• 제목/요약/키워드: Electrochemical regeneration

검색결과 21건 처리시간 0.02초

Immobilization of a Mediator onto Carbon Cloth Electrode and Employment of the Modified Electrode to an Electroenzymatic Bioreactor

  • Jeong, Eun-Seon;Sathishkumar, Muthuswamy;Jayabalan, Rasu;Jeong, Su-Hyeon;Park, Song-Yie;Mun, Sung-Phil;Yun, Sei-Eok
    • Journal of Microbiology and Biotechnology
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    • 제22권10호
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    • pp.1406-1411
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    • 2012
  • 5,5'-Dithiobis(2-nitrobenzoic acid) (DTNB) was selected as an electron transfer mediator and was covalently immobilized onto high porosity carbon cloth to employ as a working electrode in an electrochemical $NAD^+$-regeneration process, which was coupled to an enzymatic reaction. The voltammetric behavior of DTNB attached to carbon cloth resembled that of DTNB in buffered aqueous solution, and the electrocatalytic anodic current grew continuously upon addition of NADH at different concentrations, indicating that DTNB is immobilized to carbon cloth effectively and the immobilized DTNB is active as a soluble one. The bioelectrocatalytic $NAD^+$ regeneration was coupled to the conversion of L-glutamate into ${\alpha}$-ketoglutarate by L-glutamate dehydrogenase within the same microreactor. The conversion at 3 mM monosodium glutamate was very rapid, up to 12 h, to result in 90%, and then slow up to 24 h, showing 94%, followed by slight decrease. Low conversion was shown when substrate concentration exceeding 4 mM was tested, suggesting that L-glutamate dehydrogenase is inhibited by ${\alpha}$-ketoglutarate. However, our electrochemical $NAD^+$ regeneration procedure looks advantageous over the enzymatic procedure using NADH oxidase, from the viewpoint of reaction time to completion.

Electrochemical Capacitance of Activated Carbons Regenerated using Thermal and Chemical Activation

  • Park, Jung Eun;Lee, Gi Bbum;Hwang, Sang Youp
    • Journal of Electrochemical Science and Technology
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    • 제12권3호
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    • pp.339-345
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    • 2021
  • Spent activated carbons (SACs) collected from a water treatment plant were regenerated and then adopted as electrochemical material in capacitors. The SACs used in this study were regenerated via two steps, namely thermal and chemical activation. However, during the activation process, the adsorbates were converted into ashes, which caused pore blockage and decreased specific surface area. The regenerated SACs were washed with acid solutions with different levels of acidity (strong: HCl, mild: H3PO4, and weak: H2O2) to remove the ashes. The regenerated SACs washed with HCl exhibited the highest specific surface area, although their capacitance was not the highest. Conversely, the specific surface area of regenerated SACs washed using H3PO4 was slightly lower than that of HCl, but exhibited higher capacitance and electrochemical stability. Although the strong acid removed the generated ashes in the pores efficiently, it could adversely affect their structural stability, which would lead to lower capacitance.

전기화학 반응에 의한 염화철 폐식각액의 재생 및 구리 회수에 관한 연구 (A Study on Electrochemical Regeneration of Waste Iron-chloride Etchant and Copper Recovery)

  • 김성은;이상린;강신춘;김이철;리즈완 셰이크;박융호
    • 청정기술
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    • 제18권2호
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    • pp.183-190
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    • 2012
  • PCB에칭에 의해 발생한 염화철 폐식각액 중 염화철을 산화시키고 구리를 석출시키는 전기화학적 재생공정은 환경오염을 줄이면서도 부산물을 얻어내어 경제성이 크다. 그러나, 염화철 폐식각액은 철과 구리, 두 가지 금속이 함께 함유되어 있기 때문에 전해조에서 일어나는 반응이 복잡하다. 본 연구에서는 회분식 공정을 통하여 전기화학적인 염화철 산화 및 구리 석출반응의 특성을 조사하고 관련된 공정변수들의 최적 조건을 도출해내었다. 염화철의 산화는 항상 원하는 수준으로 되었으며, 탄소 음전극을 사용한 반응에서 $350mA/cm^2$의 전류밀도와 12 g/L의 구리 농도 조건에서, $Fe^{2+}$이온의 비율이 높을수록 구리 석출 효율이 높았다. 또한, 도출해낸 최적 조건을 바탕으로 Bench 장치 연속운전을 통해서 scale-up 가능성을 확인하였다.

