• 환경위생공학
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• 제18권2호
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• pp.87-93
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• 2003

This study carried out to recommend adaptable technologies and countermeasures for performance improvement of Wet Scrubber(WS) in industrial waste incinerator. When not using the Activated Carbon(AC), the removal efficiency of dust and HCl is 73%, 92%. And particulate phase and gaseous phase dioxins removal efficiency was evaluated up to 31% and 12%. In this case, dioxins enrichment was not revealed in WS. When using the AC mixing with scrubbing water, the case of 1,000ppm, removal efficiency of particulate phase dioxins was about 51%, and gaseous phase dioxins was about 96%. The case of 2,000ppm, removal efficiency of particulate phase dioxins was about 55%, and gaseous phase dioxins was about 97%. And the case of 3,500ppm, the removal efficiency of particulate phase dioxins was about 35%, and gaseous phase dioxins was about 96% respectively. By this study, using the AC was more useful to remove the gaseous phase dioxins, and needed to use proper concentration of the AC, that in case of 3,500ppm, the particulate phase dioxins removal efficiency was more lower than other cases.

• 한국대기환경학회:학술대회논문집
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• 한국대기환경학회 2007년도 추계학술대회 논문집
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• pp.181-182
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• 2007

• 자원리싸이클링
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• 제8권5호
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• pp.51-58
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• 1999

석탄화력 발전소에서 발생하는 수백만 톤의 석탄회는 콘크리트 혼화재 및 건축자재로 재활용이 가능함에도 불구하고 과다한 미연탄소 함량으로 인해 대부분 회사장(Ash Pond) 되는데, 이로 인해 환경오염유발, 회사장 포화에 따른 발전소의 수명 감소, 그리고 재활용 가능한 자원의 낭비와 같은 문제가 발생한다. 본 연구는 석탄회 내의 미연탄소분을 분리하여 미연탄소분 함량이 낮은 고순도 석탄회를 회수하기 위해 직류관 믹서(In-Line Mixer) 발생기키는 역류형 컬럼부선기를 이용하였다. 이때 입자 표면에 소수성의 특성을 강화시키는 포스제의 증가에 따른 석탄회와 미연탄소 입자의 분리 특성을 분석하였다. 석탕회 톤당 8ι의 포수제를 사용한 역류형 컬럼 부선기를 이용하여 미연탄소분 함유량이 7%인 석탄회를 분리 실험한 결과 미연탄소분 함유량 0.5%인 고순도 석탄회를 88.2% 회수하였다. 그리고 질량 평균입경이 21.2$mu extrm{m}$인 석탄회를 분리 실험하여 입도를 분석한 결과 분리 정도에 따라 입도는 뚜렷하게 구별되어 나타났는데, 분리효율이 증가할수록 정제 석탄회의 경우 입도는 조대해져 입도 분포의 양극화 현상이 뚜렷하게 나타났다. 포수제의 투입량이 증대함에 따라 미연탄소 입자의 계면에 소수성이 강화되어 분리 특성이 향상되었으며, 이때 회수한 고순도 석탄회의 입도는 미세화 되는 경향이 나타났다.

• 방사성폐기물학회지
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• 제3권1호
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• pp.9-16
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• 2005

To evaluate parameters influencing on the dust removal of the High Temperature Filter(HTF) system, a computer simulation of fluid dynamics inside the system had been performed. The results showed that the optimum pulse jet periods were 50ms and 90ms for the 1000mm and 1500mm long filter elements respectively. Dust removal effect was very excellent under the pulse jet pressure of 3 bar. But the distance between the pulse jet nozzle and the venturi of a filter element had no meaningful effect on the performance with the variation from 5mm to 10mm. Compared to the dispersion mode of pulse jet, the collective mode of pulse jet flow was preferable in maintaining the pressure inside the system stable.

• 한국염색가공학회지
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• 제22권2호
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• pp.94-100
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• 2010

Colored compounds adsorption from the textile dyeing effluents on activated carbons produced from various indigenous vegetable sources by zinc chloride activation is studied. The most important parameters in chemical activation were found to be the chemical ratio of $ZnCl_2$ to feed (3:1), carbonization temperature (460-470 $^{\circ}C$) and time of activation (75 min). The absorbance at 511 nm (red effluent) and 615 nm (blue effluent) are used for estimation of color. It is established that at optimum temperature ($50^{\circ}C$), time of contact (30-40 min) and adsorbent loading (2 g/L), activated carbons developed from rain tree (Samanea saman) saw dust and blackberry (Randia formosa) tree saw dust showed great capability to remove color materials from the effluents. It is observed that adsorption of reactive dyes by all types of activated carbons is more than that of disperse dyes. It is explained that because of its acidic nature the activated carbon can adsorb better reactive dye particles containing large number of nitrogen sites and $-SO_3Na$ group in their structure. The use of activated carbons from the indigenous biomass would be economical, because saw dusts are readily available waste worldwide.

