• 제목/요약/키워드: C1 reduction

검색결과 3,940건 처리시간 0.027초

Hydrogenotrophic Sulfate Reduction in a Gas-Lift Bioreactor Operated at $9^{\circ}C$

  • Nevatalo, Laura M.;Bijmans, Martijn F. M.;Lens, Piet N. L.;Kaksonen, Anna H.;Puhakka, Jaakko A.
    • Journal of Microbiology and Biotechnology
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    • 제20권3호
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    • pp.615-621
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    • 2010
  • The viability of low-temperature sulfate reduction with hydrogen as electron donor was studied with a bench-scale gas-lift bioreactor (GLB) operated at $9^{\circ}C$. Prior to the GLB experiment, the temperature range of sulfate reduction of the inoculum was assayed. The results of the temperature gradient assay indicated that the inoculum was a psychrotolerant mesophilic enrichment culture that had an optimal temperature for sulfate reduction of $31^{\circ}C$, and minimum and maximum temperatures of $7^{\circ}C$ and $41^{\circ}C$, respectively. In the GLB experiment at $9^{\circ}C$, a sulfate reduction rate of 500-600 mg $l^{-1}d^{-1}$, corresponding to a specific activity of 173 mg ${SO_4}^{2-}g\;VSS^{-1}d^{-1}$, was obtained. The electron flow from the consumed $H_2$-gas to sulfate reduction varied between 27% and 52%, whereas the electron flow to acetate production decreased steadily from 15% to 5%. No methane was produced. Acetate was produced from $CO_2$ and $H_2$ by homoacetogenic bacteria. Acetate supported the growth of some heterotrophic sulfate-reducing bacteria. The sulfate reduction rate in the GLB was limited by the slow biomass growth rate at $9^{\circ}C$ and low biomass retention in the reactor. Nevertheless, this study demonstrated the potential sulfate reduction rate of psychrotolerant sulfate-reducing mesophiles at suboptimal temperature.

마그네슘 열환원에 의한 저응집 초미립 TiCN 분말합성 (Synthesis of Ultrafine and Less Agglomerated TiCN Powders by Magnesiothermic Reduction)

  • 이동원
    • 한국분말재료학회지
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    • 제19권5호
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    • pp.356-361
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    • 2012
  • The ultra-fine and less agglomerated titanium carbonitride particles were successfully synthesized by magnesiothermic reduction with low feeding rate of $TiCl_4+1/4C_2Cl_4$ solution. The sub-stoichiometric titanium carbide ($TiC_{0.5{\sim}0.6}$) particles were produced by reduction of chlorine component by liquid magnesium at $800^{\circ}C$ of gaseous $TiCl_4+1/4C_2Cl_4$ and the heat treatments in vacuum were performed for 5 hours to remove the residual magnesium and magnesium chloride mixed with produced $TiC_{{\sim}0.5}$. The final $TiC_{{\sim}0.5}N_{0{\sim}0.5}$ particle with near 100 nm in mean size and high specific surface area of $65m^2/g$ was obtained by nitrification under nitrogen gas at $1,150^{\circ}C$ for 2 hrs.

Some articulatory reflexes observed in intervocalic consonantal sequences: Evidence from Korean place assimilation

  • Son, Minjung
    • 말소리와 음성과학
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    • 제12권2호
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    • pp.17-27
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    • 2020
  • This paper examines kinematic characteristics of /pk/ clusters, as compared to /kk/ and /pp/ with varying vowel contexts and speech rate. The results of EMMA data from eight Seoul-Korean speakers indicate as follows. Firstly, comparing /pk/ to /pp/ sequences, lips closing movement was faster and spatially greater in the /a/-to-/a/ context while temporally longer in the /i/-to-/i/ context. It was smaller in spatial displacement and shorter in temporal duration in /pk/ sequences. Peak velocity did not vary. Secondly, comparing /pk/ with /pp/ and /kk/ controls, lip aperture was less constricted in the /a/-to-/a/ context than /i/-to-/i/, but the maximum contact between the upper and lower lips was invariant across different vocalic contexts within /pk/ sequences (/apka/=/ipki/). Categorical reduction of C1 in /pk/ sequences fell in with the low-vowel and fast-rate conditions with across-/within-speaker variability. Gradient reduction of C1 was observed in all C1C2 types, being more frequent in fast rate. Lastly, the jaw articulator was a stable indicator of rate effects. The implication of the current study is that gestural reduction occurs with categorical reduction and general spatiotemporal weakening in the assimilating contexts, while quantitative properties of gestures may be a reason for gradient reduction, not necessarily confined to place assimilation.