과황산염과 나노영가철을 이용한 페놀의 전기화학적 산화 (Electrochemical Oxidation of Phenol using Persulfate and Nanosized Zero-valent Iron)

  • 김철용;안준영;김태유;황인성
    • 한국지하수토양환경학회지:지하수토양환경
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    • 제22권2호
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    • pp.17-25
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    • 2017
  • The efficiency and mechanism of electrochemical phenol oxidation using persulfate (PS) and nanosized zero-valent iron (NZVI) were investigated. The pseudo-first-order rate constant for phenol removal by the electrochemical/PS/NZVI ($1mA^*cm^{-2}/12$ mM/6 mM) process was $0.81h^{-1}$, which was higher than those of the electrochemical/PS and PS/NZVI processes. The electrochemical/PS/NZVI system removed 1.5 mM phenol while consuming 6.6 mM PS, giving the highest stoichiometric efficiency (0.23) among the tested systems. The enhanced phenol removal rates and efficiencies observed for the electrochemical/PS/NZVI process were attributed to the interactions involving the three components, in which the electric current stimulated PS activation, NZVI depassivation, phenol oxidation, and PS regeneration by anodic or cathodic reactions. The electrochemical/PS/NZVI process effectively removed phenol oxidation products such as hydroquinone and 1,4-benzoquinone. Since the electric current enhances the reactivities of PS and NZVI, process performance can be optimized by effectively manipulating the current.

Photocatalytic Systems of Pt Nanoparticles and Molecular Co Complexes for NADH Regeneration and Enzyme-coupled CO2 Conversion

  • Kim, Ellen;Jeon, Minkyung;Kim, Soojin;Yadav, Paras Nath;Jeong, Kwang-Duk;Kim, Jinheung
    • Rapid Communication in Photoscience
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    • 제2권2호
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    • pp.42-45
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    • 2013
  • Natural photosynthesis utilizes solar energy to convert carbon dioxide and water to energy-rich carbohydrates. Substantial use of sunlight to meet world energy demands requires energy storage in useful fuels via chemical bonds because sunlight is intermittent. Artificial photosynthesis research focuses the fundamental natural process to design solar energy conversion systems. Nicotinamide adenine dinucleotide ($NAD^+$) and $NADP^+$ are ubiquitous as electron transporters in biological systems. Enzymatic, chemical, and electrochemical methods have been reported for NADH regeneration. As photochemical systems, visible light-driven catalytic activity of NADH regeneration was carried out using platinum nanoparticles, molecular rhodium and cobalt complexes in the presence of triethanolamine as a sacrificial electron donor. Pt nanoparticles showed photochemical NADH regeneration activity without additional visible light collector molecules, demonstrating that both photoactivating and catalytic activities exist together in Pt nanoparticles. The NADH regeneration of the Pt nanoparticle system was not interfered with the reduction of $O_2$. Molecular cobalt complexes containing dimethylglyoxime ligands also transfer their hydrides to $NAD^+$ with photoactivation of eosin Y in the presence of TEOA. In this photocatalytic reaction, the $NAD^+$ reduction process competed with a proton reduction.

전기화학적 방법을 이용한 Spent Granular Activated Carbon (GAC)의 재생 연구 (A Study of the Regeneration of Spent GAC using an Electrochemical Method)

  • 이상민;주수빈;조영수;오예지;김형준;심인태
    • 대한토목학회논문집
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    • 제42권4호
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    • pp.481-491
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    • 2022
  • 본 연구는 CSOs의 고도처리를 목적으로 다단 횡류식 여과와 GAC 흡착조의 융합공정의 운영에서 GAC 흡착조의 유기물 처리 특성을 조사하고 설계 파과점에 도달한 GAC를 전기화학적 방법을 통한 재생효율을 평가하는 것이다. 여과공정은 부유물질은 용이하게 제거되지만 용존 유기물이 제거되지 않아 CSOs의 고도처리를 위해서는 용존유기물질의 제거능이 추가로 필요하다. 일반적으로 GAC 흡착은 정수처리 공정이나 하수의 3차 처리공정과 같은 저농도 유기물 조건에서 적용되어왔고 하수나 CSOs와 같이 유기물 농도가 높은 조건에서는 거의 적용이 되지 않았기에 본 연구에서 GAC를 이용한 CSOs 처리는 흥미로운 경험을 제공할 것이다. 본 연구는 유입 유기물 강도에 따른 GAC의 연속 운전 및 파과 특성을 조사하고 사용된 GAC를 전기화학적 재생을 적용하였으며, 이때 전압강도 및 전해액이 종류에 따른 흡착 유기물의 탈착 특성을 조사하였고 재생 후 GAC의 재흡착실험을 통해서 재생효율을 평가하였다. GAC 연속 운전결과 파과기간은 고농도 조건에서 21일, 중농도에서 28일 그리고 저농도에서 32일을 나타내었다. 전기분해를 통한 흡착 유기물의 탈착은 전기 분해 조건에 따라 188~609 mgCOD/L까지 발생하였고 전해액 종류의 영향은 NaOH가 H2O2보다 조금 우수한 탈착 특성을 나타냈다.

