• 자원리싸이클링
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• 제20권4호
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• pp.71-77
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• 2011

$MoO_3$ 분말을 723 K ~ 873 K에서 Ar+$H_2$ 혼합기체를 이용히여 수평관상로에서 $MoO_2$로 훤원하였으며, 반용속도를 배가스 중의 상대습도를 측정하여 계산하였다. 반응속도는 수소가스 분압과 반응속도에 따라 현저하게 증가하였다. 환원 반응초기에 $H_2O$의 발생속도가 급격하게 증가하였으며, 시간의 경과에 따라 배가스 중의 $H_2O$ 분압은 급격하게 감소하였다. 이 시기에 환원 반응율은 직선적으로 증가하였다. 환원반응 초기의 $MoO_3$에서 $MoO_2$로의 환원반응의 활성화 에너지는 73.56 kJ/mol로 계산되었다.

• 상하수도학회지
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• 제23권5호
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• pp.669-678
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• 2009

The reduction of excess activated sludge from petrochemical plant was investigated by the electro fenton (E-Fenton) process using electrogenerated hydroxyl radicals which lead to mineralization of activated sludge to $CO_2$, water and inorganic ions. Factors affecting the disintegration efficiency of excess activated sludge in E-Fenton process were examined in terms of five criteria: pH, $H_2O_2/Fe^{2+}$ molar ratio, current density, initial MLSS (mixed liquid suspended solids) concentration, $H_2O_2$ feeding mode. TSS total suspended solid and $TCOD_{cr}$ reduction rate increased with the increasing $H_2O_2/Fe^{2+}$ molar ratio and current density until 42 and $6.7 mA/cm^2$, respectively but further increase of $H_2O_2/Fe^{2+}$ molar ratio and current density would reduce the reduction rate. On the other hand, as expected, increasing pH and initial MLSS concentration of activated sludge decreas TSS and $TCOD_{cr}$ reduction rate. The E-Fenton process was gradually increased during first 30 minutes and then linearly proceed till 120 minutes. The optimal E-Fenton condition showed TSS reduction rate of 62~63% and $TCOD_{cr}$ (total chemical oxygen demand) reduction rate of 55~56%. Molar ratio $H_2O_2/Fe^{2+} = 42$ was determined as optimal E-Fenton condition with initial $Fe^{2+}$ dose of 5.4 mM and current density of $6.7{\sim}13.3 mA/cm^2$, initial MLSS of 7,600 mg/L and pH 2 were chosen as the most efficient E-Fenton condition.

• Bulletin of the Korean Chemical Society
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• 제19권4호
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• pp.417-422
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• 1998

The electrocatalytic reduction of molecular oxygen was investigated with a Co(II)-glyoxal bis(2-hydroxyanil) complex coated-glassy carbon (GC) electrode in aqueous media. The reduction of $O_2$ at the modified electrode was an irreversible and diffusion-controlled reaction. The complex coated-GC electrode demonstrated an excellent electrocatalytic effect for $O_2$ reduction in an acetate buffer solution of pH 3.2. The coated electrode made the $O_2$ reduction potential shift of 60-510 mV in a positive direction compared to the bare GC electrode depending on pH. The Co(II)-glyoxal bis(2-hydroxyanil) coated electrode converted about 51% of the $O_2$ to $H_2O_2$ via a two-electron reduction pathway, with the balance converted to H_2O$.

• 한국재료학회지
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• 제23권11호
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• pp.631-637
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• 2013

Synthesis of sub-micron $2SnO{\cdot}(H_2O)$ powders by chemical reduction process was performed at room temperature as function of viscosity of methanol solution and molecular weight of PVP (polyvinylpyrrolidone). Tin(II) 2-ethylhexanoate and sodium borohydride were used as the tin precursor and the reducing agent, respectively. Simultaneous calcination and sintering processes were additionally performed by heating the $2SnO{\cdot}(H_2O)$ powders. In the synthesis of the $2SnO{\cdot}(H_2O)$ powders, it was possible to control the powder size using different combinations of the methanol solution viscosity and the PVP molecular weight. The molecular weight of PVP particularly influenced the size of the synthesized $2SnO{\cdot}(H_2O)$ powders. A holding time of 1 hr in air at $500^{\circ}C$ sufficiently transformed the $2SnO{\cdot}(H_2O)$ into $SnO_2$ phase; however, most of the PVP (molecular weight: 1,300,000) surface-capped powders decomposed and was removed after heating for 1 h at $700^{\circ}C$. Hence, heating for 1 h at $500^{\circ}C$ made a porous $SnO_2$ film containing residual PVP, whereas dense $SnO_2$ films with no significant amount of PVP formed after heating for 1 h at $700^{\circ}C$.

