• Korean Chemical Engineering Research
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• 제44권4호
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• pp.356-362
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• 2006

본 연구에서는 석탄가스화복합발전(integrated gas combined cycle, 이하 IGCC) 시스템의 석탄가스화기로부터 생산되는 석탄가스가 환원제로 이용되는 $SO_2$ 환원공정인 직접 황 회수 공정(direct sulfur recovery process, 이하 DSRP)에서 이용 가능한 Sn-Zr계 촉매 상에서의 $SO_2$ 환원반응특성을 조사하였다. Sn-Zr계 촉매는 0/1, 1/4, 1/1, 2/1, 3/1, 1/0의 Sn/Zr 몰비로 조절하여 침전법 및 공침법으로 제조되었다. 공간속도가 $10,000ml/g_{-cat.}{\cdot}h$, 반응물 몰비$([CO(or\;H_2)]/[SO_2])$가 2.0인 반응조건 하에서 Sn-Zr계 촉매를 이용하여 온도를 변화시킨 가운데 석탄가스에 포함되어 있는 $H_2$ 또는 CO를 환원제로 사용하여 $SO_2$ 환원에 대한 반응특성이 조사되었다. 실험 결과, 환원제의 종류에 상관없이 $SnO_2$와 $ZrO_2$보다 Sn-Zr계 촉매가 활성이 더 높았으며, 환원제의 종류에 대한 반응성 조사 결과, $H_2$보다 CO가 $SO_2$ 환원에 더 높은 반응성을 나타내었다. $H_2$가 환원제로 이용된 $SO_2$ 환원특성을 조사한 결과, Sn/Zr 비에 따라 제조된 Sn-Zr계 촉매의 종류에 상관없이 온도가 증가함에 따라 반응성이 증가하는 경향을 보이며 Sn/Zr 몰비가 1/4인 촉매를 사용한 경우 $550^{\circ}C$에서 $SO_2$전환율이 94.4％, 원소 황 수율이 66.4％로 높은 반응성을 나타내었다. 반면 CO를 환원제로 이용한 경우에는 Sn/Zr 몰비가 높은 촉매일수록 최적 반응온도가 감소되는 특이한 경향을 나타내었다. Sn-Zr계 촉매 중 Sn/Zr 몰비가 3/1인 $SnO_2-ZrO_2$ 촉매가 가장 낮은 최적 반응온도에서 높은 반응성을 나타내었는데, $325^{\circ}C$에서 $SO_2$전환율이 약 100％, 원소 황 수율이 약 99.5％로 가장 높은 반응성을 얻었다. 그리고 CO가 $H_2$보다 더 많이 포함되어 있는 석탄모사가스에 대하여 환원제로서의 이용가능성을 확인하고자 $CO/H_2$ 비를 달리한 각각의 합성가스에 대하여 $SO_2$ 환원반응실험을 수행하였다. Sn/Zr 몰비가 2/1인 Sn-Zr계 촉매 상에서 $SO_2$ 환원반응 실험 결과, CO 함량이 높은 합성가스일수록 효과적인 환원제임을 확인할 수 있었다. 따라서 Sn-Zr계 촉매가 적용된 DSRP에서 석탄모사가스가 환원제로 이용 가능하다는 것을 알 수 있었다.

• 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.

• 한국수소및신에너지학회논문집
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• 제26권6호
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• pp.600-608
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• 2015

As a candidate for cheap oxygen carrier, $CaSO_4$ based oxygen carriers have been developing. However, research on reaction characteristics and side reaction of $CaSO_4$ based oxygen carrier is very limited. There are many possible reactions for main components of syngas from coal. In this study, we prepared three $CaSO_4$ based oxygen carriers ($CaSO_4$-$Fe_2O_3$/bentonite, $CaSO_4$-$K_2CO_3$/bentonite, $CaSO_4$-CaO/bentonite) and performed reduction tests by hydrogen. Cyclic reduction-oxidation tests up to $5^{th}$ cycle are also conducted using hydrogen as fuel. Reduction reactivity of those $CaSO_4$ based oxygen carriers were compared with that of NiO based oxygen carrier (OCN703-1100). Real weight change fractions of $CaSO_4$ based oxygen carriers were higher than theoretical oxyen transfer capacity and reactivity of these particles decreased with the number of cycle increased. To check possible side reaction of $CaSO_4$ based oxygen carriers, $CaSO_4$ decomposition tests were carried out and $SO_2$ was detected even at $700^{\circ}C$. Consequently, we could conclude that $CaSO_4$ based oxygen carriers decompose and release $SO_2$ and this reaction lead reactivity decay of $CaSO_4$ based oxygen carries.

