• 제목/요약/키워드: sulfur oxidation

검색결과 230건 처리시간 0.023초

다양한 생태계에서 분리한 황 산화 세균 (Isolation of Sulfur Oxidizing Bacteria from Different Ecological Niches)

  • ;;;;;최관호;사동민
    • 한국토양비료학회지
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    • 제38권4호
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    • pp.180-187
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    • 2005
  • 다양한 인도 토양에서 Starkey's 배지를 이용하여 9종류의 화학합성독립영양 및 12종류의 화학합성종속영양 황산화 세균을 분리하였다. 분리한 세균은 황을 황산으로 산화시키는 기능이 있으며 생육 중 배지의 산도를 감소시켰다. 분리한 황 산화 세균은 혐기 조건에서는 생육하지 못했다. 화학합성독립영양세균 SGA6 및 JIG 2종만이 포도당을 이용하는 능력이 있었으며, LCH 1종을 제외한 모든 분리세균은 thiosulfate를 에너지원으로 이용하였다. 분리한 세균 중 황 산화 능력이 가장 우수한 것은 화학합성독립영향세균인 LCH이었으며 화학합성종속영향세균인 JIG의 황 산화 능력이 가장 낮았다. 분리한 황 산화 세균을 이용하여 점토를 이용하여 입제형태로 만들었을 때 균의 밀도는 약 $2.5{\times}10^7cfu\;g^{-1}$ 이었다.

고체산화물 연료전지의 운전 조건에 따른 니켈 전극 황 피독 현상 (Sulfur Poisoning of Ni Anode as a Function of Operating Conditions in Solid Oxide Fuel Cells)

  • 이호성;이현미;임형태
    • 대한금속재료학회지
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    • 제56권12호
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    • pp.893-899
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    • 2018
  • In the present study, we investigated the sulfur poisoning of the Ni anode in solid oxide fuel cells (SOFCs) as a function of operating conditions. Anode supported cells were fabricated, and sulfur poising tests were conducted as a function of current density, $H_2S$ concentration and humidity in the anode gas. The voltage drop was significant under the higher current density (${\sim}714mA/cm^2$) condition, while it was much reduced under the lower current density (${\sim}389mA/cm^2$) condition, at 100 ppm of $H_2S$. A secondary voltage drop, which occurred only at the high current density, was attributed to Ni oxidation in the anode. Thus, operation at high current density with high $H_2S$ concentration may lead to permanent deterioration in the anode. The effect of water content (10%) on the sulfur poisoning was also investigated through a constant current test (${\sim}500mA/cm^2$) at 10 ppm of $H_2S$. The cell operating with 10% wet anode gas showed a much smaller initial voltage drop, in comparison with a dry anode gas. The present study indicates that operating conditions, such as gas humidity and current density, should be carefully taken into account, especially when fuel cells are operated with $H_2S$ containing fuel.

Sulfur Tolerance Effects on Sr0.92Y0.08Ti0.5Fe0.5O3-δ as an Alternative Anode in Solid Oxide Fuel Cells

  • Kim, Jun Ho;Yun, Jeong Woo
    • Journal of Electrochemical Science and Technology
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    • 제9권2호
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    • pp.133-140
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    • 2018
  • $Sr_{0.92}Y_{0.08}Ti_{0.5}Fe_{0.5}O_{3-{\delta}}$ (SYTF0.5) is investigated as an alternative anode in $H_2$ fuels containing $H_2S$ (0-200 ppm). Although additional ionic conductivity is introduced by aliovalent substitution of $Ti^{4+}$ by $Fe^{3+}$ in the B-site, the SYTF0.5 has lower electrical conductivity than that of the $Sr_{0.92}Y_{0.08}TiO_{3-{\delta}}$. Due to the mixed ionic and electronic conductive (MIEC) property exhibited in the SYTF0.5 anode, the electrochemical performance of the SYTF0.5 anode is improved, as well as the sulfur tolerance. The maximum power densities in $H_2$ at $900^{\circ}C$ for the SYT anode and the SYTF0.5 anode were 56.9 and $98.6mW/cm^2$, respectively. The maximum power density in the SYTF0.5 anode at 200 ppm of $H_2S$ concentration decreased by only 12.9% (86.3 to $75.2mW/cm^2$).

