• 한국환경과학회지
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• 제32권8호
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• pp.555-561
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• 2023

A study is to predict the effective pulsing distance following to the pulsing pressure, nozzle diameter, filtration velocity using numercial analysis techniques and use it as an efficient operation condition and economic data for on-line type pulse air jet bag filter. Filtration area 6 m² condition, calculate filter resistance coefficient for simulation through the primary experiments using coke dust. For CFD simulation, analysis pulsing characteristics about nozzle diameter, filtration velocity and pulsing pressure. The maximum pulsing length of on-line type pulse air jet bag filter, in 10mm nozzle, filtration velocity 1.5m/min and pulsing pressure 5 bar conditions, is 2,285 mm, maximum length is 76.2% of the total filter bag, which is sufficient to pulsing. In 12mm nozzle, pulsing pressure 5 bar and filtration area 1.22 m² conditions, the maximum pulsing length of on-line type pulse air jet bag filter is 1,744~2,952 mm, and the maximum length is 2,952 mm indicates pulsing air can be reached to the bottom of filter bag. When the nozzle diameter is increased 8mm to 10mm, maximum pulsing length is extended 40~47%, and increased 10mm to 12 mm, maximum pulsing length is extended 10~17%. For effective pulsing, over the 5bar of pulsing pressure and larger than 10 mm of nozzle diameter are required.

• 한국환경과학회지
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• 제32권9호
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• pp.659-669
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• 2023

The purpose of this study is to predict the pressure drop due to the installation of venturi under diverse operating conditions such as dust concentration, pulse interval and pressure, and filtration velocity using algebraic-linear regression model and use it as an economic data and efficient operating condition for a pulse air jet bag filter. A pilot scale bag filter with a filter a filter size(Ø140 × 850ℓ, 12) was used, and the filters used in the experiment were the polyester filters most commonly used in real industrial sites. The SAS 9.4 program (SAS Institute, USA) was used to predict and to determine the effects of inlet concentration (C_i), pulse interval (P_i) and pressure (P_p), filtration velocity (V_f), presence or absence of venturi, etc. The results are shown below. The variation in pressure drop with or without venturi installation was 38.8 mmAq when venturi is installed and 47.6 mmAq when venturi is not installed, indicating a difference in pressure drop of 8.8 mmAq depending on venturi installation. It is estimated that the efficiency can be improved by about 18.5% if the venturi is installed.

• 한국입자에어로졸학회지
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• 제12권3호
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• pp.95-102
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• 2016

본 연구에서는 호흡용 보호구 필터의 나노물질에 대한 여과특성을 측정하기 위해서 소금(NaCl)과 은나노입자(Ag)를 대상으로 입경별 집진효율을 평가하였다. 호흡용 보호구 필터는 특급 방진마스크와 1급 방진마스크의 두 가지 안면부 여과식 방진마스크인 사용하였고, 마스크의 배기밸브 부분을 제외한 필터 여재 부분을 직경 47 mm로 잘라내어 필터홀더에 부착하여 입경별 입자제거효율을 시험하였다. 시험입자는 일반적으로 시험 입자로 사용되는 소금입자는 분무형 입자발생장치를 사용하여 발생하였고 중화기를 통과시켜 입자의 하전특성을 볼츠만 분포로 만들어 공급하였다. 은나노입자의 경우, 기화-응축 방법을 이용한 금속나노입자 생성방법인 ISO10801 방법을 사용하였다. 작업장의 은나노입자의 고농도 노출을 모사하기 위해, 중화기를 통과하지 않은 나노입자를 시험입자로 사용하였다. 은나노입자의 경우 소금입자로 만들기 어려운 20nm 이하의 입자를 안정적으로 효과적으로 만들어 시험에 적용하였고, 나노 크기에서도 매우 안정적인 데이터를 확보할 수 있었다. 1급 마스크 필터와 특급 마스크 필터에 대한 소금입자의 평가에서, 입경별 최소효율이 30~50nm 사이에서 나타나는 특성은 기존 연구와 비슷한 결과를 얻었다. 반면, 은나노입자의 경우 1급 마스크 필터와 특급 마스크 필터 모두에서 비슷한 크기의 소금 입자와 비교할 때 높은 효율을 나타냈다. 이것은 소금 입자의 경우 중화기를 통과시켜 시험입자로 사 용한 반면, 은나노입자의 경우 중화기를 통과시키지 않았기 때문이다. 본 연구에서는 작업장에서 은나노 입자가 고농도로 노출될 경우를 모사하여, 기화-응축에 의한 방법의 은나노입자 발생장치를 사용하였는데, 이 때 상대적으로 높게 대전된 입자들이 많이 만들어진다(Jung et al., 2006). 이로 인해, 정전필터인 마스크 필터의 포집 효과가 상대적으로 크기 때문에, 입경별 효율이 높아진 것으로 생각된다. 본 연구에서 평가한 1급 및 특급 방진마스크 여재의 최소 포집효율은 유럽 EN 149 기준인 95 LPM 유량 기준을 만족하는 것으로 나타났지만, 이것은 여재에 대한 평가 결과로, 실제 마스크에 대해서는 여재의 구조적인 불균일성이나 마스크를 착용하는 과정에서 밀착이 되지 않아 누출될 가능성은 마스크 사용에 고려되어야 한다. 불시에 발생할 수 있는 작업장 내 안전사고의 예방을 위하여 적절한 보호구의 선택과 올바른 착용 및 유지관리가 필요할 것으로 생각된다.

