• Journal of the Korean Chemical Society
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• v.51 no.1
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• pp.14-20
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• 2007

The anodic dissolution of electrodeposited iron group elements (Fe, Co, Ni) were studied in phthalate buffer solution. The pH dependence of the corrosion potential, the corrosion current and Tafel slope was measured for each element. Based on the electrochemical parameters including Tafel slopes, we proposed the redox mechanism of the corrosion and the passivation. The adsorption of various phthalate species on the electrodeposited iron group elements seemed to be affected the corrosion mechanisms.

• Journal of the Korean Chemical Society
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• v.33 no.6
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• pp.577-581
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• 1989

Activated Cu-Zn by the reaction of aqueous cupric sulfate and excess Zn showed the exceptional catalytic activity for the reduction of aromatic nitro compounds to the corresponding amino compounds in the presence of hydrazine monohydrate in ethanol. But, aliphatic nitro compounds were not reduced to the amino compounds.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2015.05a
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• pp.157-158
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• 2015

$Ni-TiO_2$ 복합체를 전기도금법으로 제조할 때, pH, 전류밀도 변화에 따른 $TiO_2$ 부피분율을 측정하였다. 산화물의 부피분율은 pH가 높아질수록 낮아지고, 전류밀도가 증가하면, $100mA/cm^2$에서 최댓값을 가진 뒤에 감소하였다. 기존의 산화물 공석량 예측식 모델에 수소발생반응을 고려하여 적용한 결과, 기존 모델보다 실험값과 예측값의 정확도가 더 높았다. 따라서, 산화물이 전기도금층에 공석될 때에는 수소이온의 환원반응과 니켈이온의 환원반응을 종합적으로 고려하여야 한다.

• Journal of Korean Society of Environmental Engineers
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• v.31 no.10
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• pp.839-844
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• 2009

This research investigates the importance of the microbial metabolic pathways such as denitrification, iron reduction, and methanogenesis, in the degradation of organic matters of the sediments. There are statistically significant differences( P < 0.05) in the rates of denitrification, iron reduction, and methanogenesis according to the location: Site A has no plant, Site B is dominated by Scirpus, and Site C is dominated by Phragmites. Among them, Site C showed different methanogenesis rate depending on the sediments depth. The organic matter content increased from Site A to Site C. Site A had the smallest organic matter content whereas it showed the largest denitrification rate and iron reduction rate. Site C had the largest methanogenesis rate. Denitrification is the dominant pathways based on the assumption that anaerobic degradation of organic matter is mainly carried out through denitrification, iron reduction, and methanogenesis.

• Korean Chemical Engineering Research
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• v.47 no.1
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• pp.96-104
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• 2009

In order to lower a reaction temperature with high conversions for simultaneous catalytic reduction of NO and $N_2O$ over Pd-Rh supported mixed metal oxide honeycomb catalysts, $H_2$ or CO was utilized as a reductant. When using the reductants, the effects of reaction conditions were examined in NO and $N_2O$ conversions, where reaction temperatures, concentrations of the reductants and oxygen and the concentration ratio of $N_2O$ to NO were varied. In using $H_2$ reductant, larger than 50% of NO and $N_2O$ conversions was observed at the temperatures below $200^{\circ}C$ in absence of $O_2$. In using CO reductant, NO and $N_2O$ conversions increased from the temperatures higher than $200^{\circ}C$ and $300^{\circ}C$, respectively. However, in use of both reductants, NO and $N_2O$ conversions decreased with increasing oxygen concentration. As a result, $H_2$ reductant could reduce simultaneously NO and $N_2O$ at relatively lower reaction temperature than CO. Also, NO and $N_2O$ conversions were less influenced by using $H_2$ reductant than CO one. Concentration ratio between NO and $N_2O$ did not affect their conversions regardless the type of reductants. Pretreatment of the catalyst in $H_2$ was more effective in simultaneous reduction of NO and $N_2O$ at low reaction temperature than that in $O_2$.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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• v.8 no.1
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• pp.19-32
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• 2010

