of experimental analysis for hydrogen production capacity by various organic concentrations, the hydrogen production yield was the highest at 80 g/L, and the efficiency was improved by the pretreatment of waste activated sludge (acid treatment, alkali treatment). Hydrogen production efficiency was improved by mixing food wastes and waste activated sludge if waste activated sludge was below than 30%, however, it was decreased when it was more than 50%. The impacts of heavy metals on the hydrogen production shows that the inhibition level depends on the concentration of Cr, Zn, and Cu, Fe was able to enhance the hydrogen production.

다공성 폼에 코팅된 $CeO_2/ZrO_2$ 를 이용한 고온 태양열 합성가스 및 수소 생산 연구 (Syngas and Hydrogen Production from $CeO_2/ZrO_2$ coated Foam Devices under Simulated Solar Radiation)

  • 장종탁;윤기준;한귀영
    • 한국태양에너지학회:학술대회논문집
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    • 한국태양에너지학회 2012년도 춘계학술발표대회 논문집
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    • pp.260-266
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    • 2012
  • Syngas and hydrogen from the $CeO_2/ZrO_2$ coated foam devices were investigated under simulated solar radiation. The $CeO_2/ZrO_2$ coated SiC, Ni and Cu foam device were prepared using drop-coating method. Syngas production step was performed at $900^{\circ}C$, and hydrogen production process was performed for ten repeated cycles to compare the CeO2 conversion in syngas production step, $H_2$ yield in hydrogen production step and cycle reproducibility. The produced syngas had the $H_2$/CO ratio of 2, which was suitable for methanol synthesis or Fischer-Tropsch synthesis process. In addition, syngas and hydrogen production process is one of the promising chemical pathway for storage and transportation of solar heat by converting solar energy to chemical energy. After ten cycles of redox reaction, the $CeO_2/ZrO_2$ was analyzed using XRD pattern and SEM image in order to characterize the physical and chemical change of metal oxide at the high temperature.

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열처리 시간과 pH 하한값이 음식물쓰레기 연속 중온 수소 발효에 미치는 영향 (Effects of Pretreatment Time and pH low set value on Continuous Mesophilic Hydrogen Fermentation of Food Waste)

  • 김상현;이채영
    • 상하수도학회지
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    • 제25권3호
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    • pp.343-348
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    • 2011
  • Since 2005, food waste has been separately collected and recycled to animal feed or aerobic compost in South Korea. However, the conventional recycling methods discharge process wastewater, which contain pollutant equivalent to more than 50% of food waste. Therefore, anaerobic digestion is considered as an alternative recycling method of food waste to reduce pollutant and recover renewable energy. Recent studies showed that hydrogen can be produced at acidogenic stage in two-stage anaerobic digestion. In this study, the authors investigated the effects of pretreatment time and pH low set value on continuous mesophilic hydrogen fermentation of food waste. Food waste was successfully converted to $H_2$ when heat-treated at $70^{\circ}C$ for 60 min, which was milder than previous studies using pH 12 for 1 day or $90^{\circ}C$. Organic acid production dropped operational pH below 5.0 and caused a metabolic shift from $H_2/butyrate$ fermentation to lactate fermentation. Therefore, alkaline addition for operational pH at or over 5.0 was necessary. At pH 5.3, the result showed that the maximum hydrogen productivity and yield of 1.32 $m^3/m^3$.d and 0.71 mol/mol $carbohydrate_{added}$. Hydrogen production from food waste would be an effective technology for resource recovery as well as waste treatment.