• 한국분말재료학회지
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• 제21권6호
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• pp.454-459
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• 2014

In this study, the porous ceramic filter was developed to be able to remove both dust and hazardous gas contained in fuel gas at high temperature. The porous ceramic filters were fabricated and used as a catalyst support. And the effects have been investigated such as the mean particle size, organic content and addition of foaming agent on the porosity, compressive strength and pressure drop of ceramic filters. With the increase of mean powder size and the organic content for the cordierite filter, the porosity was increased, but the compressive strength and pressure drop were decreased. From the results of the research, the optimum condition for the fabrication of ceramic filters could be acquired and they had the porosity of 58%, the compressive strength of 13.4 MPa and the pressure drop of 250 Pa. It was expected that this ceramic filter was able to be applied to the glass melting furnace, combustor, and dust/toxic gas removal filter.

• 상하수도학회지
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• 제10권4호
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• pp.103-110
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• 1996

Excessive phosphorus (P as orthophosphate) is one of the major pollutants in natural water that are responsible for algal blooms and eutrophication. P removal by slag is an attractive solution if the P sorption capacity of the slag is significant. To design an efficient land treatment facility, basic information on the behaviour of P in the media-water environment is required. In this study, detailed column experiments were conducted to study the P transport under dynamic condition, and mathematical models were developed to describe this process. The column experiments conducted with dust and cake waste products (slag) from BHP steel industry in Australia as adsorbing media indicated that they had higher sorption capacity of P than that of a sandy loam soil from North Sydney, Australia. P transport in the dust and cake columns exhibited characteristics S-shaped or curvilinear breakthrough curves. The simulated results from a dynamic physical non-equilibrium sorption model (DPNSM) and Freundlich isotherm constants satisfactorily matched the corresponding experimental breakthrough data. The mobility of P is restricted proportionally to the adsorbent's sorption capacity.

• 한국응용과학기술학회지
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• 제15권1호
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• pp.79-90
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• 1998

One of the objectives of this study were to develop a process for manufacturing activated carbons from agricultural by-products(rice shells and saw dust) and another is to measure the iodine number, ash content and removal ratio of COD. The other is to compare those values with those of commercialized activated carbons. Agricultural by-products based activated carbons were manufactured through the steam-reaction method. A rotary kiln type furnace was used for both carbonization and activation. The optimum operating temperatures for carbonization and activation were $650^{\circ}C$ and $900^{\circ}C$, respectively. For the activated carbons produced under these conditions, the iodine number was 1,127mg/g. Especially, removal efficiency of COD was 61.5% for 40mg/L of wastewater and 30% for 150mg/L of SLS(Sodium Lauryl Sulfate).

• 공업화학
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• 제22권1호
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• pp.77-80
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• 2011

본 연구에서는 볏짚, 톱밥, 밤껍질, 땅콩껍질 등 목질계 바이오매스를 이용하여 전처리과정으로 산처리과정을 진행한 후 리그닌 함량변화를 측정하고, 이에 따른 셀룰로오스 에탄올로의 전환특성을 해석하였다. 목질계 바이오매스의 리그닌 함량을 측정한 결과 밤껍질 < 볏짚 < 톱밥 < 땅콩껍질 순으로 리그닌 함량이 높게 측정되었으며, 셀룰로오스 에탄올로의 전환특성은 땅콩껍질 < 톱밥 < 볏짚 < 밤껍질 순으로 우수한 것으로 나타나 산처리과정으로 리그닌의 제거가 필요한 것으로 나타났다. 또한 산처리과정에서 황산의 농도가 증가함에 따라 리그닌 함량이 감소하여 셀룰로오스 에탄올의 수율은 증가하였으며, 최적 황산의 농도는 20 wt%로 선정하였다.

• 환경위생공학
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• 제23권3호
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• pp.9-22
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• 2008

This study was conducted to develop a system that processes harmful gases and dust, which being generated in the production of micro-inorganic fabric. This can be obtained by melt spinning raw materials such as agalmatolite, fluorspar, limestone, silica under high temperature at $1500-1600^{\circ}C$ in a glass recuperator using a dry method by Cyclone Reactor or Envelope Type (ET) type Bag Filter. If the number of the members of Korea Glass Industry Association reaches up to 45, the damage of the harmful gas being generated in recuperator should not be small. In addition, research of existing facilities showed the most of harmful gas treatment facilities which adopt wet treatment or semi-dry treatment process. This was caused the problems for wastewater and the second pollutive materials. Moreover, in the dust collecting facility behind recuperator, it is also problematic that electric dust collector requires enormous initial investment. We have researched various methods to show both economic and efficient new processes for the preventive facilities of recuperator. As the result of the experiments, the removal efficiencies of HF and SOx were 99% and 87%, respectively. Although it was insignificant reaction, a pretty much interesting result that NOx showed an absorption reaction with $Ca(OH)_2$(removal efficiency was more than 25%) was obtained.