• Title/Summary/Keyword: hydrogen purification

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Oxygen Removal Performance of M/γ-Al2O3 Catalyst through H2-O2 Recombination Reaction and the Effect of Oxygen Vacancies on the Catalyst (H2-O2 재결합 반응을 통한 M/γ-Al2O3 촉매의 산소 제거 성능과 산소 결손이 촉매에 미치는 영향)

  • TAEJUN KIM;PUTRAKUMAR BALLA;DAESEOB SHIN;YOUJUNG SONG;SUNGTAK KIM
    • Transactions of the Korean hydrogen and new energy society
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    • v.34 no.5
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    • pp.535-548
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    • 2023
  • The intermittent nature of renewable energy is a challenge to overcome for safety and stable performance in water electrolysis systems linked to renewable energy. Oxygen removal using the catalyst is suitable for maintaining the oxygen concentration in hydrogen below the explosive level (4%) even in intermittent power supply. Metals such as Pd, Pt, and Ni are expected to be effective materials due to their hydrogen affinity. The oxygen removal performance was compared under high hydrogen concentration conditions by loading on γ-Al2O3 with high reactivity and large surface area. The characteristics of the catalyst before and after the reaction were analyzed through X-ray diffraction, transmission electron microscope, H2-temperature programmed reduction, X-ray photoelectron spectroscope, etc. The Pd catalyst that showed the best performance was able to lower 2% oxygen to less than 5 ppm. Changes in catalyst characteristics after the reaction indicate that oxygen vacancies are related to oxygen removal performance and catalyst deactivation.

Production of Bacteriocins by Strains of Lactobacillus acidophilus from Different Animal Origins

  • Kim, Sae-Hun
    • 한국유가공학회:학술대회논문집
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    • 1996.11a
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    • pp.30-34
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    • 1996
  • Twenty seven strains of Lactobacillus acidophilus among 92 isolated from fecal contents of humans, pigs, calves, chickens, rodents and turkeys demonstrated inhibitory attributed to bacteriocin(s). The bacteriocin(s) were heat stable and nondialyzable proteinous compounds and exhibited narrow inhibitory spectra of activity. Neither hydrogen peroxide nor low pH were responsible for inhibitory action. All of the producer strains were resistant to their own bacteriocin or bacteriocin(s) produced by other strains. The bacteriocins from several strains from different host species were purified for further characterization. The bacteriocin(s) all exhibited similar characteristics.

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Experimental and Theoretical study of H2 Separation Using PSA Process (PSA를 이용한 수소분리 실험과 이론에 관한 연구)

  • Chol, Byoung-Uk;Hong, Sung-Chul;Choi, Dae-Ki;Lee, Byung-Gwon;Baek, Young-Soon;Lee, Chang-Ha
    • Transactions of the Korean hydrogen and new energy society
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    • v.14 no.1
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    • pp.81-95
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    • 2003
  • 본 연구는 압력균등화 공정이 추가된 2 컬럼 6 스뎁의 활성탄 PSA공정을 이용하여 비단열, 비등은 조건에서 메탄(80%)과 수소(20%)의 2성분계로부터 수소분리에 관한 연구이다. 공급가스의 압력, 흡착시간, 공급속도와 P/F 비율이 PSA공정에 미치는 영향에 대하여 평가했고 전산모사를 통해 최적조건을 구했다. 전산모사에 의한 최적 조건은 공급속도 17 LPM, 흡착압력 11 atm, P/F 비율이 0.07~0.1로 나타났으며, 이 조건으로부터 순도 99%, 회수율 85% 이상의 수소가스를 얻을 수 있었다.

Formation of Mixed Oxidants and Inactivation of E. coil by the Electrochemical Process using a Grid Shape Pt/Ti Electrode (Pt/Ti 격자형 평판 전극을 이용한 혼합 산화제 생성 및 E. coli 불활성화)

