• Proceedings of the Korean Institute of Industrial Safety Conference
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• 2003.05a
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• pp.474-477
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• 2003

산성가스용 방독마스크 정화통은 활성탄에 정화제를 첨착시킨 첨착 활성탄을 사용하여 유해가스를 제거하여 왔으며, 일반적으로 알칼리제인 Ca(OH)$_2$를 첨착시켜 유독가스와 중화반응을 유도하여 왔다. 그러나 이들의 흡착제거 능력이 크지 않아 많은 양을 사용하여야 하는 문제점이 있었다. 따라서 정화통의 성능을 좌우하는 새로운 첨착물질을 선정하여야 고효율ㆍ저비용 정화통을 개발할 수 있으며, 본 연구에서는 이러한 첨착흡착제를 개발하여 이를 방독마스크 정화통에 적용하고자 하였다.(중략)

• KSBB Journal
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• v.25 no.5
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• pp.421-428
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• 2010

This paper reports on the experimental investigation carried out to evaluate the physical optimal conditions in the absorption column to remove odorous hydrogen sulfide gas. Hydrogen sulfide gas, as a highly undesirable contaminant, is most widely emitted from environmental treatment facilities. The absorbent mixed with natural second metabolites extracted from conifer trees and chemical absorbent of 2-aminoethanol was applied to remove it via chemical neutralization. The absorbent of natural second metabolites was achieved by a removal efficiency of 20-40% by itself depending on the treatment conditions, but the complex absorbent mixed with 0.1% amine chemical provides the removal efficiency of 98%. The optimal removal efficiencies have been examined against the two major parameters of temperature and pH. This study shows that the aqueous solution by natural second metabolites can be used as an appropriate absorbent in the column absorbed for the removal of hydrogen sulfide gas.

• Journal of Conservation Science
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• v.26 no.4
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• pp.437-443
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• 2010

The influence of noxious corrosive gas, which is the product of fossil fuel, and the acidic descent material, which becomes the reason for such reaction, on wax which protects the cultural assets, and the habitat factor were researched. It could be viewed that corrosion occurred rapidly due to the acidic descent material, which have the long staying on the material, rather than harmful corrosive gas. Also, it could be figured out that such corrosion began from whitening phenomenon of coated wax. As the acidity increased, more whitening phenomenon occurred, and eventually, it could be found out that whitening effect began due to the acidic descent material, corrosive gas and various 0.1 M acid solution, which lead to the exposure of internal metal, and corrosion occurred. The wax with the greatest resistance to the acidity due to its least changing aspect seemed to be Renaissance wax, except sulfuric acid.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.1
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• pp.21-31
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• 2000

Performance characteristics of a wet air cleaning system were investigated experimentally, and discussed in relation with physicochemical properties of the target pollutants. The system is composed of an air cleaner, a separator, and a medium filter. Removal efficiency of the system was measured for ambient particles and gaseous air pollutants: $SO_2$, NO, $NO_2$, HCHO, and $NH_3$. For particle removal test, particles were introduced into the system through a fan, and the particle size distribution was measured at three locations by using two laser particle counters. Particle removal efficiency for each system component was obtained from the particle size distribution. It was found that the separator primarily removed coarse particles greater than $5{\mu}m$ in diameter, and that the medium filter mainly removed fine particles less than $5{\mu}m$ in diameter. For gas removal test, air with gaseous air pollutant was injected into the outlet of the fan, and the concentration was measured both at the upstream of the air cleaner and at the downstream of the separator. It was found that the gaseous species with high Henry's law coefficients, such as $SO_2$, HCHO, and $NH_3$, showed high removal efficiency, but the gaseous species with low Henry's law coefficients, such as NO and $NO_2$, showed low removal efficiencies. It was also found that negative ions were generated from the air cleaner.

• 한국가스학회:학술대회논문집
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• 1997.09a
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• pp.211-216
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• 1997

• Journal of Adhesion and Interface
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• v.21 no.2
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• pp.51-57
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• 2020

Recently, there has been growing interest in the study of removal of harmful and hazardous pollutants emitted by industrial activities. In this study, we have developed porous activated carbon fibers prepared by a water vapor activation method and analyzed the adsorptions of the harmful gases with electrochemical responses of activated carbon fibers. To control the uniformity of pore structures, active reaction areas, and active sites, the reaction conditions of activation temperatures were varied from 750 to 850 ℃ with the predetermined reaction time intervals (30 to 240 min). The SO₂ and NO gas adsorptions of activated carbon fibers prepared by various reaction conditions were analyzed and monitored by electrochemical sensor responses. In particular, the activated carbon fibers prepared at the reaction temperature of 850 ℃ and time of 45 min showed the highest specific surface area (1,041.9 ㎡/g) and pore characteristics (0.42 ㎤/g), and excellent adsorption capabilities of SO₂ (1.061 mg/g) and NO (1.210 mg/g) gases, respectively.

• 월간 기계설비
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• s.63
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• pp.62-66
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• 1995

• Proceedings of the Korea Society of Poultry Science Conference
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• 2004.11a
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• pp.41-51
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• 2004

• The monthly packaging world
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• s.129
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• pp.142-143
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• 2004

• Proceedings of the Korea Technical Association of the Pulp and Paper Industry Conference
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• 2010.04a
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• pp.19-19
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• 2010