• 공업화학
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• 제23권2호
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• pp.190-194
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• 2012

다양한 상용 $TiO_2$ 담체를 이용한 10 wt%의 Mn계 촉매를 습윤함침법으로 제조하여 $NH_3$에 의한 NO의 저온 선택적 촉매환원법(SCR) 반응 특성을 연구하였다. 촉매의 특성은 BET, XRD, XPS 그리고 TPR과 같은 물리화학적 분석을 통해 수행되었다. MnOx/$TiO_2$ 촉매의 MnOx 표면밀도는 비표면적에 영향을 받는다. 고분산된 망간산화물에 의한 낮은 MnOx surface density로 저온 SCR 활성이 증가하고 망간산화물의 $MnO_2$에서 $Mn_2O_3$로 환원되는 온도가 감소되었다. 우수한 SCR활성을 위해서는 망간산화물을 높은 비표면적을 가진 $TiO_2$에 담지되어야 하고 고분산된 비정질종이 존재해야 한다.

• 한국건설순환자원학회논문집
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• 제3권4호
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• pp.366-373
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• 2015

재건축 재개발 사업 등으로 인하여 증가하는 건설폐기물을 효율적이고 친환경적으로 처리하기 위하여 건설폐기물을 재활용하여 사용하고 있다. 대표적으로 순환골재가 있으며, 이는 수산화칼슘에 의하여 높은 강알칼리성을 나타내며 많은 환경문제를 발생시키고 있다. 따라서 본 연구는 순환골재의 pH를 저감하기 위해 인산나트륨계암모늄염을 사용하여 순환골재의 강알칼리성을 감소시키기 위한 연구이다. 또한, 순환골재 pH 저감제의 현장적용 가능성을 평가하였다. 그 결과 pH 저감제 비율이 증가할수록 pH가 감소하는 것을 확인할 수 있었으며 순환골재 생산과정 중 pH 저감제를 이용한 침지, 분사 등의 방법으로 현장적용이 가능할 것으로 판단된다.

• 한국광물학회지
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• 제27권4호
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• pp.311-320
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• 2014

슬래그를 매립한 토양을 대상으로 자기분리연구를 수행하였다. 토양세척을 거친 토양과 토양세척 전 토양을 대상으로 습식자기분리와 건식자기분리를 수행하여 분리된 부분과 분리되지 않은 부분의 중금속 농도를 측정하여 중금속의 농축효과를 측정하였다. 습식자기분리의 경우 토양세척 전 시료의 자력분리율이 상대적으로 높으며 토양세척 후 시료의 경우 약 40% 정도가 자기분리 되었다. 토양 : 물의 비가 농축효과에는 큰 영향을 미치지 못하며, Fe, Pb, Cu, Zn, Cd의 세척 전 토양과 세척 후 토양의 자기분리에 의한 평균 농축비는 3.2, 2.1, 12.1, 2.5, 1.5와 17.4, 7.0, 15.7, 9.6, 7.0으로 토양 세척을 거친 경우 자기분리에 의해 토양 세척 전 토양에 비해 더 큰 토양 부피 감량효과를 기대할 수 있다. 건식자기분리의 경우에도 자기분리에 의해 중금속의 농축효과를 얻을 수 있으나 자기분리에 의한 회수율이 너무 높은 경우 오염토 저감을 기대하기 어렵다. 철과 같은 강자성체를 포함하는 토양의 경우 자기분리에 의해 토양세척의 효과와 유사하게 오염토양의 양을 줄일 수 있고, 오염이 한쪽에 농축되는 결과를 얻을 수 있다.

• 마이크로전자및패키징학회지
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• 제23권3호
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• pp.51-56
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• 2016

내산화 특성을 가지는 구리(Cu) 기반의 미세 도전 필러를 제조하기 위하여 서브마이크론급의 은(Ag) 코팅 Cu 입자를 제조하고, 그 내산화 특성을 평가하였다. 평균 크기 $0.705{\mu}m$의 Cu 입자들을 습식 합성법으로 제작한 후, 에틸렌글리콜 용매를 사용한 연속 공정으로 Ag 도금을 실시하여 Ag 도금 Cu 입자를 제조하였다. Ag 도금 공정에서 제어한 주요 변수는 환원제 아스코빅산의 첨가 농도, Ag 전구체 용액의 주입속도 및 혼합 용액의 교반속도였는데, 이들의 변화에 따른 Ag 도금의 특성과 미세한 순수 은Ag 입자의 생성 변화를 관찰하였다. 그 결과 공정변수들을 최적화시킴으로써 불필요한 순수 Ag 입자들이 생성을 막고, Ag 도금 Cu 입자들간의 응집을 억제할 수 있었다. 최적 제조조건에서 제조된 Ag 도금 Cu 입자들은 다소간의 응집을 나타내었으나, 대기중에서 $10^{\circ}C/min$의 승온속도로 가열 시 약 $225^{\circ}C$에서야 0.1%의 무게 증가를 나타내었고, $150^{\circ}C$의 대기중에서는 75 분까지 무게 증가가 없는 우수한 내산화 특성을 나타내었다.

