• Title/Summary/Keyword: Electrolyser

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A Study for Correlativity of Hydrogen Production Using Artificial Luminous Intensity (인공조도를 이용한 수소발생량과의 상관성에 관한 연구)

  • Jung, You-Ra;Hong, Chang-Woo;Choi, Young-Sung;Lee, Kyung-Sup
    • The Transactions of the Korean Institute of Electrical Engineers P
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    • v.59 no.2
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    • pp.218-221
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    • 2010
  • This paper presents energy efficiency about an electrolyser which is related with the hybrid system of solar cell and fuel cell for using the system more fully. The water electrolyser is the exact reverse of a hydrogen fuel cell; it produces gaseous hydrogen and oxygen from water. Electrolyser technology may be implemented at a variety of scales wherever there is an electricity supply to provide hydrogen and/or oxygen for virtually any requirement. Also, this paper shows optimum operating point in the electrolyser for saving cost of the electrical energy with hybrid system.

Effect of Electrolyte Concentration Difference on Hydrogen Production during PEM Electrolysis

  • Sun, Cheng-Wei;Hsiau, Shu-San
    • Journal of Electrochemical Science and Technology
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    • v.9 no.2
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    • pp.99-108
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    • 2018
  • Proton exchange membrane (PEM) water electrolysis systems offer several advantages over traditional technologies including higher energy efficiency, higher production rates, and more compact design. In this study, all the experiments were performed with a self-designed PEM electrolyser operated at 1 atm and $25^{\circ}C$. Two types of electrolyte were used: (i) potassium hydroxide (KOH), and (ii) sulfuric acid ($H_2SO_4$). In the experiments, the voltage, current, and time were measured. The concentration of the electrolyte significantly affected the electrolyser performance. Overall the best case was with 15 wt% $H_2SO_4$ at the anode channel and 20 wt% at the cathode channel with. In addition, increasing the difference in concentration of the sulfuric acid had an effect on the diffusion. The diffusion flux became larger when the difference in concentration became larger, increasing electrolyser efficiency without the addition of extra energy.

Electrolyser for CECE Process

  • Lee, Min-Soo;Chung, Hong-Suk;Paek, Seung-Woo;Kim, Kwang-Rag;Yim, Sung-Paal;Ahn, Do-Hee
    • Proceedings of the Korean Nuclear Society Conference
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    • 2005.05a
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    • pp.197-198
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    • 2005
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Performance change according to the catalyst intrusion rate in the MEA for the PEM water electrolysis (고분자전해질 수전해용 MEA의 촉매침투도에 따른 성능변화)

  • Kim, Hong-Youl
    • 한국신재생에너지학회:학술대회논문집
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    • 2009.11a
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    • pp.254-256
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    • 2009
  • The performances of proton exchange membrane (PEM) water electrolysis depend on many factors such as materials, geometries, fabrication methods, operating conditions, and so forth. The fabrication method is concerned, membrane electrode assemblies (MEA) are a most important part to show different performances by different fabrication methods. The performance change of PEM water electrolysis was experimentally measured according to the fabrication differences of the anode electrodes. One point of view is the catalyst intrusion rate to the anode gas diffusion layer (GDL), and the other point of view is the catalyst loading distribution in depth of the anode GDL. Results show that the performances of MEA with deep intrusion of the catalysts are better in the range of low current densities but worse at higher current densities. The catalyst loading distribution does not affect significantly to the performance of PEM water electrolyser.

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Effects of organic additives in cyanide zinc electroplating Bath(Part 2) (시안화아연 도금욕에 있어서 유기화합물 첨가제의 영향 (제 2 보))

  • Lee, Ju-Seong;Park, Jung-Il
    • Journal of Surface Science and Engineering
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    • v.12 no.3
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    • pp.174-179
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    • 1979
  • The effects of brightness, electrochemical behaviour on the organic additives, such as aldehydes, polymers, amines and condensed product obtained from epichlorohydrin and nicotinamide, in cyanide zinc electrolplating bath have been studied by controlled potential electrolyser. The results were summerized as follows: (1) It was found that the addition of only one compound of these organic compounds in the bath was unsuitable but mixture of anisaldehyde or monoethanolamine and condensed product as suitable as brightener. (2) The cathodic polarization curve of polymers or aldehydes in cyanide zinc electroplating bath was almost the same but the cathodic polarization curve of condensed product remarkable shifted to noble potential more than non-additive curve.

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Composite Ni-TiO2 nanotube arrays electrode for photo-assisted electrolysis

  • Pozio, Alfonso;Masci, Amedeo;Pasquali, Mauro
    • Advances in Energy Research
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    • v.3 no.1
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    • pp.45-57
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    • 2015
  • This article is addressed to define a new composite electrode constituted by porous nickel and an array of highly ordered $TiO_2$ nanotubes obtained by a previous galvanostatic anodization treatment in an ethylene glycol solution. The electrochemical performances of the composite anode were evaluated in a photo-electrolyser, which showed good solar conversion efficiency with respect to the UV irradiance together with a reduction of energy consumption. Such a combination of materials makes our system simple and able to work both in dark and under solar light exposure, thus opening new perspectives for industrial-scale applications.

