• 제목/요약/키워드: oxidation reaction

검색결과 1,989건 처리시간 0.034초

N3S-ligated Copper(II) Complex Catalyzed Selective Oxidation of Benzylic Alcohols to Aldehydes under Mild Reaction Conditions

  • Dharmalingam, Sivanesan;Koo, Eunhae;Yoon, Sungho;Park, Gyoosoon
    • Bulletin of the Korean Chemical Society
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    • 제35권3호
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    • pp.715-720
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    • 2014
  • A Cu(II) complex with an three nitrogens and one sulfur coordination environment was synthesized and characterized. Its redox potential was observed at 0.483 V vs. NHE, very similar to that of a Cu-containing fungal enzyme, galactose oxidase, which catalyzes the oxidation of alcohols to corresponding aldehydes with the concomitant reduction of molecular oxygen to water. The Cu(II) complex selectively oxidizes the benzylic alcohols using TEMPO/$O_2$ under mild reaction conditions to corresponding aldehydes without forming any over-oxidation product. Moreover, the catalyst can be recovered and reused multiple times for further oxidation reactions, thus minimizing the waste generation.

Evaluation of effective process for oxidation and coagulation by ferrous ion and hydrogen peroxide

  • Moon, H.J.;Kim, Y.M.;Lee, S.H.
    • 한국환경과학회:학술대회논문집
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    • 한국환경과학회 2003년도 가을 학술발표회 발표논문집
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    • pp.319-321
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    • 2003
  • This research was carried out to evaluate the removal efficiencies of CODcr and colour for the dyeing wastewater by ferrous solution in Fenton process. The results showed that COD was mainly removed by Fenton coagulation, where the ferric ions are formed in the initial step of Fenton reaction. On the other hand colour was removed by Fenton oxidation rather than Fenton coagulation. The removal mechanism of CODcr and colour was mainly coagulation by ferrous ion, ferric ion and Fenton oxidation. The removal efficiencies were dependent on the ferric ion amount at the beginning of the reaction. However the final removal efficiency of COD and colour was in the order of Fenton oxidation, ferric ion coagulation and ferrous ion coagulation. The reason of the highest removal efficiency by Fenton oxidation can be explained by the chain reactions with ferrous solution, ferric ion and hydrogen peroxide.

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Effect of Al Alloy Content on Processing of Reaction-Bonded Al2O3 Ceramics Using Al Alloy Powder

  • Lee, Hyun-Kwuon
    • 한국재료학회지
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    • 제25권5호
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    • pp.215-220
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    • 2015
  • The effect of Al content on the processing of reaction-bonded $Al_2O_3$ (RBAO) ceramics using 40v/o ~ 80v/o Al-Zn-Mg alloy powder was studied in order to improve traditional RBAO ceramic processes that use ~ 40v/o pure Al powder. The influence of high Al content in starting $Al_2O_3$-Al alloy powder mixtures on its particulate characteristics, reaction-bonding, microstructure, physical and mechanical properties was revealed. Starting $Al_2O_3$-Al alloy powder mixtures with 40v/o ~ 80v/o Al alloy powder were milled, reaction-bonded, post-sintered, and characterized. With an increasing Al alloy content, the milling efficiency of Al alloy powder was lowered, resulting in a larger particle size after milling. However, in spite of the larger particle size of Al alloy powder, the oxidation, i.e., reaction-bonding, of the Al alloy was successfully completed via solid and liquid state oxidation, in which the activation energy of the oxidation was nearly the same regardless of Al alloy content. After reaction-bonding and post-sintering at $1600^{\circ}C$, RBAO ceramics from 80v/o Al alloy content showed a relative density of ~97% and a flexural strength of 251 MPa compared to ~ 96% and 353 MPa for RBAO ceramics from 40v/o Al alloy content, respectively. The lower flexural strength at 80v/o Al alloy content was due to the weak spinel phase that formed from Zn, Mg alloying elements in Al.