• Korean Chemical Engineering Research
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• 제48권3호
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• pp.316-321
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• 2010

본 연구에서는 고압조건에서 $SO_2$를 원소 황으로 전환하기 위한 촉매환원반응이 수행되었다. $SO_2$ 환원을 위한 촉매로 Sn-Zr계 금속복합산화물 촉매를 사용하였으며, 환원제로 CO가 사용되었다. 촉매환원반응성을 조사하기 위하여 반응온도, 반응물의 몰비([CO]/[$SO_2$]), 공간속도에 따른 $SO_2$ 전화율과 원소 황 수율 그리고 COS의 선택도를 상압조건과 20기압조건에서 비교되었다. 상압조건에서 $SO_2$ 전화율은 반응온도가 증가될수록 함께 증가되었으며, $CO/SO_2$ 몰비가 높을수록 증가되었다. 또한 $SO_2$ 전화율의 증가와 함께 COS의 선택도도 함께 증가되어, 원소 황 수율은 오히려 낮아졌다. 그러나 20 atm의 고압조건에서는 높은 $SO_2$ 전화율과 낮은 COS의 선택도가 얻어졌다. 이와 같은 결과는 높은 압력으로 인한 반응속도의 증가와 함께 생성된 원소 황이 응축되어 CO에 의한 COS 생성이 억제되었기 때문이라 판단된다. 이와 같은 결과로부터 $SO_2$ 촉매환원반응으로 높은 황 수율은 고압조건에서 더 유리하게 얻을 수 있다.

• 한국대기환경학회지
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• 제6권1호
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• pp.51-56
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• 1990

This Study shows the effect of the district heating on the $SO_2$ concentration reduction. In order to analyze the effect of the district heating, three alternatives were set up as follows; Alternative I represented present central heating system, and Alternative II and Alternative III represented district heating system of which the scale were different from. The concludions of this study are as follows; In case of the Alternative II and III, annual average $SO_2$ concentration are reduced by 9.0% and 14.6% respectively, and winter season $SO_2$ concentrations are reduced by 12.2% and 15.8% respectively, at the highest points. The average reduction rates of $SO_2$ concentration in the district heating area are about the same as the reduction rates at the highest points. Also, it was found that using the district heating system, the ground level $SO_2$ concentrations could be reduced within the area of 5 to 10 km radius.

• 한국대기환경학회지
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• 제7권3호
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• pp.219-226
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• 1991

Results from study on physiological responses to $SO_2$ of Quercus spp. selected for restoration of vegetation damaged by air pollution in the field study were as follows. Tolerance of Quercus aliena, Q. acutissima and Q. mongolica used in this study to $SO_2$ was higher in that order and tolerance of these plants to $SO_2$ was high comparatively among trees composing of major forest vegetation of Korea including natural forests and plantations. Stomatal resistance of these plants was increased after exposure to $SO_2$ and range of increase was different among species. From discrepancy between order of tolerance to $SO_2$ and range of increase in stomatal resistance, we were estimated that resistance mechanisms of Quercus spp. were different among species as mechanism originated in avoidance and resistance, respectively. Water potential of plant leaves reduced after exposure to $SO_2$, degree of reduction accorded with order of tolerance to $SO_2$. Reduction of water potential of plants after exposure to $SO_2$ was initiated before appearance of visible damage in plant leaves and water potential of plants exposed to $SO_2$ of low concentration, in which plants were not showed viaible damage was also reduced.