• 한국재료학회지
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• 제22권5호
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• pp.253-258
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• 2012

Activated magnetite ($Fe_3O_{4-{\delta}}$) was applied to reducing $CO_2$ gas emissions to avoid greenhouse effects. Wet and dry methods were developed as a $CO_2$ removal process. One of the typical dry methods is $CO_2$ decomposition using activated magnetite ($Fe_3O_{4-{\delta}}$). Generally, $Fe_3O_{4-{\delta}}$ is manufactured by reduction of $Fe_3O_4$ by $H_2$ gas. This process has an explosion risk. Therefore, a non-explosive process to make $Fe_3O_{4-{\delta}}$ was studied using $FeC_2O_4{\cdot}2H_2O$ and $N_2$. $FeSO_4{\cdot}7H_2O$ and $(NH_4)_2C_2O_4{\cdot}H_2O$ were used as starting materials. So, ${\alpha}-FeC_2O_4{\cdot}2H_2O$ was synthesized by precipitation method. During the calcination process, $FeC_2O_4{\cdot}2H_2O$ was decomposed to $Fe_3O_4$, CO, and $CO_2$. The specific surface area of the activated magnetite varied with the calcination temperature from 15.43 $m^2/g$ to 9.32 $m^2/g$. The densities of $FeC_2O_4{\cdot}2H_2O$ and $Fe_3O_4$ were 2.28 g/$cm^3$ and 5.2 g/$cm^3$, respectively. Also, the $Fe_3O_4$ was reduced to $Fe_3O_{4-{\delta}}$ by CO. From the TGA results in air of the specimen that was calcined at $450^{\circ}C$ for three hours in $N_2$ atmosphere, the ${\delta}$-value of $Fe_3O_{4-{\delta}}$ was estimated. The ${\delta}$-value of $Fe_3O_{4-{\delta}}$ was 0.3170 when the sample was heat treated at $400^{\circ}C$ for 3 hours and 0.6583 when the sample was heat treated at $450^{\circ}C$ for 3 hours. $Fe_3O_{4-{\delta}}$ was oxidized to $Fe_3O_4$ when $Fe_3O_{4-{\delta}}$ was reacted with $CO_2$ because $CO_2$ is decomposed to C and $O_2$.

• 한국의류학회지
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• 제30권2호
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• pp.255-265
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• 2006

The purpose of this study was to examine the dyeing properties of four kinds of composite yams that were twisted in different processes. The composite yarns consist of acetate and functional polyester in ratio of 70 : 30. The composite yams were dyed at 100$^{circ}C$ and 125$^{circ}C$ using three types of dyes, disperse dyes for acetate fiber, PET fiber and PET-acetate blended fiber, in the three primary colors. The exhaustion($\%$) and K/S value were observed for each case. Also the effects of four different twisting processes to dyeing properties and physical properties were examined. Regardless of twisting methods, the composite yarns that were dyed at 125$^{circ}C$ had higher exhaustion($\%$) than those were dyed at 100$^{circ}C$ with all three types of dyes; However, tendency of the K/S value after reduction cleaning process was measured at 100$^{circ}C$ and the value measured 125$^{circ}C$ had a great difference with disperse dyes for acetate and dyes for PET. The difference of the K/S values of composite yarns, when dyed at 100$^{circ}C$ and 125$^{circ}C$ with disperse dyes for PET-acetate blended fiber, was almost negligible. According to twisting methods K/S values were in the following order: AP1 > AP3 > AP4> AP2. This means that AP1, treated at 220$^{circ}C$, had the highest K/S value and K/S value becomes higher as the yam is higher twisted and becomes lower as lower twisted. On the other hand, the dry shrinkage and wet shrinkage showed low shrinkage rate when the twist was high and steam setting temperature was high.

• 패션비즈니스
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• 제12권6호
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• pp.46-60
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• 2008

Lyocell is a regenerated cellulosic fiber manufactured by an environmentally friendly process. The major advantages of lyocell are the excellent drape forming property, the genuine bulkiness, smooth surface, and high dry/wet tenacities. However, one drawback of lyocell is its fibrillation property, which would degrade its aesthetic quality and lower the consumer satisfaction. In our previous studies, lyocell was treated with epichlorohydrin, a non-formalin based crosslinker, to reduce its fibrillation tendency. To investigate the changes of physical properties upon ECH-treatment, the hand characteristics of ECH-treated fabric were observed using KES-FB system and the 3D-virtual sewing image of the fabrics were obtained using 3D CAD simulation system in this study. Since epichlorohydrin(ECH) treatment was conducted in the alkaline medium, the weight reduction was observed in all treated lyocell. The treated lyocell became light, smooth and flexible in spite of ECH crosslinker application. LT and RT in tensile property upon the ECH treatment did not change significantly, however, EMT and WT in the tensile property increased. The significant decrease in bending rigidity was resulted in all ECH-treated lyocell, which is the result of the weight loss upon the alkali condition of ECH treatment. The bending rigidity increased again in the ECH 30% treated lyocell, however, the B value is still lower than the original. Therefore, the ECH-treated lyocell would be more stretchable and softer than the original. Shear rigidity was also decreased in all ECH-treated lyocell, which would result in more drape and body fitting when it is made as a garment. The ECH-treated fabric showed the softer smoother surface according to SMD value from KES evaluation. The virtual 3D sewing image of the ECH-treated lyocell did not show a significant change from that of the original except ECH 30% treated lyocell. ECH 30% treated lyocell showed a stiffer and more puckered image than the original.

