• 제목/요약/키워드: Reaction metal

검색결과 2,156건 처리시간 0.028초

Cu-Zn 금속합금의 산화 환원반응과 Al-Silicate의 흡착반응을 이용한 폐수 중 중금속처리에 관한 연구 (A Study on the Treatment of Heavy Metal in Wastewater by Redox Reaction of Cu-Zn Metal Alloy and Adsorption reaction of Al-Silicate)

  • 이수정;김종화;송주영
    • 한국응용과학기술학회지
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    • 제33권3호
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    • pp.441-448
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    • 2016
  • 본 연구는 구리 아연 금속합금의 산화 환원 반응과 합성 알루미늄 실리케이트의 흡착 반응을 이용한 폐수 중 중금속 처리에 관한 연구이다. 극세사 형태로 제조된 구리 아연 금속합금이 수용액 중에서 산화 환원반응에 의해 아연보다 이온화 경향이 작은 중금속은 환원 처리되고, 이온화 된 아연 및 미반응 중금속은 흡착 처리하여 제거하는 연구이다. 극세사 형태로 제조된 금속합금 물질은 표면적이 커서 1회 처리만으로도 반응 평형에 도달하게 하여 효율이 높은 것으로 나타났다. 크롬($Cr^{+3}$)은 redox 반응 1회 처리만으로도 100.0 % 제거 되었으며, 수은은 98.0 %, 주석 92.0 %, 구리는 91.4 % 정도 제거되었다. 카드뮴, 니켈, 납도 각각 40.0 %, 50.0 %, 58.0 %가 제거 되었다. 크롬($Cr^{+3}$)은 아연과 이온화 경향 차이가 거의 없지만 제거 효율이 높은 것으로 나타났는데 이는 3가 크롬은 이온 상태로 존재하면 redox 반응에서 발생한 $OH^-$ 이온과 결합하여 수산화물 침전을 형성하는 것으로 판단된다. Redox 반응 후 증가한 아연 및 미반응 중금속 농도를 알루미늄실리케이트를 1회 통과하여 거의 100.0 % 제거할 수 있었다. 이는 합성 알루미늄 실리케이트의 비표면적이 크고 금속 이온의 흡착능력이 우수한 것으로 나타났으며, 반응 후 알루미늄 이온은 증가하지 않는 것으로 보아 이온 교환이 아닌 흡착으로 아연 및 중금속 이온들을 제거할 수 있는 것으로 나타났다.

귀금속 계열 촉매의 수성가스전환반응특성과 유효인자 (Noble metal catalysts for water gas shift reaction and their effectiveness factor)

  • 임성광;배중면;김기현
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2008년도 춘계학술대회 논문집
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    • pp.514-517
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    • 2008
  • Water gas shift(WGS) is an important step in fuel process for fuel cells, and improperness of commercial WGS catalysts for use in fuel cell systems has prompted numerous researches on noble metal catalysts. A selected noble metal catalyst for water gas shift reaction(WGS) was prepared with various metal loadings. The prepared catalysts were tested under two feeding conditions. At moderate residence time, carbon monoxide conversion was much higher on the noble metal catalysts as compared to commercial high-temperature shift catalyst. Effects of metal loading were examined by activity tests at short residence time. Higher metal loading effected higher reaction rate. The kinetic data was fitted to simple reaction equations and effectiveness factor was estimated. The results suggest the necessity of a structural design for the highly active noble metal catalysts.

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APPLICATION OF DISPROPORTIONATION REACTION TO SURFACE TREATMENT

  • Oki, Takeo
    • 한국표면공학회지
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    • 제29권5호
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    • pp.478-481
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    • 1996
  • Disproportionation reaction is very important and interesting reaction to be applied to such surface treatment as metal, alloy, compound coating, a surface etching and so on. In gaseous system, the reaction of Al chloride is applied to Al and Al alloy coating, and the similar reaction of Ti chloride is also used for Ti, Ti alloy and Ti compound coating. As for aqueous system, this reaction is utilized to such metal coat as Sn etc. and metal etching such as Cu, Fe and so on. Also in molten salts system, this reaction has many application for surface treatment like metal, alloy and compound coatings for corrosion, wear, heat resistance and so forth. For instance, carbide film, nitride film, boride film, alloy film, quite new different film from the components of substrate material are coated in single and multiple component film system by the disproportionation reaction.