• 한국환경과학회지
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• 제22권1호
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• pp.73-81
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• 2013

The present work has been devoted to the catalytic reduction of $N_2O$ by $H_2$ with $Pt/SiO_2$ catalysts at very low temperatures, such as $110^{\circ}C$, and their nanoparticle sizes have been determined by using $H_2-N_2O$ titration, X-ray diffraction(XRD) and high-resolution transmission electron microscopy(HRTEM) measurements. A sample of 1.72% $Pt/SiO_2$, which had been prepared by an ion exchange method, consisted of almost atomic levels of Pt nanoparticles with 1.16 nm that are very consistent with the HRTEM measurements, while a $Pt/SiO_2$ catalyst possessing the same Pt amount via an incipient wetness technique did 13.5 nm particles as determined by the XRD measurements. These two catalysts showed a noticeable difference in the on-stream $deN_2O$ activity maintenance profiles at $110^{\circ}C$. This discrepancy was associated with the nanoparticle sizes, i.e., the $Pt/SiO_2$ catalyst with the smaller particle size was much more active for the $N_2O$ reduction. When repeated measurements of the $N_2O$ reduction with the 1.16 nm Pt catalyst at $110^{\circ}C$ were allowed, the catalyst deactivation occurred, depending somewhat on regeneration excursions.

• 한국환경보건학회지
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• 제19권3호
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• pp.29-35
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• 1993

This study was performed to obtain optimal conditions for reduction of color in dye wastewaters using coagulation-sedimentation processes with redox reactions. The reduction of color as well as organic matters variation was observed after coagulation-sedimentation processes using FeSO$_4$ $\cdot$ 7H$_2$O and NaOCl. Coagulation-redox reaction was done with the dose of Coagulant and oxidant at various pH values. Redox reaction was done through jar-mixing and aeration. The results of study were as follows: 1. In the coagulation-sedimentation processes using FeSO$_4$ $\cdot$ 7H$_2$O, color reduction was heigher at pH 3. With variance of dosage of FeSO$_4$ $\cdot$ 7H$_2$O, color reduction was higher at 250 mg/l. When coagulation-sedimentation using FeSO$_4$ $\cdot$ 7H$_2$O 250 mg/l was added at pH 3, the reduction of color, COD$_{Mn}$, and COD$_{Cr}$ showed 47.6%, 21.3% and 22.1%, respectively. 2. When NaOCI was added at level of 100 ppm in raw wastewater at pH 3, the reduction of color, COD$_{Mn}$, and COD$_{Cr}$ showed 30.2%, 5.5% and 6.2%, respectively. 3. After coagulation-sedimentation processes by addition of FeSO$_4$ $\cdot$ 7H$_2$O, when NaOCl was added at level of 250 mg/l in supernant, color reduction was 47.8% in aeration and 37.5% in jar-mixing. 4. Color reduction by aeration was higher than that by jar-mixing.

• 대한화학회지
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• 제9권2호
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• pp.71-74
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• 1965

Reduction of Ti(Ⅳ)-oxalate complex on dropping mercury electrode has been studied as a function of oxalate concentration and of pH varied with HCl. Assuming there are equilibrium $TiO(C_2O_4)_2= \;+\;2H^+\;=\;Ti^{+4}\;+\;2C_2O_4\;=\;+\;H_2O,\;K_4$ in addition to $TiO(C_2O_4)_2\;^=\;=\;TiO^{++}\;+\;2C_2O_4=\;K_2\;Ti(C_2O_4)_2\;^-\;=\;Ti^{+3}\;+\;2C_2O_4=\;K_3$ in the system cathodic wave has been well explained for that pH is higher than 0.5. The equilibrium constants $K_2,\;K_3$ and $K_4$ have been to be $2{\times}10^{-12},\;5{\times}10^{-13}$ and $10^{-11}$, respectively. The reduction of Ti(Ⅳ)-oxalate system is $Ti^{+4}\;+\;e\;{\to}\;Ti^{+3}$ in the concentration of hydrochloric acid, higher than 3M.

