• 제목/요약/키워드: iron kinetics

검색결과 101건 처리시간 0.029초

Fe-TNU-9 제올라이트 상에서 아산화질소의 분해반응 속도론 (Kinetics of N2O Decomposition over Fe-TNU-9 Zeolite)

  • 박정현;전성희;위엔반과;신채호
    • 공업화학
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    • 제20권4호
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    • pp.453-458
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    • 2009
  • Fe의 함량을 0.5~3.3 wt%의 범위에서 이온 교환하여 제조한 Fe-TNU-9 제올라이트 촉매상에서 $N_2O$ 농도를 2000~8500 ppm, 반응온도를 $300{\sim}550^{\circ}C$ 범위 내에서 $N_2O$ 직접분해반응을 수행하였다.제조된 촉매는 X-선 회절분석, 질소흡착, 주사전자현미경 등으로 특성분석을 수행하였다. 최적 Fe 함량은 2.7 wt%로 그 이상의 함량에 있어 Fe 함량은 $N_2O$ 직접분해반응에 큰 영향을 미치지 않았다. 이온교환 후에 TNU-9의 XRD 상으로는 안정된 상태를 유지하였지만 0.01 M Fe 용액 하에서 이온 교환한 3.1 wt% Fe-TNU-9 제올라이트는 H-TNU-9에 비해 최대 60%까지의 결정화도가 감소하였다. 이러한 결정화도의 감소는 비표면적 및 기공부피와 연관질 수 있지만 감소정도는 약 10% 정도로 결정화도 감소와 비교하면 영향은 크지 않았다. 멱차수법을 이용한$N_2O$ 분해반응에 있어$N_2O$ 부분 반응차수는 $420^{\circ}C$에서 0.69, $464^{\circ}C$에서 0.97차까지 변화하였다. 활성화 에너지는$N_2O$의 농도가 증가하면 같은 경향으로 증가하였고, 34~43 kcal/mol 범위 내에서 넓게 분포하였다.

다이옥신의 환원적 탈염화 분해 경로와 독성 변화예측을 위한 LFER 모델 (Prediction of Pathway and Toxicity on Dechlorination of PCDDs by Linear Free Energy Relationship)

  • 김지훈;장윤석
    • 대한환경공학회지
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    • 제31권2호
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    • pp.125-131
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    • 2009
  • 영가철과 혐기성 미생물을 이용한 환원적 탈염화반응을 통한 다이옥신 처리 능력을 평가하기 위해, 자유에너지 선형관계(linear free energy relationship)를 이용하여 다이옥신의 탈염화에 의한 농도 및 독성변화 예측 모델을 최초로 정립하였다. 수용액상에 존재하는 다이옥신류의 깁스자유에너지는 기존 문헌의 열역학적 계산결과를 범밀도함수이론(density functional theory)을 이용한 계산 수준으로 보정하였으며, 보정된 깁스자유에너지와 실험을 통해 얻은 탈염화 반응속도 상수와의 선형관계를 통해 다이옥신의 탈염화 반응 256개에 대한 반응속도상수를 예측하였다. 본 모델을 통해 탈염화에 의해 변화하는 다이옥신 류 76종에 대한 시간 별 농도를 계산할 수 있다. 8염화다이옥신(Octachlorinated dibenzo-p-dioxin, OCDD)이 완전히탈염화되어 dibenzo-p-dioxin (DD)로 탈염화되기까지는 100년 이상의 반응시간이 필요하였으며, 독성등가값(toxic equivalent quantity, TEQ)의 경우 탈염화가 진행되면서 초기농도의 10배 이상까지 증가하는 것으로 밝혀졌다. 이를 통해, 다이옥신의 처리를 위해서는 좀 더 빠른 탈염화 반응속도를 갖는 다른 전자공여 시스템을 사용하거나, 환원적 탈염화-라디칼 산화와 같은 복합 연계처리가 필요함을 알 수 있다. 본 논문을 통해 제시된 예측 기법은 다이옥신뿐 아니라 다른 할로겐화 화합물의 탈염화 예측과 여러 전자공여 시스템에 대한 평가에 적용이 가능하다.

