• Title/Summary/Keyword: Electrolysis cell

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Eletrochemical Characteristics of Ozone Generator using Boron-doped Diamond Electrode (붕소가 도핑된 다이아몬드전극을 이용한 오존발생기의 전기화학적 특성)

  • ;;Yasuaki Einaga;Akira Fujishima
    • Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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    • 2001.11a
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    • pp.585-588
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    • 2001
  • Thin, Boron-doped conducting diamond films are expected to be excellent electrodes for industrial electrolysis. Boron-doped conducting diamond films were used as anode for generating ozone gas by electrolysis of acidic solution. In this work, we have studied ozone generating system using Boron-doped Diamond electrode. Electrochemical cell and ozone generating system were designed for decreasing the temperature of the system, which was elevated during the reaction. by circulation of electrolyte in the system. In order to determine the ozone generation properties of diamond electrode, experimental conditions, electrolyte concentration, temperature, flow rate and reaction time were varied diversely. As a result, we could confirm that ozone gas was generated successfully and the performance of diamond electrode was stable while PbO$_2$ electrode was disintegrated. Actually we are found that ozone amount increased by lowering the temperature of electrolyte.

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Research Trend in Electrocatalysts for Anion Exchange Membrane Water Electrolysis (음이온교환막 수전해 촉매기술 동향)

  • Kim, Jiyoung;Lee, Kiyoung
    • Journal of the Korean Electrochemical Society
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    • v.25 no.2
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    • pp.69-80
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    • 2022
  • The anion exchange membrane (AEM) water electrolysis for high purity hydrogen production is attracting attention as a next-generation green hydrogen production technology by using inexpensive non-noble metal-based catalysts instead of conventional precious metal catalysts used in proton exchange membrane (PEM) water electrolysis systems. However, since AEM water electrolysis technology is in the early stages of development, it is necessary to develop research on AEM, ionomers, electrode supports and catalysts, which are key elements of AEM water electrolysis. Among them, current research in the field of catalysts is being studied to apply a previously developed half-cell catalyst for alkali to the AEM system, and the applied catalyst has disadvantages of low activity and durability. Therefore, this review presented a catalyst synthesis technique that promoted oxygen evolution reaction (OER) and hydrogen evolution reaction (HER) using a non-noble metal-based catalyst in an alkaline medium.

Effect of Operation Temperature on the Durability of Membrane and Electrodes in PEM Water Electrolysis (PEM 수전해에서 막과 전극의 내구성에 미치는 구동 온도의 영향)

  • Donggeun Yoo;Seongmin Kim;Byungchan Hwang;Sohyeong Oh;Kwonpil Park
    • Korean Chemical Engineering Research
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    • v.61 no.1
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    • pp.19-25
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    • 2023
  • Although a lot of research and development has been conducted on the performance improvement of PEM (Proton Exchange Membrane) water electrolysis, the research on durability is still in early stage. This study investigated effect of temperature on the water electrolysis durability when driving temperature of the PEM water electrolysis was increased to improve performance. Voltage change, I-V, CV (Cyclic Voltammetry), LSV (Linear Sweep Voltammetry), Impedance, and FER (Fluoride Emission Rate) were measured while driving under a constant current condition in a temperature range of 50~80 ℃. As the operating temperature increased, the degradation rate increased. At 50~65 ℃, the degradation of the IrO2 electrocatalyst mainly affected the durability of the PEM water electrolysis cell. At 80 ℃, the polymer membrane and electrode degradation proceeded similarly, and the short resistance decreased to 1.0 kΩ·cm2 or less, and the performance decreased to about 1/3 of the initial stage after 144 hours of operation due to the shorting phenomenon.

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%.

Characterization of Electrochemical Ammonia Electrolysis Using a Platinum Electrode for Anodic Reaction (Pt포일 양극을 이용한 전기화학적 암모니아 수전해 특성 연구)

  • CHOI, JEONGMIN;KIM, HAKDEOK;SONG, JUHUN
    • Journal of Hydrogen and New Energy
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    • v.33 no.4
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    • pp.337-342
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    • 2022
  • In this study, a water electrolysis was studied to investigate the effect of ammonia on current density and H2 gas production. A H type cell with three electrodes was used and KOH solution was used as electrolyte. The conventional platinum foil was used for working electrode, whereas nickel foam was used for counter electrode. CV experiment was performed to see the activity of ammonia oxidation reaction. In addition, CP experiment was done to examine the dependence of Faraday efficiency of hydrogen on current density and NH3 concentration. The CV result shows the 0.5M NH3 concentration required for highest current density and reliable operation. The CP result shows the increased current density leads to higher H2 generation. The higher H2 production and subsequent energy efficiency was observed for 0.5M NH3 using a Pt/13%Rh coil for a cathode as compared to those in water electrolysis.

