• 제목/요약/키워드: Electrochemical reduction analysis

검색결과 153건 처리시간 0.018초

Electrochemical Study on the Coumarin Derivatives

  • Kim, Il Kwang;Chun, Hyun Ja;Paik, Soon Ok;Park, Sung Woo
    • 분석과학
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    • 제8권4호
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    • pp.655-661
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    • 1995
  • The electrochemical reduction of coumarin derivatives in 0.1M TEAP acetonitrile solution was investigated by the direct current, differential pulse polarography, cyclic voltammetry and controlled potential coulometry. The electrochemical reduction of 7-acetoxy-4-bromomethyl-coumarin(ABMC) was proceeded as an irreversible three steps(-0.58, -1.63 and -2.25 volts) of electrochemical transfer before chemical reaction. The solution color turned to yellow after the carboxyl group was reduced at 2nd step(-1.63 volts vs. Ag-AgCl) and the change in color was independant to the bromo group. Upon the basis of the results on the products analysis and the interpretaton of polarograms, a possible electrochemical reaction mechanism was suggested.

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ASSESSMENT OF ACTIVITY-BASED PYROPROCESS COSTS FOR AN ENGINEERING-SCALE FACILITY IN KOREA

  • KIM, SUNGKI;KO, WONIL;BANG, SUNGSIG
    • Nuclear Engineering and Technology
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    • 제47권7호
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    • pp.849-858
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    • 2015
  • This study set the pyroprocess facility at an engineering scale as a cost object, and presented the cost consumed during the unit processes of the pyroprocess. For the cost calculation, the activity based costing (ABC) method was used instead of the engineering cost estimation method, which calculates the cost based on the conceptual design of the pyroprocess facility. The calculation results demonstrate that the pyroprocess facility's unit process cost is $194/kgHM for pretreatment, $298/kgHM for electrochemical reduction, $226/kgHM for electrorefining, and $299/kgHM for electrowinning. An analysis demonstrated that the share of each unit process cost among the total pyroprocess cost is as follows: 19% for pretreatment, 29% for electrochemical reduction, 22% for electrorefining, and 30% for electrowinning. The total unit cost of the pyroprocess was calculated at $1,017/kgHM. In the end, electrochemical reduction and the electrowinning process took up most of the cost, and the individual costs for these two processes was found to be similar. This is because significant raw material cost is required for the electrochemical reduction process, which uses platinum as an anode electrode. In addition, significant raw material costs are required, such as for $Li_3PO_4$, which is used a lot during the salt purification process.

Improvement in Catalytic Activity of Ag Catalyst via Simple Mixing with Carbon

  • Choun, Myounghoon;Baek, Ji Yun;Eom, Taehyoung
    • KEPCO Journal on Electric Power and Energy
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    • 제5권4호
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    • pp.331-335
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    • 2019
  • In this study we investigate catalytic activity and selectivity of mixture of Ag and ketjenblack according to their ratios by product analysis and electrochemical experiments, such as cyclic voltammetry, linear sweep voltammetry and chronoamperometry. We reveal that catalytic activity toward CO2 reduction to CO is improved by simple mixing Ag nanoparticle and ketjenblack because addition of ketjenblack suppresses aggregation of Ag nanoparticles and brings increase in electrochemical active surface area. However, excess amount of ketjenblack rather inhibit the CO2 reduction to CO. These observations provide clues to develop highly active Ag catalyst or electrode toward electrochemical reduction of CO2.

Resolution of a Multi-Step Electron Transfer Reaction by Time Resolved Impedance Measurements: Sulfur Reduction in Nonaqueous Media

  • Park, Jin-Bum;Chang, Byoung-Yong;Yoo, Jung-Suk;Hong, Sung-Young;Park, Su-Moon
    • Bulletin of the Korean Chemical Society
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    • 제28권9호
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    • pp.1523-1530
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    • 2007
  • The first reduction peak of the cyclic voltammogram (CV) for sulfur reduction in dimethyl sulfoxide has been studied using time resolved Fourier transform electrochemical impedance spectroscopic (FTEIS) analysis of small potential step chronoamperometric currents. The FTEIS analysis results reveal that the impedance signals obtained during short potential steps can be resolved into electron transfer reactions of two different time constants in a high frequency region. The FTEIS method provides snap shots of impedance profiles during an earlier phase of the reaction, leading to time resolved EIS measurements. Our results obtained by the FTEIS analysis are consistent with a series of electron transfer and chemical equilibrium steps of a complex reaction, making up an ECE (electrochemical-chemical-electrochemical) mechanism postulated from the results of computer simulation.