• 청정기술
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• 제20권3호
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• pp.212-217
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• 2014

재생공정에서 황화 된 탈황흡수제의 재생을 위하여 산소는 산화제로 사용되었다. 재생공정에서 미량의 미 반응 산소는 직접 황 회수 공정으로 유입된다. 그러나, $SO_2$ 환원을 위한 반응성은 미 반응 산소의 다양한 이유에 의해서 저하된다. $SO_2$ 환원을 위한 반응성 실험을 위해 Sn-Zr계 촉매가 사용되었으며, $SO_2$와 $O_2$는 각각 5.0 vol%와 4.0 vol%로 고정하였고 $300-450^{\circ}C$와 1-20 atm에서 수행되었다. 본 연구에서는 고온건식 탈황공정의 직접 황 회수공정에 유입되는 미 반응산소에 의한 촉매반응성 저하에 미치는 영향을 조사하였다. $SO_2$ 환원으로 생성된 원소 황은 미 반응산소에 의해서 재산화되고, redox반응기구에서 Sn-Zr계 촉매의 빈 격자 산소자리가 미 반응산소에 의해서 재산화되므로 $SO_2$ 전화율은 감소되는 것으로 판단된다. 한편 환원제로써 공급된 CO는 미 반응산소에 의해서 산화되어 연소열에 의해 촉매 충전 층 온도가 상승되기도 한다. 결과적으로 충전 층의 빠른 온도상승은 활성 물질을 소결시켜 촉매의 비활성화를 초래하게 된다.

• 한국분말재료학회지
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• 제18권3호
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• pp.244-249
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• 2011

Spherical nanosized cobalt powder with an average size of 150-400 nm was successfully prepared at room temperature from cobalt sulfate heptahydrate ($CoSO_4{\cdot}7H_2O$). Wet chemical reduction method was adopted to synthesize nano cobalt powder and hypophosphorous acid ($H_3PO_2$) was used as reduction agent. Both the HCP and the FCC Co phase were developed while $CoSO_4{\cdot}7H_2O$ concentration ranged from 0.7 M to 1.1 M. Secondary phase such as $Co(OH)_2$ and $CO_3O_4$ were also observed. Peaks for the crystalline Co phase having HCP and FCC structure crystallized as increasing the concentration of $H_3PO_2$, indicating that the amount of reduction agent was enough to reduce $Co(OH)_2$. Consequently, a homogeneous Co phase could be developed without second phase when the $H_3PO_2/CoSO_4{\cdot}7H_2O$ ratio exceeded 7.

• 한국재료학회지
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• 제13권8호
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• pp.524-530
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• 2003

In order to prepare the uniform copper particles from copper sulfate solution by using hydrazine as a reduction agents, the reduction behavior of copper particles from copper sulfate was investigated in detail at room temperature by the observation of reaction products. The effects of $NH_4$OH and $Na_4$$P_2$$O_{7}$ on the formation of uniform copper particles were discussed. ($NHCu_3$)$_4$$SO_4$was completely formed at over pH 11 by adding $NH_4$OH in copper sulfate solution. The fine $Cu_2$O with the particle size of 50 nm was produced in the initial reduction process of (NH$Cu_3$)$_4$$SO_4$solution with $Na_4$$P_2$$O_{ 7}$ and then the Cu$_2$O was converted into copper particles by inserting additional hydrazine. When Cu(NH$_3$)$_4$SO$_4$solution with $Na_4$$P_2$$O_{ 7}$ was reduced at $80^{\circ}C$ by hydrazine, the highly dispersed copper particles with the particle size of about 0.8 $\mu\textrm{m}$ was obtained.

• 한국분말재료학회지
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• 제31권2호
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• pp.163-168
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• 2024

As the demand for lithium-ion batteries for electric vehicles is increasing, it is important to recover valuable metals from waste lithium-ion batteries. In this study, the effects of gas flow rate and hydrogen partial pressure on hydrogen reduction of NCM-based lithium-ion battery cathode materials were investigated. As the gas flow rate and hydrogen partial pressure increased, the weight loss rate increased significantly from the beginning of the reaction due to the reduction of NiO and CoO by hydrogen. At 700 ℃ and hydrogen partial pressure above 0.5 atm, Ni and Li₂O were produced by hydrogen reduction. From the reduction product and Li recovery rate, the hydrogen reduction of NCM-based cathode materials was significantly affected by hydrogen partial pressure. The Li compounds recovered from the solution after water leaching of the reduction products were LiOH, LiOH·H₂O, and Li₂CO₃, with about 0.02 wt% Al as an impurity.