산화·환원법에 의한 폐텅스텐 스크랩의 재활용에 관한 기초연구 (Basic Study on the Recycling of Waste Tungsten Scraps by the Oxidation and Reduction Process)

  • 김상욱;윤지석;김태욱;조봉휘;김인호;김상무;송창빈
    • 한국분말재료학회지
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    • 제24권1호
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    • pp.34-40
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    • 2017
  • This study is carried out to obtain basic data regarding oxidation and reduction reactions, originated on the recycling of waste tungsten hard scraps by oxidation and reduction processes. First, it is estimated that the theoretical Gibbs free energy for the formation reaction of $WO_2$ and $WO_3$ are calculated as ${\Delta}G_{1,000K}=-407.335kJ/mol$ and ${\Delta}G_{1,000K}=-585.679kJ/mol$, from the thermodynamics data reported by Ihsan Barin. In the experiments, the oxidation of pure tungsten rod by oxygen is carried out over a temperature range of $700-1,000^{\circ}C$ for 1 h, and it is possible to conclude that the oxidation reaction can be represented by a relatively linear relationship. Second, the reduction of $WO_2$ and $WO_3$ powder by hydrogen is also calculated from the same thermodynamics data, and it can be found that it was difficult for the reduction reaction to occur at $1,027^{\circ}C$, in the case of $WO_2$, but it can happen for temperatures higher than $1127^{\circ}C$. On the other hand, $WO_3$ reduction reaction occurs at the relatively low temperature of $827^{\circ}C$. Based on these results, the reduction experiments are carried out at a temperature range of $500-1,000^{\circ}C$ for 15 min to 4 h, in the case of $WO_3$ powder, and it is possible to conclude that the reduction at $900^{\circ}C$ for 2h is needed for a perfect reduction reaction.

Application of SNCR/SCR Combined process for effective operation of SCR Process

  • 최성우;최상기
    • 한국환경과학회지
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    • 제12권1호
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    • pp.47-54
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    • 2003
  • This paper have examined the optimum combination of SNCR and SCR by varying SNCR injection temperature and NSR ratio along with SCR space velocity. NOx reduction experiments using a SNCR/SCR combined process have been conducted in simple NO/NH$_3$/O$_2$ gas mixtures. Total gas flow rate was kept constant 4 liter/min throughout the SNCR and SCR reactors, where initial NOx concentration was 500 ppm in the presence of 5% O$_2$. Commercial catalyst, sulfated V$_2$O$\_$5/-WO$_3$/TiO$_2$, was used for SCR NOx reduction. The residence time and space velocity were around 1.67 sec, 2,400 h$\^$-1/ and 6,000 h$\^$-1/ in the SNCR and SCR reactors, respectively. SNCR NOx reduction effectively occurred in a temperature window of 900-950$^{\circ}C$. About 88% NOx reduction was achieved with an optimum temperature of 950$^{\circ}C$ and NSR=1.5. SCR NOx reduction using commercial V$_2$O$\_$5/-WO$_3$-SO$_4$/TiO$_2$ catalyst occurred in a temperature window of 200-450$^{\circ}C$ 80-98% NOxreduction was possible with SV=2400 h$\^$-1/ and a molar ratio of 1.0-2.0. A SNCR/SCR(SV=6000 h$\^$-1/) combined process has shown same NOx reduction compared with a stand-alone SCR(SV=2400 h$\^$-1/) unit process of 98% NOx reduction. The NH$_3$-based chemical could routinely achieve SNCR/SCR combined process total NOx reductions of 98% with less than 5 ppm NH$_3$ slip at NSR ranging from about 1.5 to 2.0, SNCR temperature of 900$^{\circ}C$-950$^{\circ}C$, and SCR space velocity of 6000 h$\^$-1/. Particularly, more than 98% NOx reduction was possible using the combined process under the conditions of T$\_$SNCR/=950$^{\circ}C$, T$\_$SCR/=350$^{\circ}C$, 5% O$_2$, SV=6000 h$\^$-1/ and NH$_3$/NOx=1.5. A catalyst volume was about three times reduced by SNCR/SCR combined process compared with SCR process under the same controlled conditions.