• 한국대기환경학회지
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• 제20권6호
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• pp.773-781
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• 2004

Ceramic foams prepared from silica -clay were coated with TiO$_2$ and V$_2$O$_{5}$ catalysts for selective catalytic reduction of NOx with NH$_3$. The effects of V$_2$O$_{5}$ loading, reaction temperature, space velocity, and oxygen content on NOx reduction with NH$_3$ were mainly investigated. Also, the NOx reduction characteristics of V$_2$O$_{5}$ and V$_2$O$_{5}$ -TiO$_2$ filters were compared when sulfur dioxide exists. From the results, the optimal NOx reduction with the maximum reduction efficiency of 91 % could be performed under the condition with V$_2$O$_{5}$ loading 6.0 wt. %, reaction temperature 35$0^{\circ}C$, space velocity 6,000h$^{-1}$ , and oxygen content 5%. And, the V$_2$O$_{5}$ -TiO$_2$ filters have shown higher NOx reduction efficiency and acid resistance against sulfur dioxide than the V$_2$O$_{5}$ filters.

• Korean Chemical Engineering Research
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• 제47권1호
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• pp.96-104
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• 2009

혼합금속산화물에 담지된 Pd-Rh 허니컴 촉매 상에서 NO와 $N_2O$를 동시에 저감하기 위한 반응 온도를 낮추면서 각각의 반응물에 대한 전환율을 높이기 위하여, 환원제로 수소 또는 일산화탄소 사용에 대해 조사하였다. 각각의 환원제 사용 시, NO와 $N_2O$의 전환율에 대한 반응 조건의 영향을 조사하기 위해 반응온도, 각 환원제와 산소의 농도, NO와 $N_2O$ 간의 농도 비율 등을 변화시켰다. 먼저 수소를 환원제로 사용하는 경우, 산소의 부재시 $200^{\circ}C$ 미만의 저온에서 50% 이상의 NO와 $N_2O$ 전환율을 얻을 수 있었다. 한편, 일산화탄소를 환원제로 사용하는 경우에는 NO와 $N_2O$ 전환율이 각각 $200^{\circ}C$와 $300^{\circ}C$ 이상에서 증가하기 시작하였다. 그러나, 두 가지 환원제 모두의 경우에서, 반응 가스내에 산소 농도가 증가함에 따라 $N_2O$와 NO 전환율에 감소하였다. 결과적으로 일산화탄소 환원제에 비해, 수소 환원제가 상대적으로 저온에서 NO와 $N_2O$를 동시에 저감할 수 있으며, 산소 농도에 의한 영향을 덜 받는 것으로 나타났다. 반면, 반응물내 $N_2O$와 NO 농도비에 의한 NO와 $N_2O$ 전환율의 영향은 환원제의 종류에 크게 영향을 받지 않는 것으로 관찰되었다. 저온에서 NO와 $N_2O$를 동시에 저감시키기 위해서는 산소 분위기보다는 수소 분위기에서 촉매를 전처리하는 것이 보다 효과적인 것으로 나타났다.

• 대한화학회지
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• 제18권2호
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• pp.110-116
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• 1974

백금전극을 사용해서 $CrO_4^=$이온의 환원을 중성인 비완충용액과 pH 8∼10 범위의 완충용액 및 강한 알카리성용액에서 조사하였다. pH 8∼10 범위의 완충용액에서 $CrO_4^=$이온의 환원에 관여한 전하이전의 수는 pH가 증가하므로써 점점 증가되었다. $CrO_4^=$이온dl 0.2N NaOH 용액에서 환원되어 질때 반응기구가 다음과 같이 가정되었다. $CrO_4^=+H_2O+2e{\rightarrow}CrO_3^=+2OH^-,\;CrO_3^=3H_2O+e{\rightarrow}Cr(OH)_3+3OH^-$ pH 13.5이고 지지전해질인 $(CH_3)_4NOH$ 용액에서 $CrO_4^=$ 이온이 환원되어 질때 두째번 파에서 심한 흡착을 보여주었다. 0.1N KCl의 비완충용액에서 linear sweep voltammogram은 initial voltage와 voltage sweep rate에 따라 세개 혹은 네개의 분명한 파로 나타나지만 첫째번 파는 확산에 의해서만 된 파라고 설명하기에는 어려움이 있었다.