Simple and Ultrasensitive Chemically Amplified Electrochemical Detection of Ferrocenemethanol on 4-Nitrophenyl Grafted Glassy Carbon Electrode

  • Koh, Ahyeon;Lee, Junghyun;Song, Jieun;Shin, Woonsup
    • Journal of Electrochemical Science and Technology
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    • 제7권4호
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    • pp.286-292
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    • 2016
  • Chemically amplified electrochemical detection, redox-active probe being amplified its electrochemical anodic current by a sacrificial electron donor presenting in solution, holds great potential for simple and quantitative bioanalytical analysis. Herein, we report the chemically amplified electrochemical analysis that drastically enhanced a detection of ferrocenemethanol (analyte) by ferrocyanide (chemical amplifier) on 4-nitrophenyl grafted glassy carbon electrodes at $60^{\circ}C$. The glassy carbon electrode grafted with a 4-nitrophenyl group using an electrochemical reduction suppressed the oxidation of ferrocyanide and thus enabled detection of ferrocenemethanol with excellent selectivity. The ferrocenemethanol was detected down to an nM range using a linear sweep voltammetry under kinetically optimized conditions. The detection limit was improved by decreasing the concentration of the ferrocyanide and increasing temperature.

산소 환원 반응을 위한 탄소기반 Pt-Cu 합금의 높은 전기적 촉매 활성 (High Electrochemical Activity of Pt-Cu Alloy Support on Carbon for Oxygen Reduction Reaction)

  • 김한슬;류수착;이영욱;신태호
    • 한국수소및신에너지학회논문집
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    • 제30권6호
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    • pp.549-555
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    • 2019
  • Electrocatalysis of oxygen reduction reaction (ORR) using Pt nanoparticles or bimetal on carabon was studied. Currently, the best catalyst is platinum, which is a limited resource and expensive to commercialize. In this paper, we investigated the cheaper and more active electrocatalysts by making Pt nanoparticles and adding 3D transition metal such as copper. Electrocatalysts were obtained by chemical reduction based on ethylene glycol solutions. Elemental analysis and particle size were confirmed by XRD and TEM. The electrochemical surface area (ECSA) and activity of the catalyst were determined by electrochemical techniques such as cyclic voltammetry and linear sweep voltammetry method. The commercialized Pt support on carbon (Pt/C, JM), synthesis Pt/C and synthesis Pt3Cu1 alloy nanoparticles supported on carbon were compared. We confirmed that the synthesized Pt3-Cu1/C has high electrochemical performance than commercial Pt/C. It is expected to develop an electrocatalyst with high activity at low price by increasing the oxygen reduction reaction rate of the fuel cell.

양이온 교환막을 이용한 이산화탄소의 전기화학적 환원 (Electrochemical Reduction of Carbon Dioxide Using a Proton Exchange Membrane)

  • 김학윤;안상현;황승준;유성종;한종희;김지현;김수길;장종현
    • 전기화학회지
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    • 제15권4호
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    • pp.216-221
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    • 2012
  • 전기화학적 환원을 통한 이산화탄소의 활용을 위한 노력은 오래 전부터 계속되어 왔다. 최근에는 액체연료 중 가격이 비싸고 그 활용도가 높은 포름산의 생성을 위한 연구가 많이 진행되고 있지만 실제 포름산을 생성하고 분석하는 과정에서 효율의 개선과 분석에 어려움이 따른다. 따라서 이산화탄소 환원을 이용한 포름산 생성에 필요한 시스템의 제조, 반응 조건의 개발 및 분석 방법의 정량화가 필요하다. 본 연구에서는 이산화탄소의 전기화학적 환원을 통한 포름산의 생성을 진행하고 생성된 포름산의 양을 분석하였다. 실험에 이용된 셀은 양이온 교환막을 사용하는 대용량의 회분형 셀을 이용하였으며 전위차계를 통하여 삼전극에서 전기화학 실험을 진행하였다. 전기화학 실험은 다양한 촉매 금속을 이용하여 선형 전위 주사법과 chronoamperometry를 통해 진행했으며 이 때 기준전극은 염화은 전극을 이용하였고 상대전극은 백금 전극을 사용하였다. 실험을 통해 생성된 포름산의 농도를 high performance liquid chromatography(HPLC)를 통하여 분석하여 시스템의 적정성과 분석 방법의 유효성을 검증하였다.