백금계 촉매상에서 산화질소(NO)의 산화반응속도에 관한 실험 및 모델링 연구 (An Experimental and Modeling Study on the Oxidation Kinetics of Nitric Oxide over Platinum-based Catalysts)

  • 김영득;정수진;김우승
    • 한국자동차공학회논문집
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    • 제20권5호
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    • pp.71-80
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    • 2012
  • To improve the $NO_X$ conversion over a SCR (selective catalytic reduction) catalyst, the DOC (diesel oxidation catalyst) is usually placed upstream of the SCR catalyst to enhance the fast SCR reaction ($4NH_3+2NO+2NO_2{\rightarrow}4N_2+6H_2O$) using equimolar amounts of NO and $NO_2$. Here, a ratio of $NO_2/NO_X$ above 50% should be avoided, because the reaction with $NO_2$ only ($4NH_3+4NO+O_2{\rightarrow}4N_2+6H_2O$) is slower than the standard SCR reaction ($4NH_3+4NO+O_2{\rightarrow}4N_2+6H_2O$). In order to accurately predict the performance characteristics of SCR catalysts, it is therefore desired to develop a more simple and reliable mathematical and kinetic models on the oxidation kinetics of nitric oxide over a DOC. In the present work, the prediction accuracy and limit of three different chemical reaction kinetics models are presented to describe the chemicophysical characteristics and conversion performance of DOCs. Steady-state experiments with DOCs mounted on a light-duty four-cylinder 2.0-L turbocharged diesel engine then are performed, using an engine-dynamometer system to calibrate the kinetic parameters such as activation energies and preexponential factors of heterogeneous reactions. The reaction kinetics for NO oxidation over Pt-based catalysts is determined in conjunction with a transient one-dimensional (1D) heterogeneous plug flow reactor (PFR) model with diesel exhaust gas temperatures in the range of 115~$525^{\circ}C$ and space velocities in the range of $(0.4{\sim}6.5){\times}10^5\;h^{-1}$.

Consideration of reversed Boudouard reaction in solid oxide direct carbon fuel cell (SO-DCFC)

  • Vahc, Zuh Youn;Yi, Sung Chul
    • Journal of Ceramic Processing Research
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    • 제19권6호
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    • pp.514-518
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    • 2018
  • The direct carbon fuel cell (DCFC) has attracted researcher's attention recently, due to its high conversion efficiency and its abundant fuel, carbon. A DCFC mathematical model has developed in two-dimensional, lab-scale, and considers Boudouard reaction and carbon monoxide (CO) oxidation. The model simulates the CO production by Boudouard reaction and additional electron production by CO oxidation. The Boudouard equilibrium strongly depends on operating temperature and affects the amount of produced CO and consequentially affects the overall fuel cell performance. Two different operating temperatures (973 K, 1023 K) has been calculated to discover the CO production by Boudouard reaction and overall fuel cell performance. Moreover, anode thickness of the cell has been considered to find out the influence of the Boudouard reaction zone in fuel cell performance. It was found that in high temperature operating DCFC modeling, the Boudouard reaction cannot be neglected and has a vital role in the overall fuel cell performance.

산화반응에 의한 이방성 메조페이스 탄소섬유의 구조 변화(II)-주사전자현미경을 이용한 표면구조 관찰 (Structural Changes during Oxidation Process of Anisotopic Mesophase Carbon Fibers(II)-Surface Texture Observation by Scanning Electron Microscopy)

  • 노재승
    • 한국재료학회지
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    • 제13권12호
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    • pp.831-838
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    • 2003
  • Anisotropic mesophase carbon fiber(AMCFs) was exposed to isothermal oxidation in air and $CO_2$atmosphere, and burn-off rates have measured by TGA. The microstructure changes of oxidized carbon fibers, were observed by SEM. It was observed that oxidation rate in the air is over 100 times faster than that in $CO_2$atmosphere. The activation energy obtained in air was about 43.4 Kcal/mole in the temperature range of $600∼800^{\circ}C$, and in $CO_2$was about 55.2 Kcal/mole in the temperature range of $950∼1200^{\circ}C$. Therefore, the oxidation reaction in both atmospheres was under chemical reaction regime in the above temperature ranges. It was shown that the oxidation of the AMCFs is initiated at the end of fibers at high temperature($1100^{\circ}C$) with developing the large pores, and the small pores are developed on the fiber surface at low temperature($900^{\circ}C$). In conclusion, the oxidation of the AMCFs is progressed through the imperfection.

자일렌의 기상 산화반응에서의 반응 메카니즘과 담체영향 (Reaction Mechanism and Support Effect for the Gas-Phase Oxidation of o-Xylene)

  • 이근대;이호인
    • 공업화학
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    • 제2권2호
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    • pp.155-164
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    • 1991
  • o-자일렌 산화반응의 반응메카니즘과 촉매활성에 대한 산화바나듐의 산화상태 및 담체의 영향을 연구하였다. o-자일렌의 산화반응은 연계반응 메카니즘 및 병렬반응 메카니즘에 의해 동시에 진행되는 것으로 나타났다. 높은 산화수를 지닌 산화바나듐은 무수프탈산으로의 선택적 산화반응에 유리한 것으로 나타났고, 반면에 낮은 산화수의 경우는 무수프탈산의 CO 및 $CO_2$로의 완전 산화반응을 유발함을 알 수 있었다. 그리고 결정성 $V_2O_5$가 낮은 비결정성의 경우보다 부분 산화반응에 대한 높은 선택도를 나타내었다.