  • Jung, Yeon Jung;Oh, Byung Soo;Park, Sang Yeon;Baek, ko Woon;Kang, Joon-Wun
    • Journal of Korean Society on Water Environment
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    • v.22 no.5
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    • pp.851-855
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    • 2006
  • The aim of this study was to investigate characteristics of formation of mixed oxidants and some aspects of the performance of electrochemical process as an alternative disinfection strategy for water purification. The study of electrochemical process has shown free chlorine to be produced, but smaller amounts of stronger oxidants, such as ozone, hydrogen peroxide and OH radicals, were also generated. The formation of ozone and hydrogen peroxide increased with increasing electric conductivity, but was limited at conductivities greater than 0.6 mS/cm. Also, formation of OH radical was enhanced as electric conductivity was increased to 0.9 mS/cm and The stead-state concentrations of OH radical were calculated at $1.1{\sim}6.4{\times}10^{-14}M$. Using E. coti, inactivation kinetic studies were performed. With the exception of free chlorine, the role of mixed oxidants, especially OH radical, was investigated for enhancement of the inactivation rate.

Hydrogen Production Using Membrane Reactors

  • Giuseppe Barbieri;Paola Bernardo;Enrico Drioli;Lee, Dong-Wook;Sea, Bong-Kuk;Lee, Kew-Ho
    • Korean Membrane Journal
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    • v.5 no.1
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    • pp.68-74
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    • 2003
  • Methane steam reforming (MSR) reaction for hydrogen production was studied in a membrane reactor (MR) using two tubular membranes, one Pd-based and one of porous alumina. A higher methane conversion than the thermodynamic equilibrium for a traditional reactor (TR) was achieved using MRs. The experimental temperature range was 350-500$^{\circ}C$; no sweep-gas was employed during reaction tests to avoid its back-permeation through the membrane and the steam/methane molar feed ratio (m) varied in the range 3.5-5.9. The best results (the difference between the MR conversion and the thermodynamic equilibrium was of about 7%) were achieved with the alumina membrane, working with the highest steam/methane ratio and at 450$^{\circ}C$. Silica membranes prepared at KRICT laboratories were characterized with permeation tests on single gases (N$_2$, H$_2$ and CH$_4$). These membranes are suited for H$_2$ separation at high temperature.

Technical Trends of Hydrogen Production (수소생산 기술동향)

  • Ryi, Shin-Kun;Han, Jae-Yun;Kim, Chang-Hyun;Lim, Hankwon;Jung, Ho-Young
    • Clean Technology
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    • v.23 no.2
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    • pp.121-132
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    • 2017
  • The increase of greenhouse gases and the concern of global warming instigate the development and spread of renewable energy and hydrogen is considered one of the clean energy sources. Hydrogen is one of the most elements in the earth and exist in the form of fossil fuel, biomass and water. In order to use hydrogen for a clean energy source, the hydrogen production method should be eco-friendly and economic as well. There are two different hydrogen production methods: conventional thermal method using fossil fuel and renewable method using biomass and water. Steam reforming, autothermal reforming, partial oxidation, and gasification (using solid fuel) have been considered for hydrogen production from fossil fuel. When using fossil fuel, carbon dioxide should be separated from hydrogen and captured to be accepted as a clean energy. The amount of hydrogen from biomass is insignificant. In order to occupy noticeable portion in hydrogen industries, biomass conversion, especially, biological method should be sufficiently improved in a process efficiency and a microorganism cultivation. Electrolysis is a mature technology and hydrogen from water is considered the most eco-friendly method in terms of clean energy when the electric power is from renewable sources such as photovoltaic cell, solar heat, and wind power etc.

Fermentative Water Purification based on Bio-hydrogen (생물학적 수소 발효를 통한 수처리 시스템)

  • Lee, Jung-Yeol;Chen, Xue-Jiao;Min, Kyung-Sok
    • Journal of Korean Society on Water Environment
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    • v.27 no.6
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    • pp.926-931
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    • 2011
  • Among various techniques for hydrogen production from organic wastewater, a dark fermentation is considered to be the most feasible process due to the rapid hydrogen production rate. However, the main drawback of it is the low hydrogen production yield due to intermediate products such as organic acids. To improve the hydrogen production yield, a co-culture system of dark and photo fermentation bacteria was applied to this research. The maximum specific growth rate of R. sphaeroides was determined to be $2.93h^{-1}$ when acetic acid was used as a carbon source. It was quite high compared to that of using a mixture of volatile fatty acids (VFAs). Acetic acid was the most attractive to the cell growth of R. sphaeroides, however, not less efficient in the hydrogen production. In the co-culture system with glucose, hydrogen could be steadily produced without any lag-phase. There were distinguishable inflection points in the accumulation of hydrogen production graph that resulted from the dynamic production of VFAs or consumption of it by the interaction between the dark and photo fermentation bacteria. Lastly, the hydrogen production rate of a repeated fed-batch run was $15.9mL-H_2/L/h$, which was achievable in the sustainable hydrogen production.