• 대한환경공학회지
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• 제29권3호
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• pp.297-303
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• 2007

오리멀젼은 중유에 비해 황과 바나듐의 함유량은 높지만 경제성과 가채매장량이 우수하여 세계 여러나라에서 중유발전시설의 대체 에너지원으로 생각되고 있다. 국내 Y화력발전소에서 오리멀젼을 발전시설을 가동하고 있으나, 가시백연이 많이 발생하고 있다. 이를 해결하고자 가시백연을 저감하는 일반적인 방법인 MgO 주입법을 시도하였으나 공급라인의 플러깅과 같은 잦은 고장이 발생하여 효과적인 가시백연 저감을 이루지 못하고 있다. 이에 본 연구에서는 가시백연의 원인을 파악하여, 추후 지속연구를 통해 가시백연을 저감하는 방법을 제안하기 위한 기초자료로 활용하고자 하였다. 이를 위하여 공정 데이터를 검토하였고, 전기집진기(EP, Electrostatic Precipitator) 전단, 배연가스탈황장치(FGD, Fuel Gas Desulfurization) 전단, 굴뚝자료모니터링시스템(TMS, Telecommunications Management System) 전단에서 각각 미세입자를 실측하여 입도분포를 확인하였다. 이를 통해 wet-FGD 내의 $SO_3$로 인한 입자의 재성장이 가시백연을 유발한다는 것을 밝혔다.

• 한국환경과학회지
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• 제27권6호
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• pp.349-358
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• 2018

In this study, using coke dust from ironwork, the pulse pressure on a pulse air jet bag filter was investigated considering the influence of the pressure loss due to filtration velocity and pressure intervals. The research on the optimal pulse pressure prediction of a pulse air jet type bag filter using coke dust showed the following results. Pressure loss volatility produced by the pulse pressure under low dust concentration(0.5, $1g/m^3$) and low face velocity(1.25 m/min) was less than $10mmH_2O$. This suggests that the pulse pressure has a low impact on the pressure loss. In contrast, pressure loss volatility under high dust concentration($3g/m^3$) and high face velocity(1.75 m/min) was $25mmH_2O$. Therefore, pulse pressure with high dust concentration and high face velocity has a strong influence on the pressure loss volatility, compared to the condition of low dust concentration and low face velocity. The optimal pulse pressure of inlet dust concentration($0.5g/m^3$) was $6kg/cm^2$ under the same face velocity(1.75 m/min). As concentration increased from 1 to $2g/m^3$, the pulse pressure gradually reached $5kg/cm^2$ thus indicating that the pulse pressure($5kg/cm^2$) is pertinent at a high concentration($3g/m^3$). The pulse intervals: 20, 25 and 30 sec, which are relatively longer than 10 and 15 sec, corresponded to high pressure loss volatility produced by the pulse pressure. Furthermore, low pressure loss volatility was noted at $5kg/cm^2$ of the overall pulse pressure.

• 한국환경과학회지
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• 제16권4호
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• pp.449-458
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• 2007

Research results for the pressure drop variance depending on operation conditions such as change of inlet concentration, pulse interval, and face velocity, etc., in a pulse air jet-type bag filter show that while at $3kg/cm^2$ whose pulse pressure is low, it is good to make an pulse interval longer in order to form the first layer, it may not be applicable to industry because of a rapid increase in pressure. In addition, the change of inlet concentration contributes more to the increase of pressure drop than the pulse interval does. In order to reduce operation costs by minimizing filter drag of a filter bag at pulse pressure $5kg/cm^2$, the dust concentration should be minimized, and when the inlet dust loading is a lower concentration, the pulse interval in the operation should be less than 70 sec, but when inlet dust loading is a higher concentration, the pulse interval should be below 30 sec. In particular, in the case that inlet dust loading is a higher concentration, a high-pressure distribution is observed regardless of pulse pressure. This is because dust is accumulated continuously in the filter bag and makes it thicker as filtration time increases, and thus the pulse interval should be set to below 30 sec. If the equipment is operated at 1m/min of face velocity, while pressure drop is low, the bag filter becomes larger and thus, its economics are very low due to a large initial investment. Therefore, a face velocity of around 1.5 m/min is considered to be the optimal operation condition. At 1.5 m/min considered to be the most economical face velocity, if the pulse interval increases, since the amount of variation in filter drag is large, depending on the amount of inlet dust loading, the operation may be possible at a lower concentration when the pulse interval is 70 sec. However, for a higher concentration, either face velocity or pulse interval should be reduced.