경계요소법에 의한 전해가공물의 형상예측에 관한 연구 (A Study on The Prediction of Workpiece Shape of The Electrochemical Machining by Boundary Element Method)

  • 강대철;양재봉;김헌영;전병희
    • 한국소성가공학회:학술대회논문집
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    • 한국소성가공학회 2003년도 춘계학술대회논문집
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    • pp.443-447
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    • 2003
  • The BEM (Boundary Element Method) is a computational technique for the approximate solution of problems in continuum mechanics. In the BEM both volume and surface integrals transformed into boundary integral equations. So, we applied the ECM (Electrochemical Machining) process to boundary problem, because our focus is only deformed shape. The ECM process is modeled as a two-dimensional problem assuming constant properties of electrolyte, and an incremental formulation is used with automatic mesh regeneration. As a result the final shape is roughly agreed with experimental shape. But, it has an error of exact shape, because a chemically factor is not considered

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Electrochemical Activity of a Blue Anatase TiO2 Nanotube Array for the Oxygen Evolution Reaction in Alkaline Water Electrolysis

  • Han, Junhyeok;Choi, Hyejin;Lee, Gibaek;Tak, Yongsug;Yoon, Jeyong
    • Journal of Electrochemical Science and Technology
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    • 제7권1호
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    • pp.76-81
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    • 2016
  • An anatase TiO2 nanotube array (NTA) was fabricated by anodization and successive heat treatments. When the anatase TiO2 NTA was cathodically polarized, its color changed to blue, and it could be used as an electrochemically active anode for an oxygen evolution reaction (OER) in alkaline water electrolysis. The structure of the blue anatase TiO2 NTA was controlled by the anodization conditions and its catalytic activity increased with an increase of the surface area. The activity of the blue anatase TiO2 NTA gradually reduced with the continued OER because of the partial oxidation of Ti3+ to Ti4+. However, an intermittent cathodic regeneration process could significantly slow its reduction rate. The blue anatase TiO2 NTA could be an alternative anode for alkaline water electrolysis.

전기화학적 산소요구량 측정용 이산화납 전극 센서의 유효성 (Effectiveness of the Sensor using Lead Dioxide Electrodes for the Electrochemical Oxygen Demand)

  • 김홍원;정남용
    • 한국생산제조학회지
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    • 제21권4호
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    • pp.575-581
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    • 2012
  • The electrochemical oxygen demand (ECOD) is an additional sum parameter, which has not yet found the attention it deserves. It is defined as the oxygen equivalent of the charge consumed during an electrochemical oxidation of the solution. Only one company has yet developed an instrument to determine the ECOD. This instrument uses $PbO_2$-electrodes for the oxidation and has been successfully implemented in an automatic on-line monitor. A general problem of the ECOD determination is the high overpotential of electrochemical oxidations of most organic compounds at conventional electrodes. Here we present a new approach for the ECOD determination, which is based on the use of a solid composite electrodes with highly efficient electro-catalysts for the oxidation of a broad spectrum of different organic compounds. Lead dioxide as an anode material has found commercial application in processes such as the manufacture of sodium per chlorate and chromium regeneration where adsorbed hydroxyl radicals from the electro-oxidation of water are believed to serve as the oxidizing agent. The ECOD sensors based on the Au/$PbO_2$ electrode were operated at an optimized applied potential, +1.6 V vs. Ag/AgCl/sat. KCl, in 0.01 M $Na_2SO_4$ solution, and reduced the effect of interference ($Cl^-$ and $Fe^{2-}$) and an expended lifetime (more than 6 months). The ECOD sensors were installed in on-line auto-analyzers, and used to analyze real samples.

Characterization of Tribocorrosion Behaviour of CoCr Alloy by Electrochemical Techniques in Several Corrosive Media

  • Escudero, M.L.;Diaz, I.;Martinez Lerma, J.F.;Montoya, R.;Garcia-Alonso, M.C.
    • Corrosion Science and Technology
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    • 제17권2호
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    • pp.68-73
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    • 2018
  • Substitution of hip and knee joints by CoCr alloys is in great demand due to their high wear resistance and good biocompatibility. Understanding of tribocorrosion in joint replacements requires study of variables such as coefficient of friction and the choice of a proper corrosive medium in wear-corrosion tests carried out in the lab. The objective of this study was to characterize tribocorrosion behaviour of CoCr alloy with low (LCCoCr) and high carbon (HCCoCr) contents in several corrosive media: NaCl, Phosphate Buffer Solution (PBS), and PBS with hyaluronic acid (PBS-HA). Tribocorrosion tests were carried out on a pin-on-disk tribometer with an integrated electrochemical cell. A normal load of 5N was applied on the alumina ball counterpart at a rotation rate of 120 rpm. Coefficient of friction (COF) was measured and tribocorrosion behaviour was characterized by in situ application of electrochemical techniques. HCCoCr alloy immersed in PBS-HA showed the best tribocorrosion behaviour with the lowest COF. In this case, in situ measurement of corrosion potential and the impedance data under wear corrosion process showed an active state while passive film was continuously destroyed without possibility of regeneration.