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비스페놀A와 니트로벤젠의 펜톤 산화분해 특성 (A Study on the Characteristics of Fenton Oxidation of Bisphenol A and Nitrobenzene)

  • 배수진;권희원;김지영;황인성;김영훈
    • 한국환경과학회지
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    • 제30권12호
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    • pp.1005-1014
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    • 2021
  • Organic contaminants can be released into water environments due to chemical accidents and exist as dissolved and non-aqueous phase liquids (NAPL). Fenton oxidation was tested for bisphenol A and nitrobenzene as model organic contaminants in dissolved and NAPL states. Fenton oxidation was successfully applied for both of the dissolved and NAPL states of the two pollutants and the results indicated that a quick treatment was needed to reduce the risk from a chemical accidents instead of carrying out oxidation after the contaminants dissolve in water. A set of Fenton reactions were tested under seawater conditions because chemical accidents often occurs in the ocean. Chloride ions act as radical scavengers and inhibit Fenton oxidation. The reaction rate is inversely proportional to salt contents and the reduced reaction rate can be compensated by increasing the quantity of the oxidizing agents. The current study showes that Fenton oxidation could be applied as a quick treatments for organic contaminant in dissolved and NAPL state organic contaminants released as a result of leaks or chemical accidents.

물과 에탄올의 혼합용매로부터 니켈 미분말의 합성 및 산화특성 (Synthesis of nickel fine powder in the mixed solvent of water and ethanol and ie oxidation behaviors)

  • 이상근;최은영;이윤복;김광호;박희찬
    • 한국결정성장학회지
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    • 제13권3호
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    • pp.139-144
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    • 2003
  • 유기용매로서 에탄올을 함유한 염화니켈 수용액으로부터 니켈 미분말을 제조하고 이들의 산화특성을 검토하였다. 에탄올을 함유한 염화니켈 수용액에서 히드라진의 환원반응은 반응온도에 크게 의존하였다. 히드라진에 의한 환원반응시간은 반응온도가 증가함에 따라 감소하였다. 반응온도를 제어함으로써 입경이 0.1 $\mu\textrm{m}$-1.0 $\mu\textrm{m}$ 범위를 갖는 구형 분말을 얻을 수 있었다. 또한, 반응온도가 증가함에 따라 입경은 다소 증가하였고 조대한 입자들의 존재로 인하여 넓은 입도 분포를 나타내었다. $60^{\circ}C$에서 합성된 니켈 분말의 평균 입경과 비표면적은 각각 0.3 $\mu\textrm{m}$와 31.8 $m^2$/g이었다. $300^{\circ}C$에서 니켈 분말의 중량감소는 $Ni(OH)_2$의 분해반응에 기인한 것이다. $200^{\circ}C$ 공기중에서 가열처리한 경우 내산화성은 합성 분말보다 현저하였다

펜톤 산화에 의한 하수 슬러지로부터 유기산 생성에 관한 연구 (A Study on the Production of VFAs from Sewage Sludge by Fenton's Oxidation)

  • 한금석;남영우
    • 대한환경공학회지
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    • 제27권2호
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    • pp.184-190
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    • 2005
  • 하수 슬러지를 펜톤 산화공정으로 처리하는 새로운 VFAs 생산 공정을 연구하였다. 과산화수소와 촉매인 $Fe^{2+}$의 적정농도를 실험하고, 최적 반응온도 및 반응시간에 대한 기초 자료를 얻고자 하였다. 기존의 과산화수소를 액상산화제로 사용한 공정보다 저농도의 $Fe^{2+}$를 촉매로 사용하는 펜톤 산화공정으로 과산화수소의 사용량을 대폭 감소시키고도 VFAs 생성량이 4배 정도 증가하는 결과를 얻었다. 과산화수소와 $Fe^{2+}$의 적정 농도는 각각 0.62 M과 0.007M 이었다. VFAs 생성반응은 초기 1분 이내에서 빠르게 진행되었으며 생성된 VFAs의 일부가 초산과 $CO_2$로 분해되는 연속반응의 특성이 나타났다. 경제성을 감안하면 반응온도는 $25^{\circ}C$, 반응시간은 10분 정도가 적절한 반응조건으로 생각된다. 초기 pH $3{\sim}6.3$에서 VFAs의 생성에 미치는 pH의 영향은 관찰되지 않았다.