A Techno-Economic Study of Commercial Electrochemical CO2 Reduction into Diesel Fuel and Formic Acid

  • Mustafa, Azeem;Lougou, Bachirou Guene;Shuai, Yong;Razzaq, Samia;Wang, Zhijiang;Shagdar, Enkhbayar;Zhao, Jiupeng
    • Journal of Electrochemical Science and Technology
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    • 제13권1호
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    • pp.148-158
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    • 2022
  • The electrochemical CO2 reduction (ECR) to produce value-added fuels and chemicals using clean energy sources (like solar and wind) is a promising technology to neutralize the carbon cycle and reproduce the fuels. Presently, the ECR has been the most attractive route to produce carbon-building blocks that have growing global production and high market demand. The electrochemical CO2 reduction could be extensively implemented if it produces valuable products at those costs which are financially competitive with the present market prices. Herein, the electrochemical conversion of CO2 obtained from flue gases of a power plant to produce diesel and formic acid using a consistent techno-economic approach is presented. The first scenario analyzed the production of diesel fuel which was formed through Fischer-Tropsch processing of CO (obtained through electroreduction of CO2) and hydrogen, while in the second scenario, direct electrochemical CO2 reduction to formic acid was considered. As per the base case assumptions extracted from the previous outstanding research studies, both processes weren't competitive with the existing fuel prices, indicating that high electrochemical (EC) cell capital cost was the main limiting component. The diesel fuel production was predicted as the best route for the cost-effective production of fuels under conceivable optimistic case assumptions, and the formic acid was found to be costly in terms of stored energy contents and has a facile production mechanism at those costs which are financially competitive with its bulk market price. In both processes, the liquid product cost was greatly affected by the parameters affecting the EC cell capital expenses, such as cost concerning the electrode area, faradaic efficiency, and current density.

Carbon-Supported Ordered Pt-Ti Alloy Nanoparticles as Durable Oxygen Reduction Reaction Electrocatalyst for Polymer Electrolyte Membrane Fuel Cells

  • Park, Hee-Young;Jeon, Tae-Yeol;Lee, Kug-Seung;Yoo, Sung Jong;Sung, Young-Eun;Jang, Jong Hyun
    • Journal of Electrochemical Science and Technology
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    • 제7권4호
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    • pp.269-276
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    • 2016
  • Carbon-supported ordered Pt-Ti alloy nanoparticles were prepared as a durable and efficient oxygen reduction reaction (ORR) electrocatalyst for polymer electrolyte membrane fuel cells (PEMFCs) via wet chemical reduction of Pt and Ti precursors with heat treatment at $800^{\circ}C$. X-ray diffraction analysis confirmed that the prepared electrocatalysts with Ti precursor molar compositions of 40% (PtTi40) and 25% (PtTi25) had ordered $Pt_3Ti$ and $Pt_8Ti$ structures, respectively. Comparison of the ORR polarization before and after 1500 electrochemical cycles between 0.6 and 1.1 V showed little change in the ORR polarization curve of the electrocatalysts, demonstrating the high stability of the PtTi40 and PtTi25 alloys. Under the same conditions, commercial carbon-supported Pt nanoparticle electrocatalysts exhibited a negative potential shift (10 mV) in the ORR polarization curve after electrochemical cycling, indicating degradation of the ORR activity.

전기화학적 환원 분석을 통한 Sn의 산화에 대한 연구 (The Oxidation Study of Pure Tin via Electrochemical Reduction Analysis)

  • 조성일;유진;강성권
    • 마이크로전자및패키징학회지
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    • 제11권3호
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    • pp.55-62
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    • 2004
  • 여러 가지 온도와 습도에 따라 Sn의 표면에 형성되는 산화물을 전기화학적 환원방법을 이용해 분석하였다. 전기화학적 방법을 이용하여 금속표면에 형성된 산화물을 환원시킬 때 나타나는 환원전위와 소모된 전하량을 측정하여 표면 산화물의 종류와 양을 정량적으로 분석하였다 우선 전기화학적 환원 방법이 금속 표면 산화물의 분석에 적합한지 알아보기 위해 여러 가지 산화물 분말의 환원 전위와 수소 발생 전위를 측정하였고, 분석을 위한 최적의 전류밀도 값을 구하였다. Sn 표면에 생성된 산화물을 분석한 결과 $85^{\circ}C$의 건조한 환경에서 보다 T/H (Temperature/Humidity, $85^{\circ}C$/$85\%$상대습도)조건에서 SnO가 더 빠르게 성장하였다. 또한 T/H 조건에서 하루가 지난 이후부터는 Sn의 표면 최상층에 매우 얇은 (<10 ${\AA}$) $SnO_2$ 가 형성되어 있는 것을 확인하였다. $150^{\circ}C$에서는 SnO와 $SnO_2$가 같이 존재하는 것을 확인하였다. 또한 XPS와 AES 표면분석을 통하여 환원 실험 결과를 뒷받침하였다.

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