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Controlled Conversion of Sodium Metal From Nuclear Systems to Sodium Chloride

  • Herrmann, Steven;Zhao, Haiyan;Shi, Meng;Patterson, Michael
    • 방사성폐기물학회지
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    • 제19권2호
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    • pp.233-241
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    • 2021
  • A series of three bench-scale experiments was performed to investigate the conversion of sodium metal to sodium chloride via reactions with non-metal and metal chlorides. Specifically, batches of molten sodium metal were separately contacted with ammonium chloride and ferrous chloride to form sodium chloride in both cases along with iron in the latter case. Additional ferrous chloride was added to two of the three batches to form low melting point consolidated mixtures of sodium chloride and ferrous chloride, whereas consolidation of a sodium-chloride product was performed in a separate batch. Samples of the products were characterized via X-ray diffraction to identify attendant compounds. The reaction of sodium metal with metered ammonium chloride particulate feeds proceeded without reaction excursions and produced pure colorless sodium chloride. The reaction of sodium metal with ferrous chloride yielded occasional reaction excursions as evidenced by temperature spikes and fuming ferrous chloride, producing a dark salt-metal mixture. This investigation into a method for controlled conversion of sodium metal to sodium chloride is particularly applicable to sodium containing elevated levels of radioactivity-including bond sodium from nuclear fuels-in remote-handled inert-atmosphere environments.

有機할로겐化合物과 金屬과의 反應 (第 3 報) 有機클로로酸 및 에스터와 各種金屬과의 反應生成物 및 反應系中의 金屬分布에 關하여 (Reaction of Organic Halogen Compounds with metals (Part III) Metal Distribution in the Reaction Products and System of a Reaction between Organo Chloro Acid or Ester and Metals under Various Solvents)

  • 김유선
    • 대한화학회지
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    • 제9권1호
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    • pp.61-65
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    • 1965
  • 有機클로로酸, 또는 에스타와 各種金屬(亞鉛, 硅素, 마그네슘, 錫)과의 여러 溶媒存在下(아세트나이트라일, 디옥센 및 토루엔)의 反應에서 얻은 反應生成物, 또는 反應系中의 金屬分布狀態를 (n,${\gamma}$)反應으로 製造한 各種放射性 金屬트레이서를 使用하여 決定하였다. 有機클로로 金屬 콤푸렉스의 溶解度는 親水性溶媒에서는 顯著하게 增加하였으며, 無極性溶媒에는 減少하였다. 이 事實은 回收된 金屬, 또는 回收된 金屬混合物의 水洗液中의 金屬分布狀態의 增加로서 確認되었다. 카보닐化合物 存在下에서 反應시켰 때에도 같은 事實을 나타내었다. 親水性溶媒中의 金屬콤푸렉스의 溶解度는 亞鉛, 硅素, 錫 및 마그네슘이 順序로 減少되었으며 無極性溶媒下에서는 硅素, 錫, 마그네슘 및 亞鉛의 順으로 減少되었다. 有機할로겐化合物과 金屬과의 反應生成物로 普通 豫期되는 有機金屬化合物은 全反應을 通하여 거의 없었다. 反應結果를 論議하였으며, 本反應過程에서 觀察한 溶媒의 影響에 關하여 論及하였다.

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다공성 촉매 분리막을 이용한 수증기 개질 반응 특성 연구 (A Study on the Reaction Characteristics of Steam Reforming Reaction over Catalyzed Porous Membrane)

  • 홍성창;이상문
    • 공업화학
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    • 제25권2호
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    • pp.198-203
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    • 2014
  • 본 연구에서는 Ni metal foam 플레이트의 수증기 개질반응 및 표면 특성을 조사하였다. 전처리를 통하여 Ni의 산화상태를 변화시킬 수 있었으며, 활성 site로서 표면에 노출된 metallic Ni 종은 수증기 개질 반응활성에 중요한 역할을 한다. 또한 Ni metal foam 플레이트의 기공제어 및 촉매 기능을 부여하기 위하여 Ni metal foam 플레이트와 Ni-YSZ 촉매를 혼합하여 다공성 촉매 분리막을 제조하였다. SEM 분석 결과 metal foam 플레이트의 기공을 제어할 수 있었으며, 표면에 Ni-YSZ 촉매는 고르게 잘 분포되어 있었다. Ni 기반 다공성 촉매 분리막은 공간속도에 상관없이 상용촉매와 유사한 수증기 개질 활성을 가진다.

