• 한국환경과학회지
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• 제23권12호
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• pp.2045-2056
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• 2014

In this study, pressure drop was measured in the pulse jet bag filter without venturi on which 16 numbers of filter bags (Ø$140{\times}850{\ell}$) are installed according to operation condition(filtration velocity, inlet dust concentration, pulse pressure, and pulse interval) using coke dust from steel mill. The obtained 180 pressure drop test data were used to predict pressure drop with multiple regression model so that pressure drop data can be used for effective operation condition and as basic data for economical design. The prediction results showed that when filtration velocity was increased by 1%, pressure drop was increased by 2.2% which indicated that filtration velocity among operation condition was attributed on the pressure drop the most. Pressure was dropped by 1.53% when pulse pressure was increased by 1% which also confirmed that pulse pressure was the major factor affecting on the pressure drop next to filtration velocity. Meanwhile, pressure drops were found increased by 0.3% and 0.37%, respectively when inlet dust concentration and pulse interval were increased by 1% implying that the effects of inlet dust concentration and pulse interval were less as compared with those changes of filtration velocity and pulse pressure. Therefore, the larger effect on the pressure drop the pulse jet bag filter was found in the order of filtration velocity($V_f$), pulse pressure($P_p$), inlet dust concentration($C_i$), pulse interval($P_i$). Also, the prediction result of filtration velocity, inlet dust concentration, pulse pressure, and pulse interval which showed the largest effect on the pressure drop indicated that stable operation can be executed with filtration velocity less than 1.5 m/min and inlet dust concentration less than $4g/m^3$. However, it was regarded that pulse pressure and pulse interval need to be adjusted when inlet dust concentration is higher than $4g/m^3$. When filtration velocity and pulse pressure were examined, operation was possible regardless of changes in pulse pressure if filtration velocity was at 1.5 m/min. If filtration velocity was increased to 2 m/min. operation would be possible only when pulse pressure was set at higher than $5.8kgf/cm^2$. Also, the prediction result of pressure drop with filtration velocity and pulse interval showed that operation with pulse interval less than 50 sec. should be carried out under filtration velocity at 1.5 m/min. While, pulse interval should be set at lower than 11 sec. if filtration velocity was set at 2 m/min. Under the conditions of filtration velocity lower than 1 m/min and high pulse pressure higher than $7kgf/cm^2$, though pressure drop would be less, in this case, economic feasibility would be low due to increased in installation and operation cost since scale of dust collection equipment becomes larger and life of filtration bag becomes shortened due to high pulse pressure.

• 한국대기환경학회지
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• 제23권2호
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• pp.203-213
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• 2007

Numerical analysis has been performed to understand flow characteristics in the reactor with bag filters in an integrated adsorption/catalytic process which can treat dioxin and $NO_{x}$ together. Computational fluid dynamics technique was employed with Euler-Lagrangian model to consider flue gas and activated carbon particles simultaneously, so that residence time of flue gas and activated carbon particle could be obtained from the numerical analysis directly. The numerical analysis has been performed with different three particle sizes and compared each flow characteristics with particle's size. Fundamental flow patterns of flue gas and activated carbon particles, pressure distribution, residence time of flue gas and activated carbon particles, and distribution of activated carbon have been obtained from the numerical analysis. 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 results obtained would be effectively used to estimate the removal efficiency in the reactor once the residence time is combined with the reaction equation.

• 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.

• 한국막학회:학술대회논문집
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• 한국막학회 1995년도 심포지움시리즈 Jan-95 산업용 여과집진막 제조 및 신응용
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• pp.113-134
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• 1995

GORE-TEX MEMBRANE은 PTFF(POLYTETRA FLUOROETHYLENE)를 특수가공하여 극히 미세한 구조를 가지는 연속다공질체로 만들어 습,건식용 산업용 여과재로써 활용하므로써 그동안 사용되어오던 종래의 심층여과방식의 여과포로서는 도저히 이룰 수 없었던 표면여과기능을 갖춤에 따라 높은 집진효율이나 낮은압력손실로 동시에 운전을 가능하게한 새로운 기능의 첨단여과포로써 각종산업분야에 이미 널리 적용되고 있다. 근래 BOILER, 소각로, 제철, 제강용로등의 고온용 BAG FILTER 소요가 증가됨에 따라 보다 효율적이고 경제적인 고온용 여과포에 대한 관심이 높아지고 있으며, 특히, 소각로, 발전설비, CEMENT 생산공정중 KILN 공정등에 주로 사용되어오던 전기 집진기 (ELECTROSTATIC PRECIPITATOR)의 집진효율이 DIOXINE 이나 FURAN 등의 새로운 규제와 중금속, 혹은 분진들에 대해 강화되는 환경 규제치에 적응하기 어려워짐에 따라 BAG FILTER로의 전환/개선 방안이 많이 연구되고 있으며 이미 활용되어지는 부분도 있는바 이에 대한 새로운 적용방법등을 소개하고자 한다.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2012년도 제44회 KOSCO SYMPOSIUM 초록집
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• pp.151-152
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• 2012

Collectors connected to diesel engine exhaust pipe for application of PM reduction facilities which was used to reduce PM from the exhaust gas produced from ship, Filtration performance of PM was tested. In this system, it was confirmed that the bag house can remove over 90 percent of PM from a lot of high temperature and high pressure gases produced in diesel engine. The results obtained from performance test show the potential possibility for commercialization of ceramic filter collectors which is applied to reduction facilities of flue gas produced from a diesel engine on the ship.