• 환경영향평가
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• 제9권3호
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• pp.163-176
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• 2000

The purpose of this study is to analyze the pollutant loads and its distribution, and to suggest the management of nonpoint sources in Daechong Reservoir. The loads from point and nonpoint sources such as population, industry, livestock and land use were calculated per stream or river with topography(1:25,000) of the watershed of Daechong Reservoir. The generating pollutant loads were obtained through multiplication of pollutant sources by generating pollutant quantity per unit pollutant source. The effluent point sources loads is defined as loads from wastewater treatment facilities such as domestic, industrial and livestock wastewater treatment facilities, which were calculated through multiplication of effluent flowrates by water quality constituents concentration. Untreated point sources loads were estimated to be 35 % of total point sources loads. The effluent nonpoint sources pollutant loads were obtained through the multiplication of generating nonpoint sources loads by effluent ratios based on previous studies. The effluent nonpoint sources loads have the ratio of 26.2% of total BOD effluent loadings, 20.1% of total T-N effluent loadings, and 10.5% of total T-P effluent loadings. For the reduction of nonpoint sources loads in Daechong Reservoir, silviculture, artificial wet land, and grassed waterways could be applied. And untreated livestock waste scattered can result in nonpoint loadings, so required the livestock wastes treatment facilities and purifying facilities together with the management of shed, pasture, livestock waste storage site and composting site. Finally, remote sensing and GIS should be applied to the identification of distribution of water quality, watershed, the location and scale of nonpoint sources, effluent process during rainfall, for more detailed analysis of nonpoint sources.

• Nuclear Engineering and Technology
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• 제33권4호
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• pp.355-364
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• 2001

In order to evaluate and finally optimize the vitrification condition for combustible dry active waste (DAW), dust and gas generation characteristics were investigated for PE, cellulose, and mixed waste Tests were conducted by varying the operation variables such as melter configuration, excess oxygen amount, and waste feeding rate. Results showed that dust generation characteristics were affected by the operation parameters and the melter＇s configuration is the dominant one. For all tested DAWs, dust generation was reduced by increasing the waste feeding rate and the excessive oxygen amount in the melter. Among waste types, dust amount was decreased by the order of mixed wastes, PE, and cellulose. Other parameters such as temperature variation and operation time have also affected the dust generation. The optimum condition for the DAW vitrification was determined as the melter＇s configuration equipped for minimizing the waste dispersion with 20 kg/h of waste feeding rate and 100% of excessive oxygen supply. CO gas concentration in the off-gas was immediately influenced by the combustion state in the melter, but showed similar trend as the dust generation. For the NOx production during the vitrification process, thermal NOx, which is generated from the Post Combustion Chamber (PCC), rather than fuel NOx was assumed to be dominant. The gas cleaning of efficiencies of the PCC, wet scrubber, and Selective Catalytic Reduction system (SCR) were found to be high enough to keep the concentration of pollutants (CO, NOx, SOx, HCI) in the stack below their relevant emission limits.

• 한국수소및신에너지학회논문집
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• 제27권2호
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• pp.192-200
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• 2016

A characteristics of microwave drying-gasification was analyzed for converting a dewatered sewage sludge generated a wastewater treatment plant. Gas (60%) was the largest component of the product of microwave gasification, followed by sludge char (33%) and tar (2%). The main components of the producer gas were hydrogen (33%) and carbon monoxide (40%), and there was some methane and hydrocarbons ($C_2H_4$, $C_2H_6$, $C_3H_8$). Larger nitrogen and smaller oxygen amounts were generated. Gravimetric tar generated $414g/m^3$. This means a total tar which is a heavy hydrocarbons from the volatile organic substance in the sewage sludge. Selected light tars were benzene, anthracene, naphthalene, pyrene, showing lower concentrations as 2.62, 0.37, 0.49, $0.28g/m^3$, respectively. Sludge char has larger meso pores which is a mean pore size of $50.85{\AA}$ and has high adsorptivity. An amount of adsorption was $228.71cm^3/g$, showing higher quantity than acommercial adsorbers. This indicates that the gas obtained from the microwave gasification of wet sewage sludge can be used as fuel, but the heavy tar in the gas must be treated. Sludge char can be used as a tar reduction adsorbent in the process, and then burns as a solid fuel.