• 청정기술
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• 제3권1호
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• pp.96-105
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• 1997

본 연구는 유,무연탄 혼합 유동층 석탄연소로에서 폐제지슬러지를 탈황제로 사용하였을 경우 석회석 입자크기, 주입공기 유속, Ca/S 몰비, 무연탄비, 층온도 등에 따른 $SO_2$ 제거 효율에 관해 연구하였으며, 실험결과는 다음과 같다. 폐제지슬러지의 입자크기는 탈황율에 매우 큰 영항을 주는 것으로 나타났으며, 입자크기 $1016{\mu}m$ 일 때 가장 높은 탈황율을 보였고, 주입되는 공기의 유속변화에 따른 탈황율에는 큰 차이가 없었다. Ca/S 몰비가 증가할수록 탈황율도 증가하였으며, Ca/S 몰비 3까지는 급격히 탈황율이 증가하였으나 3이상에서는 큰 차이가 없었으므로 Ca/S 몰비는 3이 적절한 것으로 나타났다. 또한, 층온도는 탈황율에 큰 영향을 주는 것으로 나타나 $800^{\circ}C$에서 가장 높은 탈황율을 보였으며, 무연탄비가 증가할수록 탈황율이 약간 증가하는 것으로 나타났다. 따라서, 유,무연탄 혼합연소시 폐제지슬러지는 매우 높은 탈황율을 보여 탈황제로서의 가능성을 확인할 수 있었다.

• 상하수도학회지
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• 제19권1호
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• pp.16-24
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• 2005

Mathematical model was developed to verify a sequential particle removal taking place in a granular media gravity filter. Consequential multi-layer filtration cycle model was applied to verify the fraction of filter effluent particles that are filter influent particles that were never removed as well as the fraction of filter effluent particles that were detached after deposition were performed through laboratory experiments. Three sizes of marker particles were injected ahead of the filter column as a pulse in the presence of four sizes of polystyrene particles that were used as a primary source of particles in the raw suspension to investigate particle attachment alone in contrast to net removal from attachment and detachment. Microscopic counting of filter effluent particles was assumed to reflect attachment. Experimental results indicated that particle detachment is significant beginning from the early phase of filtration. For each size of fluorescent microspheres at one filter depth, fluorescent microsphere removal increased with filter runtime to a maximum due to ripening. The detached fraction of effluent particles increased with particle size and filter depth. The presence of detached particles and the increasing fraction of detached particles in deeper bed were confirmed.

• 한국대기환경학회:학술대회논문집
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• 한국대기환경학회 2005년도 추계학술대회 논문집
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• pp.494-496
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• 2005

• 한국안전학회지
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• 제14권1호
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• pp.78-85
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• 1999

The removal characteristics of H$_2$S from IGCC process over the natural manganese ore(NMO) containing several metal oxides($MnO_x$ : 51.85%, $FeO_y$ : 3.86%, CaO : 0.11%) were carried out in a batch type fluidized bed reactor(I.D.=40mm, height=0.8m). The $H_2S$ breakthrough curves were obtained as a function of temperature, initial gas velocity, initial gas concentration, and aspect ratio. The effect of particle size ratio and particle mixing fraction on $H_2S$ removal were investigated with binary system of different particle size. From this study, the adsorption capacity of $H_2S$ increased with temperature but decreased with excess gas velocity. The breakthrough time for $H_2S$ is reduced as the gas velocity is increased which leaded to gas by-passing and gas-solid contacting in a fluidized bed reactor. The results of the binary particle system with different size in batch experimental could predict to improve the behavior of continuous process of $H_2S$ removal efficiency. The natural manganese ore could be considered as potential sorbent in $H_2S$ removal.

• 상하수도학회지
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• 제23권6호
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• pp.719-726
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• 2009

One of the alternative runoff management measures is on-site runoff mitigation, such as rainwater retention tank and infiltration facilities especially the latter that is possible to manage simultaneously runoff quality and quantity as a perspective of water-cycle. This study was conducted to develop a particle separator, inclined-pipe settling system, that could improve particle removal efficiency of road runoff as a pre-treatment device of stormwater infiltration. Solid particles larger than $100{\mu}m$ are separated by simple sedimentation; however, the significant amount of pollutants with a diameter less than $100{\mu}m$ remain in suspension. Without any treatment in that case of the runoff into infiltrate, groundwater would be deteriorated and also infiltration rate would be decreased by clogging. Therefore, we suggest optimal design parameters (inclined angle, pipe length, and surface loading rate) of inclined-pipe settling system which can be designed to effectively remove particles diameter smaller then $70{\mu}m$. Thus, the results showed TSS removal efficiency more than 80% with a particle diameter between $20{\mu}m$ and $70{\mu}m$, 100% above particle diameter $70{\mu}m$ for the inflow rate $0.018 m^3/m^2{\cdot}hr$ with pipe inclined at angle $15^{\circ}$.

