• Clean Technology
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• v.10 no.2
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• pp.89-100
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• 2004

The optimization for the water bath design and the skimmer installation are conducted to separate floated-sludge from the waste water in a water bath of a painting booth. VOF(volume of fluid) model is used to analyze the flow pattern of sludge-water-air mixture in a water bath. From the results of numerical analysis, the design criteria of the skimmer, the separation plate and the sludge inlet port of a water bath are obtained for effective sludge separation from water in bath. Furthermore, the installation condition of the skimmer immersed in water is optimized to minimize entrained air and pressure loss.

• The KSFM Journal of Fluid Machinery
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• v.8 no.1 s.28
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• pp.30-36
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• 2005

A sludge treatment system for introducing the waste water mixture with paint sludge from the water bath of paint booth and for recycling cleaned water to paint booth after sludge separation is developed. Floated sludge is introduced from the water surface in the bath by using floating-skimmer, and is conveyed by pump to the centrifugal separator where sludge and cleaned water are separated. From the operation results of the present sludge treatment systems applied in actual paint booths, paint sludge can be separated automatically and effectively from water bath with its water content of $60-70\%$, and sludge-free clean water is returned to paint booth.

• 유체기계공업학회:학술대회논문집
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• 2004.12a
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• pp.259-266
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• 2004

Developed is a sludge treatment system for introducing the waste water mixture with paint sludge from the water bath of paint booth and for recycling cleaned water to paint booth after sludge separation. Floated sludge is introduced from the water surface in the bath by using floating skimmer, and is conveyed by pump to the centrifugal separator where sludge and cleaned water are separated. From the operation results of the present sludge treatment systems applied in actual paint booths, paint sludge can be separated automatically and effectively from water bath with its water content of $60-70\%$, and sludge-free clean water is returned to paint booth.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2003.11b
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• pp.179-180
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• 2003

자동차 도장 작업 시 배출되는 대표적인 용매물질인 부틸아세테이트, n-부탄올 및 톨루엔을 대상기체로 하여 활성탄에 의한 흡착 특성을 연구결과는 다음과 같았다. 처리대상가스의 유입농도가 증가할수록 파과시간은 점점 감소하였으며. 파과곡선의 기울기 또한 급격해졌다. 유량이 증가할수록 파과시간은 감소하였다.

• Congress of the korean instutite of fire investigation
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• 2010.12a
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• pp.147-171
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• 2010

도장작업은 기계 기구, 금속, 자동차, 전기 전자, 선박, 가구제조업 등 각종 사업장에서 많이 취급되고 있는 작업으로서 취급물질이 대부분 합성수지 유기용매 등 인화성 또는 가연성 액체이거나 가연성 분체로서 용매 또는 분진으로 인한 폭발 화재의 위험성이 아주 높은 실정이다. 보통 4류 위험물의 유증기는 공기보다 무겁다 라는 생각으로 발생된 모든 유증기는 위험물 인근에 체류할 것이라는 생각을 하지만 상온에서 증발한 유증기 대부분은 인근의 대기와의 밀도차에 의해 주변으로 흩어지거나 연소하고 중량(重量)의 유증기만이 남아 화재조사에서 중요한 단서로 역할을 한다. 대부분분의 페인트 제품이 가열과 동시에 끊기 시작해서 비등점 측정이 어려웠고 발화점이 비슷한 다른 페인트에 비해 중량(重量)유증기 발생이 단시간 동안 낮은 온도에서 많이 발생한 것은 페인트의 안료가 유증기 발생을 방해해서 시너의 유증기 발생량과 동일한 양의 페인트 유증기 발생시간이 더 걸린 것 같다. 대부분의 유증기는 집진시설을 통해 A/C타워의 활성탄에 흡착되어 제거된다. 하지만 슬러지에 남아있는 희석제는 A/C타워를 정지하고 집진시설등의 배관에 있는 슬러지 청소 과정에서 주위 열원에 의해 많은 유증기를 발생하여 화재의 위험성이 존재함으로 작업자의 각별한 주의가 필요하다.

• Journal of Korean Society for Atmospheric Environment
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• v.31 no.1
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• pp.54-62
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• 2015

Small scale paint overspray booths are being operated nationwidely, for repair of passenger car body parts. paint aerosols are emitted from the paint overspray booth in operations. In paint overspray booth operations without ventilation system and air pollutants collection unit, it may land on nearby equipment. In this study a removal of sticky paint aerosol for application of the small-scale overspray paint booth. it's cause the surface of filter bag from generated sticky paint aerosol. To remove adhesion of paint aerosol the agglomerating agents are injected and mixed with sticky paint aerosols prior to reach the filter bag. The paint spray rate was set as $10{\pm}5g/min$ from air-atomized spray guns in the spray booth, injection rate of agglomerating was $10{\pm}5g/min$ in the mixing chamber. The filtration velocity including air pollutants varied from 0.2 m/min to 0.4 m/min. Bag cleaning air pressure was set as $5.0kg_f/min$ for detaching dust cake from surface of filter bag. Bag cleaning interval at the filtration velocity of 0.2 m/min was around 3 times longer than that of the 0.4 m/min. The residual pressure drop maintained highest value at the highest filtration velocity. Fractional efficiency of 99.952%~99.971% was possible to maintain for the particle size of 2.5 microns. Total collection efficiency at the filtration velocity of 0.2 m/min was 99.42%. During this study we could confirm high collection efficiency and long cleaning intervals for the test with filtration velocity of 0.2 m/min indicating an optimal value for the given dimensions of the test unit and test operating conditions.