Application of Ferrate(VI) on the Decomplexation of Cu(II)-EDTA

  • Tiwari, Diwakar;Yang, Jae-Kyu;Chang, Yoon-Young;Lee, Seung-Mok
    • Environmental Engineering Research
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    • 제13권3호
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    • pp.131-135
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    • 2008
  • In this study, Fe(VI) was employed as a multi-functional agent to treat the simulated industrial wastewater contaminated with Cu(II)-EDTA through oxidation of EDTA, decomplexation of Cu(II)-EDTA and subsequent removal of free copper through precipitation. The decomplexation of $10^{-4}\;M$ Cu(II)-EDTA species was performed as a function of pH at excess concentration of Fe(VI). It was noted that the acidic conditions favor the decomplexation of Cu(II)-EDTA as the decomplxation was almost 100% up to pH 6.5, while it was only 35% at pH 9.9. The enhanced degradation of Cu(II)-EDTA with decreasing the pH could be explained by the different speciation of Fe(VI). $HFeO_4^-$ and $H_2FeO_4$, which are relatively more reactive than the unprotonated species $FeO_4^{2-}$, are predominant species below neutral pH. It was noted that the decomplexation reaction is extremely fast and within 5 to10 min of contact, 100% of Cu(II)-EDTA was decomplexed at pH 4.0. However, at higher pH (i.e., pH 10.0) the decomplexation process was relatively slow and it was observed that even after 180 min of contact, maximum ca 37% of Cu(II)-EDTA was decomplexed. In order to discuss the kinetics of the decomplexation of Cu(II)-EDTA, the data was slightly fitted better for the second order rate reaction than the first order rate reaction in the excess of Fe(VI) concentration. On the other hand, the removal efficiency of free Cu(II) ions was also obtained at pH 4.0 and 10.0. It was probably removed through adsorption/coagulation with the reduced iron i.e., Fe(III). The removal of total Cu(II) was rapid at pH 4.0 whereas, it was slow at pH 10.0. Although the decomplexation was 100% at lower pH, the removal of free Cu(II) was relatively slow. This result may be explicable due to the reason that at lower pH values the adsorption/coagulation capacity of Fe(III) is greatly retarded. On the other hand, at higher pH values the decomplexation of Cu(II)-EDTA was partial, hence, slower Cu(II) removal was occurred.

Aluminum Powder Metallurgy Current Status, Recent Research and Future Directions

  • Schaffer, Graham
    • 한국분말야금학회:학술대회논문집
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    • 한국분말야금학회 2001년도 추계학술강연 및 발표대회
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    • pp.7-7
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    • 2001
  • The increasing interest in light weight materials coupled to the need for cost -effective processing have combined to create a significant opportunity for aluminum P/M. particularly in the automotive industry in order to reduce fuel emissions and improve fuel economy at affordable prices. Additional potential markets for Al PIM parts include hand tools. Where moving parts against gravity represents a challenge; and office machinery, where reciprocating forces are important. Aluminum PIM adds light weight, high compressibility. low sintering temperatures. easy machinability and good corrosion resistance to all advantages of conventional iron bm;ed P/rv1. Current commercial alloys are pre-mixed of either the AI-Si-Mg or AL-Cu-Mg-Si type and contain 1.5% ethylene bis-stearamide as an internal lubricant. The powder is compacted in closed dies at pressure of 200-500Mpa and sintered in nitrogen at temperatures between $580~630^{\circ}C$ in continuous muffle furnace. For some applications no further processing is required. although most applications require one or more secondary operations such as sizing and finishing. These sccondary operations improve the dimension. properties or appearance of the finished part. Aluminum is often considered difficult to sinter because of the presence of a stable surface oxide film. Removal of the oxide in iron and copper based is usually achieved through the use of reducing atmospheres. such as hydrogen or dissociated ammonia. In aluminum. this occurs in the solid st,lte through the partial reduction of the aluminum by magncsium to form spinel. This exposcs the underlying metal and facilitates sintering. It has recently been shown that < 0.2% Mg is all that is required. It is noteworthy that most aluminum pre-mixes contain at least 0.5% Mg. The sintering of aluminum alloys can be further enhanced by selective microalloying. Just 100ppm pf tin chnnges the liquid phase sintering kinetics of the 2xxx alloys to produce a tensile strength of 375Mpa. an increilse of nearly 20% over the unmodified alloy. The ductility is unnffected. A similar but different effect occurs by the addition of 100 ppm of Pb to 7xxx alloys. The lend changes the wetting characteristics of the sintering liquid which serves to increase the tensile strength to 440 Mpa. a 40% increase over unmodified aIloys. Current research is predominantly aimed at the development of metal matrix composites. which have a high specific modulus. good wear resistance and a tailorable coefficient of thermal expnnsion. By controlling particle clustering and by engineering the ceramic/matrix interface in order to enhance sintering. very attractive properties can be achicved in the ns-sintered state. I\t an ils-sintered density ilpproaching 99%. these new experimental alloys hnve a modulus of 130 Gpa and an ultimate tensile strength of 212 Mpa in the T4 temper. In contest. unreinforcecl aluminum has a modulus of just 70 Gpa.