비이온 계면활성제의 마찰 및 열교환효율 저감 특성 연구 (Study on the Drag Reduction and Heat Transfer Efficiency Reduction of the Non-Ionic Surfactant)

  • 조성환;태춘섭
    • 설비공학논문집
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    • 제19권2호
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    • pp.133-141
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    • 2007
  • The drag reduction (DR) and heat transfer efficiency reduction (HTER) of nonionic surfactant according to the fluid velocity, temperature and surfactant concentration were investigated experimentally. For this study, several kinds of new surfactant which contains amine-oxide and betaine were developed. And experimental apparatus equipped with two water storage tanks temperature controlled, pumps, testing pipe network, two flowmeters, two pressure gauges, heat exchanger, and data logging system was built. Results showed that existing alkyl ammonium surfactant (CTAC) had DR of $0.6{\sim}0.8$ for $1,000{\sim}2,000\;ppm$ in fluid temperature of $50{\sim}60^{\circ}C$ and had very low DR in fluid temperature over $70^{\circ}C$. And new amino oxide and betaine surfactant (SAOB) had lower DR in fluid temperature of $50{\sim}60^{\circ}C$ compared with CTAC but in fluid temperature of $70{\sim}80^{\circ}C$ DR was $0.6{\sim}0.8$ for 1$1,000{\sim}2,000\;ppm$.

Mn조성비(組成比)가 PEMFC용(用) Pt/C 전극촉매(電極觸媒) 특성(特性)에 미치는 영향(影響)에 관(關)한 연구(硏究) (Effects of PtMn composition on carbon supported PtMn catalysts for PEMFC)

  • 유성열;강석민;이진아;이충균;유호진
    • 자원리싸이클링
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    • 제21권2호
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    • pp.34-40
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    • 2012
  • 기존 Pt/C 전극촉매 제조시 사용되는 Pt를 일정량의 Mn으로 대체하여 PtMn/C 전극촉매를 제조하였다. 환원제로 포름알데히드(HCHO)를 사용하여 화학환원법으로 $Pt_{10}$/C, $Pt_9Mn_1$/C, $Pt_7Mn_3$/C 촉매를 제조하였으며 반쪽 전지(half cell)에서 순환전압전류와 대시간 전류를 측정하였다. $Pt_9Mn_1$/C촉매가 $Pt_{10}$/C, $Pt_7Mn_3$/C촉매보다 높은 산소환원반응(oxygen reduction reaction)을 보였으며 0.9, 0.8, 0.7, 0.6V에서 각각 5분동안 측정한 대 시간 전류측정에서 $Pt_9Mn_1$/C가 $Pt_{10}$/C, $Pt_7Mn_3$/C촉매보다 높은 활성을 나타냈다. 물리적 특성은 XRD, TEM분석을 통하여 알아보았으며 입자의 평균 크기는 $Pt_9Mn_1$/C, $Pt_{10}$/C가 각각 2.7 nm, 3 nm를 나타냈다. XRD분석을 통하여 Pt의 FCC(Face Centered Cubic)결정 구조를 확인할 수 있었다.