• 한국입자에어로졸학회지
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• 제16권1호
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• pp.1-8
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• 2020

Nano-pulse plasma technology has great potential as the process simplicity, high efficiency and low energy consumption for SO₂ removal. The research on the gas-to-particle conversion is required to achieve higher efficiency of SO₂ gas removal. Thus, we studied the effect of the relative humidity, NH₃ concentration and applied voltage of the nano-pulse plasma system in the gas to particle conversion of SO₂. The particles from the conversions were increased from 10 to 100 nm in diameter as relative humidity, NH₃ concentration, applied voltage increases. With these results, nano-pulse plasma system can be used to more efficient removal of SO₂ gas by controlling above parameters.

• Korean Chemical Engineering Research
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• 제57권4호
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• pp.461-468
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• 2019

석탄화력발전소에서 발생하는 분진 효율을 높이고 미세먼지와 극미세먼지까지 집진할 필요성이 높아지고 있다. 상압 영역에서 운전되는 플랜트 발생 분진 제거를 위해서는 백필터나 전기집진기를 사용하나, 고온고압에서 운전되는 석탄가스화와 같은 경우는 금속필터나 세라믹필터가 사용된다. 고온고압에서 분진 집진을 위해 2종의 5겹 압착/소결한 금속필터를 제작하였고 이를 사용했을 때 분진 포집효율과 $10{\mu}m$ 이하 입자에 대한 포집 성능을 파악하였다. 석탄가스화 분진에 대한 금속필터의 집진효율은 무게기준으로 99%대에 달하였다. 제작한 금속필터 2종의 미세먼지 입자 이하(< $2.5{\mu}m$) 크기까지 집진성능을 파악하고자 JIS 분진 표준시료를 대상으로 실험을 수행하였고, $1{\sim}2.5{\mu}m$ 입자크기 범위에 대해 97%와 70~82%의 집진 성능을 확인하였다. $1{\mu}m$ 이하 입자크기 영역에서는 입자크기가 작아짐에 따라 제작한 금속필터의 집진효율이 급격히 낮아짐을 볼 수 있었다. 이러한 $1{\mu}m$ 이하 입자들에 대한 집진 제한점을 극복하고자 금속필터 성능의 개선 방안을 제시하였다.

• 한국입자에어로졸학회지
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• 제6권4호
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• pp.173-183
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• 2010

The high temperature pleated filter bags which were used during this study were made of pleated nonwoven fabric of heat and acid resistant polysulfonate fibers which can withstand the heat up to $300^{\circ}C$ and have a filtration area which is 3 to 5 times larger than the conventional round filter bags. Cartridge module packed with 3 kind of the sulfur impregnated activated-carbon based sorbents were inserted in the inner of the pleated filter bag. This type of pleated filter bag was designed to remove not only the particulate matter but also the gaseous elemental mercury. The electrostatic precipitator part can enhance the particulate removal efficiency and reduce the pressure drop of the pleated filter bag by agglomerated particles to form a more porous dust layer on the surface of the pleated bag which is increased the filter bag cleaning efficiency. In addition, the most of particles are separated from the flue gas stream through the cyclone and the electrostatic precipitator part which were installed at the lower part and main body part of the convergence particulate collector, respectively. Thus reduce particulate loading of the high temperature pleated filter bags were applied in this study to analyze the removal characteristics of particulate matter and gaseous elemental mercury.

• 한국입자에어로졸학회지
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• 제16권4호
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• pp.119-130
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• 2020

In this study, we developed a separated two-stage electrostatic precipitator applicable in a subway air conditioning system. We studied the characteristics of collection efficiency of 0.3 ㎛ particle and ozone generation at different charger sizes and gaps of collector plates. Also, we compared the performance of the two-stage ESP to the MERV 10 filter with the removal efficiency of 10% used in actual subway air conditioning system. The maximum collection efficiency of 0.3 ㎛ particle was 93% at A charger (600 mm×250 mm×600 mm) and 84% at B charger (330 mm×280 mm×330 mm). Especially, with voltages applied to chargers with collection efficiency of about 80% or more, the ozone concentration of two different chargers was 5 ppb to 35 ppb. Finally, the filter quality of the collector developed in this study was 400 times higher than that of the MERV 10 filter. Therefore, it was concluded that the two-stage ESP could be a promising PM removal device suitable for subway air conditioning system.

• 설비공학논문집
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• 제14권10호
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• pp.792-800
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• 2002

A grease filter is used to remove grease generated from a cooking appliance in a kitchen. This numerical study has been conducted to investigate the particle collection characteristics of a grease filter having nominal flowrate of $100m^3$/h. The flow field and particle trajectories in the grease filter with a flow chamber were simulated by using the commercial code of STAR-CD. The air velocity and pressure distributions were discussed in detail. The pressure drop of a grease filter rapidly increases with increasing the air flowrate. The numerical values of the pressure drop are slightly lower than the experimental values when the air flowrates are 50, 75, and 100㎥/h. The particle collection efficiency of a grease filter increases with increasing the particle diameter, the particle density, and the air flowrate, which means that the inertial impaction is a dominant particle removal mechanism in a grease filter. The cut-off diameter of the tested grease filter representing 50-% collection efficiency is about 11.6$\mu$m for water droplets at $100m^3$/h.