• Korean Chemical Engineering Research
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• 제62권1호
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• pp.87-98
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• 2024

본 연구는 리그노셀룰로오스 섬유와 굴참나무 수피-기반 활성탄(COA)으로 제조한 3층 섬유판에 한지를 조합하여 제작한 섬유판 필터세트의 미세먼지(PM), 휘발성 유기화합물(TVOC), 폼알데하이드(HCHO) 여과능을 조사하기 위하여 수행하였다. 단백질계 접착제를 적용하여 표층에 목섬유 그리고 심층에 재생섬유/COA로 제조한 섬유판(WRF)과 한지로 제작한 섬유판 필터세트는 일반향의 연소에 의하여 발생하는 상기 오염물질을 효과적으로 여과하였다. 섬유판 제조에 있어 표층/심층에 적용되는 접착제의 함지율을 4%/4%, 5%/3%, 6%/2%로 조절하여 WRF를 제조한 후, 이를 한지와 함께 WRF-기반 필터세트 제작에 이용하였다. 이 필터세트의 PM, TVOC, HCHO 여과능은 심층의 함지율이 감소함에 따라 향상되었다. 한편 WRF-기반 필터세트 구성에 있어 45 g/m² 평량의 한지보다 25 g/m² 평량의 한지(KP-25g)를 사용하여 제작한 필터세트에서 여과능이 우수하였다. 표층에 재생섬유와 심층에 목섬유/COA로 제조한 섬유판(RWF)과 KP-25g로 구성한 섬유판 필터세트의 여과능은 WRF와 비교하여 높았다. 소형 실내공간 및 대형 옥외공간에 WRF-기반 섬유판 필터세트 및 무필터 조건과 함께 측정한 PM 및 TVOC 여과능은 RWF-기반 섬유판 필터세트에서 높았다. 따라서 RWF와 KP-25g를 조합하여 제작한 섬유판 필터세트가 실내외 공간에 존재하는 PM, TVOC 여과용 필터로서 적용이 가능할 것으로 생각한다.

• 한국산학기술학회논문지
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• 제19권2호
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• pp.56-63
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• 2018

강우사상이 발생함에 따라 시설용량을 초과하여 미처리된 상태로 방류수계에 직접 배출되는 합류식 관거 월류수(Combimed Sewer Overflows, CSOs) 및 분류식 관거 월류수(Separated Sewer Overflows, SSOs)의 관리는 집중호우가 잦아지는 근래에 들어 그 관리가 더욱 중요해지고 있다. 밀집도가 높은 도심지에 적용성이 유리한 여과기술은 지속적인 개발이 이루어지고 있음에도 불구하고 CSOs에 적용된 사례가 거의 전무한 실정이다. 따라서 본 연구에서는 로프형 섬유여재가 적용된 Pilot 규모의 수평흐름식 여과장치를 CSOs에 적용하기 위해 공정최적화를 목적으로 수행되었다. 연구방법은 인공시료를 적용한 사전연구와 하수를 적용한 현장연구로 구분하여 수행하였다. 인공시료를 적용한 사전연구에서 여재 자체의 손실수두는 약 1.1cm정도로 분석되었고, 선속도 10m/hr 증가에 따라 약 0.1cm 정도의 손실수두 증가를 유발하는 것으로 나타났다. 또한, SS 제거효율은 81.4% 정도로 안정적이었고, 여과지속시간은 6시간 이상 유지되었으며, 공기역세척만으로도 98% 정도의 손실수두 평균 회복율을 보였다. 하수를 적용한 현장평가에서는 여재의 조기폐색을 방지하기 위한 전처리공정으로 벨트 형 미세스크린(450mesh 이상)를 적용했을 때 2시간 내외의 여과지속시간을 확보할 수 있었고, 평균 83.9%의 SS 제거효율을 나타내었다. CSOs 및 SSOs에 여과공정 적용을 위해서는 효율적 측면보다 여과지속시간의 안정적 유지를 위한 수리적 측면을 보완하기 위해서 전처리공정과의 조합이 중요하다는 결론을 얻을 수 있었다. 건기와 비교하여 우기의 유입하수 수질은 다소 낮은 보였으며, 이는 분류식 관거 비율이 높은 배수구역의 특성 때문인 것으로 추정된다. 또한, 우기와 건기의 유입수질에 따른 제거효율 차이는 미미하였다.