• 한국대기환경학회지
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• 제11권4호
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• pp.373-375
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• 1995

In order to turn the Bag Filter to the Purse Filter, the past system that the adverse reason is removed, the input of synthetic materiality of dust and air is placed down, and the output is placed up has been improved so that any adverse effect shall not be raised. The form of filteration mechanism is changed from a cylinder from, and the dust and air is mixed to make the entry velocity and one person can velocity of the mixed materiality become lower by the use of infinity, and the reception of filteration mechanism has been made reasonably. The dust separated from the filteration mechanism is desceded down, snd the mixde materiality is ascended up. So, a cross point is formed, and a collision and a friction is occurred from its process, and at its result, dust is scattered to stick to a filter cloth, therefore, the loss of pressure shall ont be appeared by cause of the increase of dust-loading.

• 한국산학기술학회논문지
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• 제14권2호
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• pp.983-989
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• 2013

본 연구에서는 하나의 장치 내에서 "싸이클론-관성충돌-여과포 집진"이 동시에 이루어지는 멀티 집진기의 집진 효율을 극대화시키기 위한 설계 조건을 검토하였다. 먼저 싸이클론의 입구 형상에 대한 수치 해석 결과, 접선 유입식 입구에 가이드 베인을 추가로 설계한 경우 선회류의 회전수가 많고 강하게 형성되어 사이클론부에서 조대입자의 유선 이탈을 촉진시키는데 매우 효과적인 것으로 예측되었다. 그러나 사이클론의 하단부가 벤츄리 모양이기 때문에 약 4~5 m/s의 강한 하향 흐름이 호퍼 하단까지 지속되어 분진의 재비산 가능성이 있는 것으로 나타났다. 이에, 사이클론부 하단의 벤츄리를 제거하며 분진 재비산 문제는 해소 가능할 것으로 나타났다. 충돌 차단형 배플의 간격을 조정하여 통과유속을 빠르게 한 결과, 충돌 효과는 더욱 증가할 것으로 예측되었으나 탈리 분진이 간섭을 받을 수 있는 문제점이 예상되어 배플은 기본 설계안대로 유지하는 것이 바람직할 것으로 나타났다.

• 청정기술
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• 제6권2호
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• pp.121-127
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• 2000

소각로 배가스중에는 분진, 산성가스, 중금속, 다이옥신 등의 여러 유해물질이 함유되어 있다. 이러한 유해가스 중의 다이옥신을 제거하기 위한 방법중의 하나인 활성탄의 흡착을 이용한 유해물질 제거 방법의 효율을 조사하였다. 다이옥신의 전구물질인 1,2-dichlorobenzene (o-DCB)를 사용하였으며 기존의 소각로에 추가 설비가 필요 없이 활성탄을 반건식 반응기에서 소석회와 함께 분무하고 백필터로 여과하는 공정에 대하여 반응기 운전 온도, atomizer r.p.m., 활성탄 양 변화에 대한 효율을 조사하였다. 실험결과 소석회와 활성탄 분무를 위한 atomizer의 rpm이 클수록, 즉 분무 입자 크기가 작을수록 제거 효율은 증가하였고 반건식 반응기에서의 배가스 유출온도는 백 필터의 유입온도에 준하여 결정하는 것이 타당하며 $145^{\circ}C$로 유지하는 것이 필요하였다. 또한 백필터에서의 제거효율이 반건식 반응기에서의 제거효율보다 높음을 알 수 있었다.

• 한국대기환경학회:학술대회논문집
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• 한국대기환경학회 2001년도 추계학술대회 논문집
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• pp.95-96
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• 2001

인천항은 한국의 주항의 하나로 원자재 수입화물을 취급하는 항만이다. 수입된 원자재 중에서 대두박등의 사료 부원료의 취급 시 강한 바람, 차량의 이동, 저장시설에서의 상하차 등에 의하여 다량의 비산먼지가 발생하여 인천항의 주된 비산먼지 오염원이 되고 있는 실정이다 (Jeon et al., 2000). 일반적으로 사료 부원료의 취급에 의하여 발생하는 비산먼지의 제진을 위하여, 사료 부원료 취급시설에 bag filter에 의한 제진시설이 사용되고 있다. (중략)

• 한국대기환경학회:학술대회논문집
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• 한국대기환경학회 2002년도 추계학술대회 논문집
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• pp.415-416
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• 2002

급속한 경제발전에 따라 생활 수준이 향상되고 생활양식도 많이 변화되고 있으며 가정이나 생산현장에서 발생하는 폐기물의 발생량은 급속히 증가하고 있다. 해마다 누적되어 가는 폐기물 매립량의 증가로 인하여 기존 폐기물 매립지는 현재 거의 포화 상태에 달해 있다. 이에 따라 우리나라의 폐기물 처리 방법은 기존의 매립위주에서 소각처리로 점차 확대되어 나가고 있는 실정이지만 소각시설 인근 지역의 환경 질 저하에 대한 문제점 및 주민민원 발생 또한 빈번해지고 있는 추세이다. (중략)