Predicting Initial Construction Costs of Electrolysis Hydrogen Production Plants for Building Sustainable Energy Systems (지속 가능한 에너지 시스템 구축을 위한 전기분해 수소 생산 플랜트 초기 건설비용 예측)

  • SUNGWOOK KANG;JOONHEON KIM;JONGHWA PARK;DAEMYEONG CHO
    • Journal of Hydrogen and New Energy
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    • v.35 no.3
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    • pp.257-268
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    • 2024
  • Hydrogen serves as a clean energy source with potential applications across various sectors including electricity, transportation, and industry. In terms of policy and economic support, governmental policy backing and economic incentives are poised to accelerate the commercialization and expansion of hydrogen energy technologies. Hydrogen energy is set to become a cornerstone for a sustainable future energy system. Additionally, when constructing hydrogen production plants, economic aspects must be considered. The essence of hydrogen production plants lies in the electrolysis of water, a process that separates water into hydrogen and oxygen using electrical energy. The initial capital expenditure (CAPEX) for hydrogen production plants can vary depending on the electrolysis technology employed. This study aims to provide a comprehensive understanding of hydrogen production technologies as well as to propose a method for predicting the CAPEX of hydrogen production plants.

Electrochemical Characteristics of Solid Polymer Electrode Fabricated with Low IrO2 Loading for Water Electrolysis

  • Ban, Hee-Jung;Kim, Min Young;Kim, Dahye;Lim, Jinsub;Kim, Tae Won;Jeong, Chaehwan;Kim, Yoong-Ahm;Kim, Ho-Sung
    • Journal of Electrochemical Science and Technology
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    • v.10 no.1
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    • pp.22-28
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    • 2019
  • To maximize the oxygen evolution reaction (OER) in the electrolysis of water, nano-grade $IrO_2$ powder with a low specific surface was prepared as a catalyst for a solid polymer electrolyte (SPE) system, and a membrane electrode assembly (MEA) was prepared with a catalyst loading as low as $2mg\;cm^{-2}$ or less. The $IrO_2$ catalyst was composed of heterogeneous particles with particle sizes ranging from 20 to 70 nm, having a specific surface area of $3.8m^2g^{-1}$. The anode catalyst layer of about $5{\mu}m$ thickness was coated on the membrane (Nafion 117) for the MEA by the decal method. Scanning electron microscopy (SEM) and electrochemical impedance spectroscopy (EIS) confirmed strong adhesion at the interface between the membrane and the catalyst electrode. Although the loading of the $IrO_2$ catalyst was as low as $1.1-1.7mg\;cm^{-2}$, the SPE cell delivered a voltage of 1.88-1.93 V at a current density of $1A\;cm^{-2}$ and operating temperature of $80^{\circ}C$. That is, it was observed that the over-potential of the cell for the oxygen evolution reaction (OER) decreased with increasing $IrO_2$ catalyst loading. The electrochemical stability of the MEA was investigated in the electrolysis of water at a current density of $1A\;cm^{-2}$ for a short time. A voltage of ~2.0 V was maintained without any remarkable deterioration of the MEA characteristics.

Refining of Manganese from Anode Slime of Electrolytic Zinc and Waste Dry Cell (전해아연의 Anode Slime과 건전지의 폐기물로부터 금속망간의 회수)

  • Yoon, Byoung-Ha;Kim, Dai-Ryong
    • Journal of Surface Science and Engineering
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    • v.19 no.1
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    • pp.13-19
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    • 1986
  • Manganese in the Anode slime and the paste-positive material of waste-dry cell was recovered by leaching with the hydrochloric acid solution. The impurities (Zn, Fe, Pb), co-leached with manganese were removed from the leached solution prior to electrolysis by hydrometallurgical techniques such as the neutralization with ammonium hydroxide and cementation on manganese powder. The electrodeposition of manganese from the purified chloride solution with sodium selenate was performed. Cathode current efficiency was found to be affected significantly by the concentration of sodium selenate and ammonium chloride salt, bath temperate, current density and PH. The current efficiency of about 88.7% was obtained by electrolysis manganese chloride solution with sodium selenate (0.1/g) at 10$^{\circ}C$.

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