순수 티타늄 주조체의 주형온도에 따른 용탕반응성 및 표면거칠기 (Metal-Mold Reaction and Surface Roughness Measurement of Pure Titanium Casting Specimens with Mold Temperatures)

  • 차성수;송영주;박수철
    • 대한치과기공학회지
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    • 제32권4호
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    • pp.297-305
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    • 2010
  • Purpose: The purpose of this study was to observe the change of metal-mold reaction and surface roughness in titanium casting specimens for phosphate-silica alumina bonded investment with mold temperatures. Methods: The metal-phosphate silica alumina bonded mold interface reaction and surface roughness of titanium casting specimens according to mold temperatures were investigated. The Specimens were analysed by scanning electron microscopy and surface roughness tester. Results: The oxidation behavior indicated by the growth of oxide thickness. The titanium-oxide layer were consisted two layer of a porous external and a dense internal one. The reaction layer and surface roughness increased with increasing investment material temperature. Conclusion: In this work, The most suitable mold temperature in casting of pure titanium was $200^{\circ}C$.

질화알루미늄과 금속간 계면접합에 관한 연구: 계면반응과 미세구조 형성이 접합체 강도에 미치는 영향 (Joining of AIN Ceramics to Metals: Effect of Reactions and Microstructural Developments in the Bonded Interface on the Joint Strength)

  • 박성계
    • 한국분말재료학회지
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    • 제4권3호
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    • pp.196-204
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    • 1997
  • Joining of AIN ceramics to W and Cu by active-metal brazing method was tried with use of (Ag-Cu)-Ti alloy as insert-metal. Joints were produced under various conditions of temperature, holding time and Ti-content in (Ag-Cu) alloy Reaction and microstructural development in bonded interface were investigated through observation and analysis by SEM/EDS, EPMA and XRD. Joint strengths were measured by shear test. Bonded interface consists of two layers: an insert-metal layer of eutectic Ag- and Cu-rich phases and a reaction layer of TiN. Thickness of reaction layer increases with bonding temperature, holding time and Ti-content of insert-metal. It was confirmed that the growth of reaction layer is a diffusion-controlled process. Activation energy for this process was 260 KJ/mol which is lower than that for N diffusion in TiN. Maximum shear strength of 108 MPa and 72 MPa were obtained for AIN/W and AIN/Cu joints, respectively. Relationship between processing variables, joint strength and thickness of reaction layer was also explained.

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Ag-Cu-Ti Brazing 금속을 이용한 Inconel/$Si_3N_4$ 접합의 계면구조 (Interfacial Structure of Inconel/$Si_3N_4$ Joint Using Ag-Cu-Ti Brazing Metal)

  • 정창주;장복기;문종하;강경인
    • 한국세라믹학회지
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    • 제33권12호
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    • pp.1421-1425
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    • 1996
  • Sintered Si3N4 and Inconel composed of Ni(58-63%) Cr(21-25%) Al(1-17%) Mn(<1%) fe(balance) were pressurelessly joined by using Ag-Cu-Ti brazing filler metal at 950℃ and 1200℃ under N2 gas atmosphere of 1atm and their interfacial structures were investigated. In case that the reaction temperature was low as 950℃ its interfacial structure was "Inconel metal/Ti-rich phase layer/brazing filler metal layer/Si3N4 " Ti used as reactive metal existed in between inconel steel and brazing metal and moved to the interface of between brazing filler metal nd Si3N4 according as reaction temperature increased up to 1200℃. The interfacial structure of inconel steel-Si3N4 reacted at 1200℃ was ' inconel metal/Ni-rich phase layer containing of Fe. Cr and Si/Cu-rich phase layer containing of Mn and Si/Si3N4 " Cr Mn, Ni and Fe diffused to the interface of between brazing filler metal and Si3N4 and reacted with Si3N4 The most reactive components of ingredients of inconel metal were Cr and Mn. On the other hand Ti added as reactive components to Ag-Cu eutectic segregated into Ni-rich phase layer,.

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유기금속 촉매를 사용한 Succinic Acid과 1,4-butanediol의 에스테르화반응에 관한 연구 (A Study on the Esterification Reaction of Succinic Acid and 1,4-butanediol Using an Organic Metal Catalysts)

  • 박근호
    • 한국응용과학기술학회지
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    • 제26권4호
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    • pp.415-421
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    • 2009
  • Esterification reaction between succinic acid[SA] and 1,4-butanediol [BD} was kinetically investigated in the presence of organic metal catalysts (alkyl-silver oxide(ASO),CAT 100E) at $150{\sim}190^{\circ}C$. The reaction rates measured by the amount of distilled water from the reaction vessel. The esterification reaction was carried out under the first order kinetics with respect to the concentration of reactants and catalyst, respectively. The overall reaction order was 2nd. From the examination of relationship between apparent reaction rate constants and reciprocal absolute temperature, the activation energy has been calculate as 146.70 kJ/mol with ASO catalyst and 43.04 kJ/mol with CAT 100E catalyst.