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신규(新規) 살충제(殺蟲劑)인 O, O, O-Diethyl-O-(1-phenyl-3-trifluoromethyl-5-pyrazoyl) thiophosphoric acid ester의 열(熱)에 의한 분해성(分解性) (Thermal Decomposition of A New Insecticide KH-502 [O, O-Diethyl O-(1-phenyl -3-trifluoromethy-5-pyrazoyl) thiophosphoric acid ester])

  • 조부연;한대성
    • 한국환경농학회지
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    • 제11권3호
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    • pp.225-234
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    • 1992
  • Thermal decomposition was conducted to investigate the influence of the various factors on stability of a new insecticide, [O, O-Diethyl O-(1-phenyl-3-trifluoromethyl-5-pyrazoyl) thiophosphoric acid ester : KH-502], in view of those informations applicable for industrial exploitation. In the thermal decomposition experiment, KH-502 was, after mixing with Fe, Cu and adjustment of moisture and pH conditions, subjected to three temperatures, 25, 50, and $100^{\circ}C$. Results for stability, and degradation pattern of KH-502 from the above experiment can be summarized as follows: 1. Main products of the thermal decomposition when this was conducted in the closed system were identified as following five compounds:O, O, O-Triethylthiophosphoric acid(TEPA), 1-Phenyl-3-trifluoromethyl-5-ethoxypyrazole(PTMEP), 1-Phenyl-2-ethyl-3-trifluoromethyl-5-hydroxypyrazole(PETMHP), O, O-Diethyl O-(1-phenyl-3-trifluoromethyl-5-pyrazoyl)phosphoric acid ester(KH-502 oxo form), O, S-Diethyl O-(1-phenyl-3-trifluoromethyl-5-pyrazoyl)phospho rothiolate(S-ethyl KH-502). However, compounds such as oxo form and S-ethyl KH-502 were not identified when the thermal decomposition was proceeded in the open system. 2. KH-502 was stable at 25 and 50$^{\circ}C$, but it was decomposed at 100$^{\circ}C$ following the first-order kinetics at the early stages of decomposition. 3. Rate constants for the thermal decomposition of KH-502 at 100$^{\circ}C$ were in the orders of Cu powder addition 0.344>Cu plate addition 0.21>moisture addition 0.05>closed system=open system=iron addition=pH 5.5 adjustment 0.04>pH 8.5 adjustment 0.027 day$^{-1}$, representing KH-502 was decomposed fast at Cu powder treatment and slow at pH 8.5 adjustment. 4. Half-life for the thermal decomposition of KH-502 at 100$^{\circ}C$ was in the orders of Cu powder addition 2.02

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Structural and Kinetic Characteristics of 1,4-Dioxane-Degrading Bacterial Consortia Containing the Phylum TM7