2-Amino-1-cyclopentene-1-dithiocarboxylate 유도체들의 전극 반응메카니즘 (Mechanistic Investigation of Redox Process of 2-Amino-1-cyclopentene-1-dithiocarboxylate derivatives)

  • 김영신;김우성;심윤보;최성락
    • 대한화학회지
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    • 제34권3호
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    • pp.260-266
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    • 1990
  • N-methyl-2-amino-l-cyclopentene-l-dithiocarboxylic acid $(N-CH_3 acdc)$ 와 2-amino-l-cyclopentene-l-dithiomethyl ester $(S-CH_3 acdc)$의 전기화학적 거동을 직류폴라로그래피, 순환전압전류법 및 조절전위 전기량법을 사용하여 dimethylformamide(DMF) 용매 중에서 조사하였다. $N-CH_3$ acdc의 이합체는 + 0.98 V에서 2전자 산화반응을 거쳐 s가 한 원자 유리된 다섯 원자 고리를 형성하는 전극반응이 일어남을 알았다. 그러나, $S-CH_3 acdc의 경우에 있어서는 N-CH_3 acdc화합물과는 달리 다섯원자 고리를 형성하지 않았으므로 N-CH_3$ acdc와는 다른 전극반응을 일으킴을 확인하였다.

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일정전류 비평행교류브릿지에 의한 전도도측정과 황의 정량 (An Unbalanced A.C. Bridge with High Voltage Source for the Conductometric Determination of Sulfur in Iron Ores)

  • 채명준;최규원
    • 대한화학회지
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    • 제14권4호
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    • pp.327-332
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    • 1970
  • A simple and convenient device for deflection-type direct reading the variations in electrolytic conductance is described and applied to the analysis of sulfur by combustion-$H_2O_2$ oxidation method. The apparatus consisted of a high resistance-ratio bridge in which the other adjacent arms are the differential cells. By adopting unusually high a-c voltage source for the bridge excitation, the a-c method for unbalanced bridge is established, decreased sensitivity owing to reduced bridge factor, 0.01, is overcome and also the absolute sensitivity and linearity are greatly improved. Over 50% variations in impedance of the balanced cell, within 1% deviation from the linearity can be attained with a volt (rms)order of output which was detected directly with VTVM without further amplification. Analysis of the bridge shows that these useful features are natural result of the constant current character of the high source impedance generator and the performance of the device agreed with the theoretical predictions. A standard procedure for the rapid analysis of sulfur using the bridge is also given, the analytical accuracy was approximately 1%. A determination takes not more than 5 minutes.

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하수관거에 퇴적된 유기물에 의한 악취 발생과 산화전리시스템을 이용한 악취 저감 (Odor Emission from Sediments in Sewer Systems and Odor Removal using an Electrolytic Oxidation Process)

  • 안해영;신승규;송지현
    • 한국대기환경학회지
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    • 제27권6호
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    • pp.703-710
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    • 2011
  • Odor emission from domestic sewer systems has become a serious environmental problem. An investigation on a sewer manhole revealed that anaerobic decay of sediment organic matters (SOMs) and related declines of oxidation reduction potential (ORP) in the sediment layer were the main reason of the production of volatile sulfur compounds. In addition, as the anaerobic decaying period continued, the odor intensity rapidly increased with increasing concentrations of $H_2S$ and dimethyl sulfide. As a feasible method to control SOMs and to minimize odor emission potentials, an electrolytic oxidation process has been employed to the sediment sludge phase. In this study, voltages applied to the electrolytic oxidation process were varied as a main system parameter, and its effects on odor removal efficiencies and reaction characteristics were investigated. At the applied voltages greater than 20 V, the system efficiently oxidized the organic matter, and the ORP in the sludge phase increased rapidly. As a consequence, the removal efficiency of hydrogen sulfide was found to be >99% within 60 minutes of the electrolytic oxidation. Overall, the electrolytic oxidation process can be an alternative to control odor emission from sewer systems, and a threshold input energy needs to be determined to achieve effective operation of the process.

산화주석 얇은 막 전극에서의 이산화황 산화반응 (Electrochemical Oxidation of Sulfur Dioxide on Tin Oxide Thin Film Electrode)

  • 홍종인;백운기;김하석
    • 대한화학회지
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    • 제29권2호
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    • pp.172-177
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    • 1985
  • 안티몬이 첨가된 산화주석 얇은막 전극의 반도체적 성질을 조사하고 이산화황의 산화반응에 대한 이 전극의 전기화학적 촉매작용을 여러가지 조건하에서 조사하였다. $SO_2$(또는 아황산염)를 포함하는 전해질 용액의 pH가 증가함에 따라 점차로 낮은 전위에서 산화가 일어났으며 이 전극은 염기성 용액에서 $SO_3^=$의 산화에 대하여 뚜렷한 전기촉매 작용을 나타내었으며 이 전기촉매 작용은 백금이나 팔라듐 전극의 촉매작용과는 다른 특성을 보여주었다. 백금이나 팔라듐이 이 전극에 첨가된 경우에는 이들 금속이 전극표면에 노출된 양에 비례하는 효과만이 나타났다.