Performance Change according to the Catalyst Intrusion Rate in the MEA for the PEM Water Electrolysis (고분자전해질 수전해용 MEA의 촉매침투도에 따른 성능변화)

  • Kim, Hong-Youl;Lee, Ji-Jung;Lee, Jae-Young;Lee, Hong-Ki
    • New & Renewable Energy
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    • v.5 no.4
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    • pp.75-78
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    • 2009
  • The performances of proton exchange membrane (PEM) water electrolysis depend on many factors such as materials, geometries, fabrication methods, operating conditions, and so forth. The fabrication method is concerned, membrane electrode assemblies (MEA) are a most important part to show different performances by different fabrication methods. The performance change of PEM water electrolysis was experimentally measured according to the fabrication differences of the anode electrodes. One point of view is the catalyst intrusion rate to the anode gas diffusion layer (GDL), and the other point of view is the catalyst loading distribution in depth of the anode GDL. Results show that the performances of MEA with deep intrusion of the catalysts are better in the range of low current densities but worse at higher current densities. The catalyst loading distribution does not affect significantly to the performance of PEM water electrolyser.

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From Renewable Electricity to Green Hydrogen: Production and Storage Challenges for a Clean Energy Future

  • Hidouri Dalila;Rym Marouani;Cherif Adnen
    • International Journal of Computer Science & Network Security
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    • v.24 no.6
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    • pp.171-179
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    • 2024
  • Decentralized energy production without greenhouse gas emissions from renewable energy sources despite their advantage and environmental impact suffers from the problem of intermittent and fluctuating supply depending on weather conditions. To overcome this problem, energy storage is essential to enable reliable and continuous supply of the load. Hydrogen is one of the most promising energy storage solutions because it is easily transportable and can be used as fuel or as a raw material for the production of other chemicals.In this article, we will focus on hydrogen energy storage techniques using photovoltaic systems. We will review the different types of hydrogen storage structuresfor several applications, including residential and commercial buildings, as well as industry and transportation (electric vehicles using PEFMC fuel cells).

Evaluation of the Performance of Water Electrolysis Cells and Stacks for High-Altitude Long Endurance Unmanned Aerial Vehicle (고고도 무인기용 수전해 셀 및 스택의 제작 및 성능 평가)

  • JUNG, HYE YOUNG;LEE, JUNYOUNG;YOON, DAEJIN;HAN, CHANGHYUN;SONG, MINAH;LIM, SUHYUN;MOON, SANGBONG
    • Journal of Hydrogen and New Energy
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    • v.27 no.4
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    • pp.341-348
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    • 2016
  • The experiments related on structure and water electrolysis performance of HALE UAV stack were conducted in this study. Anode catalyst $IrRuO_2$ was prepared by Adam's fusion methods as 2~3 nm nano sized particles, and the cathode catalyst was used as commercial product of Premetek. The MEA (membrane electrode assembly) was manufactured by decal methods, anode and anode catalytic layers were prepared by electro-spray. HALE stack was composed of 5 multi-cells as $0.2Nm^3/hr$ hydrogen production rate with hydrogen pressure as 10 bar. The water electrolysis performance was investigated at atmospheric pressure and temperature of $55^{\circ}C$. Best performance of HALE UAV stack was recorded as cell voltage efficiency as 86%.

High Temperature Water Electrolysis of Covalently Cross-linked CL-SPEEK/Cs-TSiA/Ceria Composite Membrane (공유가교 CL-SPEEK/Cs-TSiA/Ceria 복합막의 고온 수전해 성능)

  • JUNG, HYEYOUNG;YOON, DAEJIN;CHUNG, JANGHOON;MOON, SANGBONG
    • Journal of Hydrogen and New Energy
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    • v.28 no.5
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    • pp.433-439
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    • 2017
  • The high temperature performance of PEM type electrolyser at $120^{\circ}C$ based on covalently cross-linked sulfonated poly ether ether ketone (SPEEK) composie membrane was investigated. Ion conductivity and other properties of SPEEK membrane were improved by adding heteropoly acid and Ceria. The membrane electrode assemblies were prepared using commercial PtC and nano-sized $IrRuO_2$ catalyst by electro-spraying and decal process. Voltage efficiency of MEA equipped with SPEEK membrane was slightly better than that of $Nafion^{(R)}$ membrane, due to its higher proton conductivity at high temperature. The cell performance of MEA with CL-SPEEK/Cs-TSiA/Ceria is 1.71 V at $1A/cm^2$ and $120^{\circ}C$.