  • Nam, Ji-Hyun;Ventura, Jey-R S.;Yeom, Ick Tae;Lee, Yongwoo;Jahng, Deokjin
    • Journal of Microbiology and Biotechnology
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    • 제26권11호
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    • pp.1951-1964
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    • 2016
  • 1,4-Dioxane-degrading bacterial consortia were enriched from forest soil (FS) and activated sludge (AS) using a defined medium containing 1,4-dioxane as the sole carbon source. These two enrichments cultures appeared to have inducible tetrahydrofuran/dioxane and propane degradation enzymes. According to qPCR results on the 16S rRNA and soluble di-iron monooxygenase genes, the relative abundances of 1,4-dioxane-degrading bacteria to total bacteria in FS and AS were 29.4% and 57.8%, respectively. For FS, the cell growth yields (Y), maximum specific degradation rate ($V_{max}$), and half-saturation concentration ($K_m$) were 0.58 mg-protein/mg-dioxane, $0.037mg-dioxane/mg-protein{\cdot}h$, and 93.9 mg/l, respectively. For AS, Y, $V_{max}$, and $K_m$ were 0.34 mg-protein/mg-dioxane, $0.078mg-dioxane/mg-protein{\cdot}h$, and 181.3 mg/l, respectively. These kinetics data of FS and AS were similar to previously reported values. Based on bacterial community analysis on 16S rRNA gene sequences of the two enrichment cultures, the FS consortium was identified to contain 38.3% of Mycobacterium and 10.6% of Afipia, similar to previously reported literature. Meanwhile, 49.5% of the AS consortium belonged to the candidate division TM7, which has never been reported to be involved in 1,4-dioxane biodegradation. However, recent studies suggested that TM7 bacteria were associated with degradation of non-biodegradable and hazardous materials. Therefore, our results showed that previously unknown 1,4-dioxane-degrading bacteria might play an important role in enriched AS. Although the metabolic capability and ecophysiological significance of the predominant TM7 bacteria in AS enrichment culture remain unclear, our data reveal hidden characteristics of the TM7 phylum and provide a perspective for studying this previously uncultured phylotype.

증기발생기 2차측 제철화학세정액의 고온적용 (High Temperature Application of Iron Removal Chemical Cleaning Solvent in the Secondary Side of Nuclear Steam Generators)

  • 허도행;이은희;정한섭;김우철
    • Nuclear Engineering and Technology
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    • 제26권1호
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    • pp.140-148
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    • 1994
  • 원전 증기발생기 2차측 제철 화학세정을 기존의 93$^{\circ}C$ 표준공정보다 고온인 1$25^{\circ}C$에서 검증시험을 수행하였다. 원전 증기발생기를 1$25^{\circ}C$에서 화학 세정한다는 가정아래 현장세정 조건을 결정하고 이를 다시 모사하여 3l 용량의 소형 검증시험 조건을 결정하였다. 1 gallon 용량의 316 스텐레스강 압력용기를 반응용기로 사용하는 화학세정 시험장치에서 검증시험을 수행하여 스러지 용해거동, 모재 부식률, 세정제 화학조성 변화거동 등을 측정하였다. 1$25^{\circ}C$ 검증시험 결과에서 93$^{\circ}C$ 표준공정보다 세정시간을 절반이하로 단축시키고도 더 효율적인 세정효과를 얻을 수 있을 뿐만이 아니라 2차측 모재의 부식률도 감소함을 확인할 수 있었다. 그러나 고온 세정공정은 아직 현장적용 경험이 없고, 별도의 외부순환 세정 장치를 이용하는 93$^{\circ}C$ 표준공정과는 달리 주냉각재의 잠열로 2차측을 가열하므로 세정이 완료될 때까지 주냉각 펌프를 계속 가동하여야 하는 단점이 있다. 가동중인 증기발생기에 대한 화학세정을 수행할 때 93$^{\circ}C$ 표준공정과 고온공정의 장 단점을 신중히 검토하여 최적공정을 적용하여야 할 것이다.

