• 상하수도학회지
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• 제14권1호
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• pp.54-61
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• 2000

Recently, our circumstances are threatened by an accident that leakage of under ground storage tank and illegal dumping of synthetic organic compounds at chemical plants and many treatment methods, Activated carbon adsorption, Ozonization, Membrane filtration and Photocatalystic oxidation, are developed to remove such a synthetic organic compounds. And it has reported that Activated carbon adsorption have a great removal efficiency to nondegradable matters and organic compounds which have a high molecular weight. Comparing with other adsorbents, Activated carbon adsorption have a worse efficiency when ad desorption speed is low. Thus improved type of adsorbents was invented and one of those is Activated Carbon Filter. The purpose of this study was getting information about adsorption characteristic phenol which can be applied Activated Carbon Fiber and Granular Activated Carbon. In detail, With comparing removal characteristics of phenol in the presence Humic Acid using Activated Carbon Fiber(ACF) and Granular Activated. Carbon(GAC), it is to certify an effective application of Activated Carbon Fiber. At the range of this study, Batch test, Isotherm adsorption test and Factorial analysis, following conclusion were obtained from the results of this study. Batch test was carried to know time of adsorption equilibrium. In this study about time of adsorption equilibrium by ACF was faster than GAC's, for developed micropore of ACF. From the result of phenol adsorption test, High removal rate of adsorption is shown at pH 5. The result of lsotherm adsorption test, it has represented that the Freundlich's isotherm is most suitable one in others, that a ACF's adsorption capacity is more excellent than GAC's. Adsorption of phenol exiting humic acid is decreased getting raised humic acid concentration. Since ACF's micropore is developed at this time, an effect of high molecular humic acid is lower. Factorial analysis was carried to know about Main effect which was injection dosage of adsorbent in the range of this study.

• 한국환경과학회지
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• 제17권8호
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• pp.899-905
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• 2008

Quality test for activated carbon(AC) filter used for drinking water purifier is now an obligatory test and the standard material for valid purifying amount in water purifier performance test has been changed from residual chlorine to chloroform according to the notice of Ministry of Environment in 2006. Therefore, this study aimed to compare the ingredients of AC filters by confirming chloroform removal rate of AC filter and conducting 4 adsorption tests (Iodine, methylene blue decolorization, phenol value, ADS value) for AC filters provided by manufacturers. With water pressure of $1kgf/cm^2$, 1,500 liters of prepared inflow went through to check chloroform removal rate. As a result, product with removal rate of below 60% from all products. On the other hand, 4 adsorption tests were conducted for filters in the market and filters from manufacturers. None of the products satisfied all 4 tests. In particular, they showed great shortage to the standard in phenol value and ADS value test. However, manufacturers' filter showed much better performance than filters in the market. Also, the result of valid purifying amount test for each of five products of appropriate product and inappropriate product based on filter quality test showed average 4,440 liters for appropriate product and average 2,620 liters for inappropriate product. According to the result, it is shown that the filter with good adsorption also had good chloroform removal efficiency and adsorption efficiency. Therefore, it is expected that customers can screen good quality product through obligatory conduct of filter quality test. However, it is considered that complementation in system is required for future inspection.

• Advances in environmental research
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• 제6권1호
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• pp.35-51
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• 2017

The use of Granular Activated Carbon (GAC) and naturally occurring silica (Sand) as filtration media in water and waste water treatment systems is very common. While GAC offers the additional functionality of being an "adsorptive" filter for dissolved organics it is also more expensive. In this paper we present an experimental evaluation of the performance of a bed of GAC for colloid removal and compare the same with that from an equivalent bed of Sand. The experiments are performed in an "intermittent" manner over extended time, to "simulate" performance over the life of the filter bed. The experiments were continued till a significant drop in water flow rate through the bed was observed. A novel "deposition" and "detachment" rate based transient mathematical model is developed. It is observed that the data from the experiments can be explained by the above model, for different aqueous phase electrolyte concentrations. The model "parameters", namely the "deposition" and "detachment" rates are evaluated for the 2 filter media studied. The model suggests that the significantly better performance of GAC in colloid filtration is probably due to significantly lower detachment of colloids from the same. While the "deposition" rates are higher for GAC, the "detachment" rates are significantly lower, which makes GAC more effective than sand for colloid removal by over an order of magnitude.

• 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.

• 분석과학
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• 제18권2호
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• pp.154-162
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• 2005

최근 국내 일부 정수장에서 검출된 것으로 보도되어진 바 있어 우리나라의 하천 수의 오염이 우려되고 있고, 일부 오염정도가 높은 하천수의 정화과정에서 제거가 완전히 이루어지지 않는 것으로 사료되는 1,4-dioxane은 그 독성과 음용수의 섭취량을 고려할 때 음용수 섭취로 인한 인체효과가 문제화 될 것으로 판단된다. 따라서 본 연구에서는 활성탄과 멤브레인으로 구성된 다단계 필터시스템에서 음용수 중에 존재하는 1,4-dioxane에 대한 제거효과에 대하여 연구하였다. 확인방법은 MTBE을 이용한 액체-액체 추출방법을 사용하였으며 제거실험은 압력별 필터단계별로 30 L마다 300 L 까지 실시하였다. 그 결과 초기에는 1차 활성탄 필터이후 70% 이상의 제거효과를 나타내었으며 멤브레인 이후 95%이상 그리고 2차 활성탄 이후 100% 제거되는 결과를 나타내었다. 그러나 통수량이 증가할수록 각 단계별 제거율은 점차 감소하였으며 300 L 통수 후 1차 활성탄에서 30%, 멤브레인 이후 88% 그리고 최종 활성탄 이후 99%의 제거율을 나타내었다.