Demonstration of MCFC Power Plant on Fuels (연료에 따른 MCFC발전 실증연구)

  • Lee, Jong-Gyu;Jun, Jae-Ho;Park, Kyu-Ho;Choi, Doo-Sung;Park, Jae-Young
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.06a
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    • pp.117-120
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    • 2007
  • Fuel cells are currently attracting tremendous interest because of their huge potential in stationary applications, in terms of substantiality of our energy use. They also offer environmental advantages, combining significantly higher efficiency with very much lower emission of SOx, NOx, and residual hydrocarbons, and significantly reduced $CO_{2}$ emissions compared to conventional power generation. The molten carbonate fuel cell (MCFC) was introduced from Fuel Cell Energy(FCE), which the one MCFC was operating by LNG and the other was operating by ADG. The ADG contains normally CH4, CO2 and various impurities such as sulfur compounds and siloxanes. Using the ADG as a fuel, MCFC have the potential to provide significant environmental and economic benefits. However, such impurities would be harmful to fuel cells. In this work, a purification process for the ADG was designed and installed in order to utilize the gas as a fuel for MCFC.

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Purification and Characterization of Manganese Superoxide Dismutase from Staphylococcus sciuri

  • Song, Chi-Hyun;Park, Eun-Kyung;Suh, Hyung-Joo;Lee, Yong-Se;Choi, Jang-Won;Ra, Kyung-Soo
    • Journal of Microbiology and Biotechnology
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    • v.9 no.3
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    • pp.271-275
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    • 1999
  • The intracellular superoxide dismutase (SOD) from Staphylococcus sciuri was isolated to homogeneity by continuous steps, including ammonium sulfate fractionation, DEAE-ion-exchange chromatography, gel filtration, and phenyl hydrophobic gel chromatography. Pure SOD had a specific activity of 4,625 U/mg and was purified 158-fold with a yield of 31 % from a cell free extract. The molecular weight of the purified SOD was determined to be approximately 35.5 kDa by gel filtration and the enzyme was also shown to be composed of dimeric subunits on denaturing SDS-PAGE. The enzyme activity remained stable at pH 5 to 11 and also to heat treatment of up to $50^{\circ}C$ at pH 7.8, with 80% relative activity. The enzyme was insensitive to cyanide, hydrogen peroxide, and azide, indicating that it is a manganese-containing SOD. The EPR spectrum showed the enzyme containing manganese as a cofactor.

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Purification and Characterization of Iron-Containing Superoxide Dismutase from Lentinus edodes

  • Park, Sang-Shin;Hwang, Soo-Myung
    • Journal of Microbiology and Biotechnology
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    • v.9 no.6
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    • pp.854-860
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    • 1999
  • Superoxide dismutase (SOD) was purified to homogeneity from fruiting bodies of edible mushroom, Lentinus edodes, by ammonium sulfate precipitation, diethylaminoethyl (DEAE)-Sepharose FF ion-exchange chromatography, Sephacryl S-200 gel filtration chromatography, and preparative PAGE. The molecular weight of the purified enzyme was estimated to be approximately 54 kDa by gel filtration chromatography, and the enzyme was shown to be consisted of two identical subunits of molecular weight 27 kDa by SDS-PAGE. The isoelectric point of the enzyme was 4.9 as determined by isoelectric focusing. The enzyme had optimal pH and temperature of pH 8.0 and $20^{\circ}C$, respectively. The activity of the enzyme was inhibited by hydrogen peroxide, but inhibited less by cyanide and azide. The native enzyme was found to contain 0.89g-atom of iron, 0.75g-atom of zinc, and 0.46g-atom of copper per mol of enzyme. Analysis of amino acids composition revealed that the SOD from L. edodes contained a relatively large amount of glutamic acid/glutamine, proline, cysteine, isoleucine, and leucine, but only a small amount of aspartic acid/asparagine, tyrosine, and tryptophan when compared to the other iron-containing SODs.

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