• 한국환경과학회지
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• 제26권2호
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• pp.231-238
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• 2017

Rapid industrial development has led to a serious problem of pollution in the industrial sector. With the increasing social need for environmental protection, research on air pollution prevention equipment for reducing pollutants in industrial processes is actively being undertaken. The deterioration of existent, installed facilities, their increased emission rates, and the strengthening of the effluent quality standards make complying with permissible emission standards difficult. In fact, installing new electric precipitators or complementing existent facilities is inevitable. The expansion and complementation of the installed electrical precipitators have led to improvements in dust collection efficiency, shorter working times, and lower costs. Because of its easy installation and simple manufacturing process, the production method with the discharge electrode of an electric precipitator is widely used. The following conclusions were reached by classifying discharge electrodes into four types based on the production method and mutually comparing them by their dust collection efficiency. None of the four types used in this study were damaged by impact. However, we were able to confirm some strain from the compression sites of both type A and type B. Both type B and type C are expected to have greater dust collection efficiencies than the other models due to their large vibration transmissibility. Moreover, the high vibrational energy is expected to cause rapping damage during its operation. Particularly, in the case of type B, some of the strain was found at the end of the compression site. The coupling schemes of both type C and type D are out of vibration transmissibility. On the other hand, the ability to maintain straightness and solidity of the side is regarded as outstanding and stable. Type D has outstanding on-site workability, considering the presence of locking, structural stability, and work conditions. From these experiments, we determined that type C is the most ideal connection method of discharge electrode, considering its construction period of renovation. Type C is inferior to type D with regard to on-site workability. However, type C has outstanding dedusting transmission with regard to the straightness, solidity maintenance, and vibration of shearing stress.

• 한국구조물진단유지관리공학회 논문집
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• 제24권2호
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• pp.9-14
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• 2020

필터가 장착 된 먼지 감소 팬을 포함하여 새로운 유형의 Composite Cyclone Scrubber를 개발하고, 목표 설치 및 유지 보수 비용에 대해서는 기존 도로 오염 저감 시스템 대비 64 %의 투자비 절감 (61 억 원 vs. 170 억 원), 기존 도로 오염 저감 조치 (72.6 억 원) 대비 사회적 비용편익이 43 % 증가, 50.8 억 원)가 예측되고 있다. 장치의 구성은 송풍기 형 나선형 가이드 베인이며, 분사 압력은 미세먼지를 포집한다. 분사 각도 및 접촉 범위가 다양한 노즐, 스프레이 액체 등과 순환 수를 이용한 스프레이이며, 분사 된 물이 Guide Vane과 45도 각도로 충돌로 인해 오염된 가스를 만나기 때문에 41.4 % 더 많은 미세 먼지를 포집한다. 이는 기존의 집진기보다 141 % 증가한 것이다. 포집 액체, 순환 빗물 및 우물 공급원과 관련하여 우리는 특허에서 막대한 양의 에너지와 경제적으로 절약되는 친환경 시스템을 기대한다. 가이드 베인 및 금속 필터는 90 % 이상의 미세 먼지를 줄였으며, 분무 된 물은 베인과 필터를 청소하여 유지 관리 예산을 최소화했다. 개발 된 설계의 예비 평가를 통해 특징적인 물분사로 인하여 유지 보수 예산을 줄일 수 있다.

• 공업화학
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• 제33권6호
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• pp.613-617
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• 2022

미세먼지 다량배출사업장의 미세먼지를 제거하는 백하우스의 백필터 여과체를 제작하기 위한 대면적 PTFE 나노섬유 제조 장치를 설계하여 제작하였다. 상용 PTFE 폼 필터의 미세먼지 여과효율을 높이기 위해 전기방사 공정과 열처리 공정을 이용하여 PTFE 나노섬유를 코팅하였다. PTFE 나노섬유를 대면적의 PTFE 폼 필터 표면에 연속적으로 코팅하기 위하여 roll-to-roll 공정용 장비와 제조 공정을 제안하였다. PTFE 나노섬유를 연속적으로 제작하기 위해 전기방사부와 열처리부를 roll-to-roll 공정에 맞게 장비를 최적화하여 설계하고 제작하였다. 본 장비를 이용하여 대면적 필터 여과체를 제조하고, 제조된 여과체의 표면 형태, 조성, 필터 특성을 확인하였다. 롤 형태의 대면적 여과체 전반에 걸쳐 PTFE 나노섬유가 균일하게 코팅되었고, 본 여과체는 280 ℃에서도 280 ℃에서도 PM_2.5 기준 91.79%의 높은 집진효율과 1 m/min 기준 62 Pa의 우수한 압력 손실 특성을 보였다.

• 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.