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Beryllium Effects on the Microstructure and Mechanical Properties of A356 Aluminium Casting Alloy

  • Lee, Jeong-Keun;Kim, Myung-Ho;Choi, Sang-Ho
    • 한국주조공학회지
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    • 제18권5호
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    • pp.431-438
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    • 1998
  • Microstructure of A356 aluminum alloys cast in the permanent mold was investigated by optical microscope and image analyzer, with particular respect to the shape and size distribution of iron intermetallics known as ${\beta}-phase$ ($Al_5FeSi$). Morphologies of the ${\beta}-phase$ was found to change gradually with the Be:Fe ratio like these. In Be-free alloys, ${\beta}-phase$ with needlelike morphology was well developed, but script phase was appeared when the Be:Fe ratio is above 0.2:1. With the Be:Fe ratios of 0.4:1-1:1, script phase as well as Be-rich phase was also observed. In case of higher Be addition, above 1:1, Be-rich phase was observed on all regions of the specimens, and increasing of the Be:Fe ratios gradually make the Be-rich phase coarse. It was also observed that the ${\beta}-phase$ with needlelike morphology was coarsened with increase of the Fe content in Be-free alloys. However, in Be-added alloys, length and number of these ${\beta}-phases$ were considerably decreased with the increased Be:Fe ratio. Beryllium addition improved tensile properties and impact toughness of the A356 aluminium alloy, due to the formation of a script phase or a Be-rich phase instead of a needlelike ${\beta}-phase$. The DSC tests indicated that the presence of Be could increase the amount of Mg which is available for $Mg_2Si$ precipitate hardening, and enhance the precipitation kinetics by lowering the ternary eutectic temperature.

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Fe-2.3%Cr-1.6%W 합금의 고온산화 부식속도와 스케일 분석 (High-temperature Oxidation Kinetics and Scales Formed on Fe-2.3%Cr-1.6%W Alloy)

  • 박상환;김민정;이재호;봉성준;김슬기;이동복
    • 한국세라믹학회지
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    • 제48권1호
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    • pp.57-62
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    • 2011
  • The T23 steel, whose composition was Fe-2.3%Cr-1.6%W, was arc-melted, and oxidized between $600^{\circ}C$ and $900^{\circ}C$ in air for up to 7 months. The amount of precipitates in the arc-melted microstructure was as large as 11.4 vol.%. The precipitates increased the oxidation rate of the arc-melted T23 steel. Owing to the low amount of Cr in the T23 steel, breakaway oxidation occurred after a few hours during oxidation above $700^{\circ}C$ in both arc-melted and as-received T23 steels. The scales that formed on arc-melted and as-received T23 steels were similar to each other. They consisted primarily of the outer $Fe_2O_3$ layer and the inner ($Fe_2O_3$, $FeCr_2O_4$)-mixed layer. The precipitates increased the microhardness and the oxidation rates.

Cu-ferrite에 의한 메탄의 부분산화 (Methane Partial Oxidation Using Cu-ferrite)

  • 우성웅;강경수;김창희;박주식
    • 한국수소및신에너지학회논문집
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    • 제18권2호
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    • pp.124-131
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    • 2007
  • Methane is partially oxidized to produce the syngas by the lattice oxygen of metal oxides in the absence of gaseous oxygen. The present work deals with ferrite including copper component, which does not chemisorb methane, to investigate the suppression of the carbon deposition during the reduction of metal oxides by methane. Iron-based oxides of $Cu_xFe_{3-x}O_4$(X=0.25, 0.5, 1.0) was synthesized by the co-precipitation method. Thermogravimetric Analysis(TGA) was used to observe the isothermal reduction behavior of $Cu_xFe_{3-x}O_4$ and $Fe_3O_4$ at $600-900^{\circ}C$ under methane atmosphere. The crystal structures of reduced specimens were characterized by X-rays powder diffraction(XRD) technique. From the analyses of TGA, it is concluded that the reduction kinetics of $CuFe_2O_4$ was the fastest among $Fe_3O_4$ and $Cu_xFe_{3-x}O_4$(X=0.25, 0.5, 1.0). The X-ray diffraction analyses indicated that $Cu_xFe_{3-x}O_4$ was decomposed to Cu and $Fe_3O_4$ phase at $600^{\circ}C$ and was reduced to Cu and Fe phase at $800^{\circ}C$. $Fe_3O_4$, which was reduced at $900^{\circ}C$, showed Fe, graphite and $Fe_3C$ phases. On the contrary, $Cu_xFe_{3-x}O_4$ does not show the graphite or $Fe_3C$ phases. This results infer that Cu component suppress the carbon deposition on Cu-ferrite.