Electrolytic reduction technology is essential for the purpose of adopting pyroprocessing into spent oxide fuel as an alternative option in a back-end fuel cycle. Spent fuel consists of various metal oxides, and each metal oxide releases an oxygen element depending on its chemical characteristic during the electrolytic reduction process. In the present work, an electrolytic reduction behavior was estimated for voloxidized spent fuel based on the assumption that each metal-oxygen system is independent and behaves as an ideal solid solution. The electrolytic reduction was considered as a combination of a Li recovery and chemical reactions between the metal oxides such as uranium oxide and the produced Li metal. The calculated result revealed that most of the metal oxides were reduced by the process. It was evaluated that a reduced fraction of lanthanide oxides increased with a decreasing $Li_2O$ concentration. However, most of the lanthanides were expected to be stable in their oxide forms. In addition, a semi-empirical model for describing $U_3O_8$ electrolytic reduction behavior was proposed by considering Li diffusion and a chemical reaction between $U_3O_8$ and Li. Experimental data was used to determine model parameters and, then, the model was applied to calculate the reduction yield with time and to estimate the required time for a 99.9% reduction.

• Journal of the Korean Chemical Society
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• v.26 no.5
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• pp.340-348
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• 1982

The presence of 10 mole percent triphenyl borate accelerated dramatically the rate of reduction of structurally different sulfoxides with borane in tetrahydrofuran at room temperature, compared to the slow reduction with borane itself. Tetramethylene sulfoxide underwent complete reduction in 5 min and diethyl sulfoxide, dibenzyl sulfoxide and benzylphenyl sulfoxide were reduced quantitatively within 1h, whereas the reduction of diphenyl sulfoxide was rather slow, giving diphenyl sulfide in 90% yield in 24h. Boron trifluoride etherate and triethyl borate were less effective than triphenyl borate. A possible mechanism is presented.

• Journal of the Korean Chemical Society
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• v.39 no.11
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• pp.842-847
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• 1995

The electrochemical reduction reactions of N '-aryl-N-alkyl-N-nitrosourea derivatives with a glassy carbon electrode were diffusion controlled and irreversible. The exchange kinetic constant ko values for reduction reaction of the N '-aryl-N-alkyl-N-nitrosoureas were at the range of $1.48{\times}10^{-6}{\sim}5.32{\times}10^{-7}\;cm/sec.$ The $k_0$ values for phenyl substituted on the aryl position were about 1.3∼2.8 times higher than that of other substituents. The same substituent for aryl groups on the both of N '-aryl-N-alkyl-N-nitrosourea and N '-aryl-N-(2-chloroethyl)-N-nitrosourea exhibited same value. The $E_p$ value was shifted to the negative direction as pH increased. The number of protons participated to the reduction was 4∼5, respectively. The substituent effect of aryl group on the reduction potential was not observed in this case.

• Resources Recycling
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• v.15 no.4 s.72
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• pp.44-51
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• 2006

Most electric arc furnace dust (EAFD) treatment processes to recover zinc from EAFD employ carbon as a reducing agent for the zinc oxide in the EAFD. In the present work, the reduction reaction of zinc oxide with carbon in the present of iron oxide was kinetically studied. The experiments were carried out at temperatures between 1173 K and 1373 K under nitrogen atmosphere using a weight-loss technique. From the experimental results, it was concluded that adding the proper amount of iron oxide to the reactant accelerates the reaction rate of zinc oxide with carbon. This is because iron oxide in the reduction reaction of zinc oxide with carbon promotes the carbon gasification reaction. The spherical shrinking core model for a surface chemical reaction control was found to be useful in describing kinetics of the reaction over the entire temperature range. The reaction has an activation energy of 53 kcal/mol (224 kJ/mol) for ZnO-C reaction system, an activation energy of 42 kcal/mol (175 kJ/mol) for $ZnO-Fe_{2}O_{3}-C$ reaction system, and an activation energy of 44 kcal/mol (184 kJ/mol) for ZnO-mill scale-C reaction system.

• Resources Recycling
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• v.13 no.5
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• pp.17-22
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• 2004

It has been carried our for establishing the methodology to upgrade $TiO_2$ by carbothermal reduction of iron oxide in ilmenite. Based on present experimental results, the possibility for substitution with rutile has been investigated. It could by proposed that the 2 wt.% $FeCl_3$ of sample and carbon of 2 equivalents are optimum conditions as a feeding materials. And also appropriate reducing temperature and reduction time were about $1100^{\circ}C$ and 30 minutes. The product obtained by the processes of carbon reduction and magnetic separation may be used the substitute mineral of rutile.