• 대한기계학회논문집B
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• 제31권5호
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• pp.425-434
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• 2007

An integrated adsorption/catalytic process has been considered to treat dioxin and $NO_x$ simultaneously. The process consists of a cyclone and a reactor with nine bag filters. In this study, numerical analysis has been performed to understand flow characteristics with inflow-duct types in the reactor. To consider flue gas and activated carbon particles simultaneously, Euler-Lagrangian model was employed. Fundamental flow patterns of flue gas and activated carbon particles, pressure distribution and distribution of activated carbon have been obtained from the numerical analysis. Also trace length and residence time of flue gas, residence time of activated carbon particles have been calculated directly. Flow patterns of flue gas and activated carbon particles in the reactor were very complicated and they moved along very various paths. Therefore, their residence time in the reactor was also various. The flow characteristics in the reactor were strongly influenced by inflow-duct types. The results obtained would be effectively used to estimate the removal efficiency in the reactor once the residence time is combined with the reaction equation.

• 설비공학논문집
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• 제25권4호
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• pp.194-200
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• 2013

In this study, an exhaust filter unit for removing bad smells is designed and manufactured to understand the characteristics, damages, and effects on humans and animals of bad smell substances in laboratory animal breeding facilities. Using the exhaust filter unit, a deodorization performance test using ammonia gas, as a typical bad smell in an animal breeding room, was carried out for three types of activated and impregnated charcoal filters. The experimental results showed that the pressure loss of the HEPA and carbon filter was increased with flow rate and that the average deodorization performance for the case where an impregnated carbon filter was installed was a maximum value of between 93 and 96%, with various fractional flow rates ranging from 1,500 to $3,500m^3/h$ in a laboratory animal breeding room. The experimental results will also be used for the design and manufacture of a practical and efficient exhaust filter unit to cope with bad smell problems in animal breeding facilities.

• Korean Chemical Engineering Research
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• 제52권2호
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• pp.261-265
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• 2014

정수처리 방식에 있어서 소형화의 필요성이 증대됨에 따라 복합적인 기능을 갖는 단일구조 여과재 개발이 절실히 요구되고 있다. 본 연구에서는 단일구조를 가지는 필터개발을 위하여 활성탄과 고분자 바인더로 구성된 성형체를 압출소결방식으로 제조하여, 제조된 성형체의 밀도, 공극률 및 유량을 평가하여, 최대유량을 가지는 성형체의 최적 압출온도를 결정하였다. 또한 성형체의 공극률 평가에 있어서 전체 공극률뿐만 아니라 관통형 기공의 공극률을 추가로 평가하여 유량과의 상관성을 평가하였다. 압출온도가 고분자 바인더의 Melting point인 $133^{\circ}C$ 이상인 $140{\sim}230^{\circ}C$에서 단일구조 복합 활성탄 성형체 구성이 가능하였으며, 압출온도 $170^{\circ}C$가 복합성형체의 밀도가 낮고, 관통기공의 공극률이 높아, 최대유량을 가지는 복합성형체의 제조가 가능한 최적 압출온도로 확인되었다. 또한 복합성형체를 통해 흐르는 물의 유량은 성형체의 전체 공극률 보다 관통형기공의 공극률에 크게 의존함을 알 수 있었다.

• Journal of Korean Society for Atmospheric Environment
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• 제18권E2호
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• pp.79-84
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• 2002

The objective of this study was to investigate the biodegradation of ethylene in an activated carbon biofilter inoculated with immobilized microbial consortium. The biofilter performance was monitored in terms of ethylene removal efficiency and carbon dioxide production. The biofilter was capable of achieving ethylene removal efficiency as much as 100% at a residence time of 14 min and an inlet concentration of 290 ppm. Under the same conditions, carbon dioxide with a concentration of up to 546 ppm was produced. Its was found that carbon dioxide was produced at a rate of 87 mg day$\^$-1/, which corresponded to a volume of 0.05 L day$\^$-1/. During operation with an inlet ethylene of 290 ppm, the maximum elimination capacity of the biofilter was 34 g of C$_2$H$_4$m$\^$-3/ day$\^$-1/. The biofilter could provide an attractive treatment technology for removing ethylene, an extremely volatile and slowly adsorbed compound.

• Composites Research
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• 제29권5호
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• pp.256-261
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• 2016

본 연구에서는 습식공정을 이용한 Pitch계 활성탄소섬유와 바인더 섬유를 이용하여 필터 페이퍼를 제조하였다. 필터 페이퍼 내 바인더 섬유의 함량이 기공특성에 미치는 영향을 알아보기 위해 77 K에서 질소 흡착 등 온선과 주사 전자 현미경을 통해 흡착특성을 비교 분석하였다. Pitch계 활성탄소섬유와 바인더 섬유와의 최적 비율은 70:30 비율로 가장 균일한 기공 및 결합력이 좋은 페이퍼의 모습을 보였으며, 바인더 섬유의 함량이 적을수록 높은 비표면적 값을 확인하였다. Pitch계 활성탄소섬유와 바인더 섬유의 종류와는 상관없이 70:30 비율에서 최적의 페이퍼가 제조되었으며, $650.4m^2/g$의 비표면적 값과 86.9%의 유해가스 제거율을 확인하였다. 또한 필터 페이퍼의 평균 기공 크기 분포는 바인더 섬유의 영향을 받지 않는 것으로 관찰되었다.