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黃化鑛의 液相酸化 (第1報) 亞鉛鑛의 암모니아溶液中에서의 濕式酸化 (Aqueous oxidation of sulfide ore (part 1) Aqueous Oxidation of Marmatite in Ammonia Solution)

  • 김동선;장태성;이용복
    • 대한화학회지
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    • 제10권2호
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    • pp.54-58
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    • 1966
  • 암모니아 溶液中에서 濕式酸化에 의하여 亞鉛鑛으로부터 亞鉛 및 黃을 抽出하였다. 암모니아의 濃度는 酸化率에 미치는 影響이 至大하여 反應溫度 및 濃度가 낮을 때는 亞鉛이 黃보다 浸出率이 低下함을 알았다. 그 含有量에 대하여 最高 Zn은 55%, S는 50% 浸出이 可能하였고 이 때의 條件은 다음과 같다. 加壓壓力;$4.2kg/cm_2$, 濃度; $60^{\circ}C$ 溶媒濃度;25%$NH_3$-sa-sol, 粒度;270mesh, 時間;20hr.

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Selective Oxidation of Hydrogen Sulfide to Elemental Sulfur with Fe/MgO Catalysts in a Slurry Reactor

  • Lee, Eun-Ku;Jung, Kwang-Deog;Joo, Oh-Shim;Shul, Yong-Gun
    • Bulletin of the Korean Chemical Society
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    • 제26권2호
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    • pp.281-284
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    • 2005
  • The Fe/MgO catalysts with different Fe loadings (1, 4, 6, 15 and 30 wt% Fe) were prepared by a wet impregnation with iron nitrate as precursor. All of the catalysts were characterized by BET surface analyzer, X-ray diffraction (XRD), temperature-programmed reduction (TPR), and X-ray photoelectron spectroscopy (XPS). The maximum removal capacity of $H_2S$ was obtained with 15 wt% Fe/MgO catalyst which had the highest BET surface area among the measured catalysts. XRD of Fe/MgO catalysts showed that well dispersed Fe particles could be present on Fe/MgO with Fe loadings below 15 wt%. The crystallites of bulk $\alpha$-$Fe_2O_3$ became evident on 30 wt% Fe/MgO, which were confirmed by XRD. TPR profiles showed that the reducibility of Fe/MgO was strongly related to the loaded amounts of Fe on MgO support. Therefore, the highest removal efficiency of $H_2S$ in wet oxidation could be ascribed to a good dispersion and high reducibility of Fe/MgO catalyst. XPS studies indicated that the $H_2S$ oxidation with Fe/MgO could proceed via the redox mechanism ($Fe^{3+}\;{\leftrightarrow}\;Fe^{2+}$).

Electrooxidation of tannery wastewater with continuous flow system: Role of electrode materials

  • Tien, Tran Tan;Luu, Tran Le
    • Environmental Engineering Research
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    • 제25권3호
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    • pp.324-334
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    • 2020
  • Tannery wastewater is known to contain high concentrations of organic compounds, pathogens, and other toxic inorganic elements such as heavy metals, nitrogen, sulfur, etc. Biological methods such as aerobic and anaerobic processes are unsuitable for tannery wastewater treatment due to its high salinity, and electrochemical oxidation offers a promising method to solve this problem. In this study, raw tannery wastewater treatment using DSA® Ti/RuO2, Ti/IrO2 and Ti/BDD electrodes with continuous flow systems was examined. Effects of current densities and electrolysis times were investigated, to evaluate the process performance and energy consumption. The results showed that a Ti/BDD electrode is able to reach higher treatment efficiency than Ti/IrO2, and Ti/RuO2 electrodes across all parameters, excluding Total Nitrogen. The main mechanism of tannery wastewater oxidation at a Ti/BDD electrode is based on direct oxidation on the electrode surface combined with the generation of oxidants such as °OH and Cl2, while at DSA® Ti/RuO2 and Ti/IrO2 electrodes, the oxidation mechanisms are based on the generation of chlorine. After treatment, the effluents can be discharged to the environment after 6-12 h of electrolysis. Electrooxidation thus offers a promising method for removing the nutrients and non-biodegradable organic compounds in tannery wastewater.