W-CuO 혼합물을 이용하여 제조된 W-Cu나노복합분말의 미세구조와 소결거동에 관한 연구 (Microstructure and Sintering Behavior of W-15 wt%Cu Nanocomposite Powder Prepared from W-CuO Mixture)

  • 김길수;김대건;김영도
    • 한국분말재료학회지
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    • 제10권4호
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    • pp.270-274
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    • 2003
  • Recently, the fabrication process of W-Cu nanocomposite powders has been researched to improve the sinterability by mechanochemical process (MCP), which consists of ball milling and hydrogen-reduction with W- and Cu-oxide mixture. However, there are many control variables in this process because the W oxides are hydrogen-reduced via several reduction stages at high temperature over 80$0^{\circ}C$ with susceptive reduction conditions. In this experiment, the W-15 wt%Cu nanocomposite powder was fabricated with the ball-milling and hydrogen-reduction process using W and CuO powder. The microstructure of the fabricated W-Cu nanocomposite powder was homogeneously composed of the fine W particles embedded in the Cu matrix. In the sintering process, the solid state sintering was certainly observed around 85$0^{\circ}C$ at the heating rate of 1$0^{\circ}C$/min. It is considered that the solid state sintering at low temperature range should occur as a result of the sintering of Cu phase between aggregates. The specimen was fully densified over 98% for theoretical density at 120$0^{\circ}C$ for 1 h with the heating rate of 1$0^{\circ}C$/min.

망간황화물을 이용한 NO의 선택적 촉매 환원 (Selective Catalytic Reduction of NO on Manganese Sulfates)

  • 정순관;박태성;홍성창
    • Korean Chemical Engineering Research
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    • 제46권3호
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    • pp.473-478
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    • 2008
  • 망간황화물이 NO의 선택적 촉매 환원에 미치는 영향을 반응성 및 속도론적평가와 TPR(Temperature Programmed Reduction), TGA분석을 통하여 고찰하였다. 망간산화물은 $200^{\circ}C$ 이하의 저온에서 우수한 질소산화물 전환을 보였으나, 망간황화물의 경우 황화정도에 따라 질소산화물 전환은 고온으로 전이하였다. 또한 질소산화물 전환율도 황화정도에 따라 감소하였다. TPR 실험결과 망간산화물들은 $160^{\circ}C$ 이하의 낮은 온도에서 환원이 시작되었으나 망간황화물은 $280^{\circ}C$ 이상의 온도에서 환원이 시작되었다. TPR 실험을 통한 환원 시작온도는 촉매의SCR 시작 온도와 관련이 있는 것으로 판단된다. 망간황화물의 활성화에너지는 다른 촉매에 비해 낮게 나타났으나 pre-exponential 상수 크기가 다른 촉매에 비해 1/1000배 만큼 작아 NO에 대한 활성이 낮게 나타났다. 천연망간광석은 함유된 다양한 금속산화물의 영향으로 순수한 망간산화물보다 낮은 온도에서 재생되었다.

Electrocatalytic Reduction of Dioxygen at Glassy Carbon Electrodes with Irreversible Self-assembly of N-hexadecyl-N'-methyl Viologen

  • Lee, Chi-Woo;Jang, Jai-Man
    • Bulletin of the Korean Chemical Society
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    • 제15권7호
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    • pp.563-567
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    • 1994
  • The electroreduction of dioxygen at glassy carbon electrodes with irreversible self-assembly of N-hexadecyl-N'-methyl viologen $(C_{16}VC_1)$ proceeds at potentials more positive than those where the reduction occurs at bare electrodes. The electrocatalyzed reduction takes place at potentials well ahead of those where the catalyst is reduced in the absence of dioxygen and the limiting currents observed at rotating disk electrodes did not deviate from the thoretical Levich line up to 6400 rpm, indicating that the electrocatalysis is extremely rapid. The rate constant for the heterogeneous reaction between $C_{16}V^+C_1$ immobilized on the electrode surface and $O_2$ in solution was estimated to be ca. $10^8\;M^{-1}s^{-1}$. The half-wave potential of dioxygen reduction was independent of solution pH.