• Membrane and Water Treatment
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• 제8권5호
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• pp.499-515
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• 2017

The purpose of this study was to investigate membrane fouling caused by microalgal cells in submerged membrane systems consisting of polymeric and ceramic microfiltration membranes. In this study, one polymeric (flat-sheet, pore size: $0.2{\mu}m$) and two ceramic (flat-sheet, pore size: $0.2{\mu}m$ and cylindrical, pore size: $1{\mu}m$) membranes were used. Physical cleaning was performed with water and air to determine the potential for reversible and irreversible membrane fouling. The study results showed that substantial irreversible membrane fouling (after four filtration cycles, irreversible fouling degree 27% (cleaning with water) and 38% (cleaning with air)) occurs in the polymeric membrane. In cleaning studies performed using water and air on ceramic membranes, it was observed that compressed air was more effective (recovery rate: 87-91%) for membrane cleaning. The harvesting performance of the membranes was examined through critical flux experiments. The critical flux values for polymeric membrane with a pore size of $0.20{\mu}m$ and ceramic membranes with a pore size of $0.20{\mu}m$ and $1{\mu}m$ were ${\leq}95L/m^2hour$, ${\leq}70L/m^2hour$ and ${\leq}55L/m^2hour$, respectively. It was determined that critical flux varies depending on the membrane material and the pore size. To obtain more information on membrane fouling caused by microalgal cells, the characterization of the fouled polymeric membrane was performed. This study concluded that ceramic membranes with a pore size of $0.2-1{\mu}m$ in the submerged membrane system could be efficiently used for microalgae harvesting by cleaning the membrane with compressed air at regular intervals.

• 한국대기환경학회지
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• 제29권5호
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• pp.625-633
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• 2013

This study attempted to find an alternative method for fine dust control in the pre-exiting facilities of metro-subway stations. A new double-layer design was proposed for the MVAC (mechanical ventilation and air control) system. Several filter lay-outs were combined a pre-filter with electret filter (EF), electret bundle filter (EBF), or electret pleated filter (EPF), and were then examined focusing on the collection efficiency of particulate matters and pressure drop across the filter layers. The experimental results from the lab and field tests showed the best collection efficiency with EPF, which achieved 85% for $PM_{10}$ and 55% for $PM_{2.5}$. It was also found from the long term field test that the new filter lay-out could provide quite consistent dust level particularly in underground platform regardless of external condition.

• 멤브레인
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• 제1권1호
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• pp.78-95
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• 1991

미국 캘리포니아주 Orange County에 위치한 Water Factory 21(WF-21)은 생물학적 처리공정을 거친 도시하수를 재생하여, 이 재생수를 지하수지층으로 유입되는 해수의 침투를 막기 위한 Reinjection System에 이용하고 있다. 장치 구성 공정은 Lime처리, Air Stripping, 사여과, 활성탄처리, 역삼투막 및 염소처리 등으로 이루어지며, 이에 대한 각 처리공정의 효율성에 대하여 실험을 실시하였다. 3년간의 장기간에 걸친 실험결과로부터, 도시하수에 대한 RO Membrane 처리수는 음료 수질 기준에 적합한 고수질의 물을 생성할 수 있음을 입증했다. Pilot Plant 실험에선 Lime Clarifier만으로 전처리를 실시하여 성공적인 결과를 얻었으며, 또한 저압 (250 psi)이 적용된 새로운 Membrane을 사용하여 에너지 절약을 통한 비용 절감 효과에 대한 실험도 상당한 가능성을 보여주었다.

• 한국환경과학회지
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• 제20권1호
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• pp.25-34
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• 2011

The new empirical static model was constructed on the basis of dimension analysis to predict the pressure drop according to the operating conditions. The empirical static model consists of the initial pressure drop term (${\Delta}P_{initial}$) and the dust mass number term($N_{dust}=\frac{{\omega}_0{\nu}_f}{P_{pulse}t}$), and two parameters (dust deposit resistance and exponent of dust mass number) have been estimated from experimental data. The optimum injection distance was identified in the 64 experimental data at the fixed filtration velocity and pulse pressure. The dust deposit resistance ($K_d$), one of the empirical static model parameters got the minimum value at d=0.11m, at which the total pressure drop was minimized. The exponent of dust mass number was interpreted as the elasticity of pressure drop to the dust mass number. The elasticity of the unimodal behavior had also a maximum value at d=0.11m, at which the pressure drop increased most rapidly with the dust mass number. Additionally, the correlation coefficient for the new empirical static model was 0.914.

• 한국물환경학회지
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• 제30권5호
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• pp.532-538
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• 2014

A cylinder-shaped filter was developed to manage the runoff from construction sites. Compressed air was used for back-washing and pore sizes of filter were $23{\mu}m$ and $46{\mu}m$. The turbid water was prepared using sediments in construction sites. The grain size analysis showed that grains smaller than $38{\mu}m$ and larger than $335{\mu}m$ in size constituted 34.4 % and 37.6 %, respectively. Removal efficiency of the filter on turbidity, SS, COD, TN and TP showed 25~37%, 20~40%, 50~55%, 23~27% and 14~20%, respectively, whereas their removal efficiecy by using coagulant PAC showed 77~84%, 70~83%, 53~60%, 27~36%, and 59~75%, respectively. The filtration time was determined to be around 10 to 20 minutes. Back-washing for 10 seconds by pressurized air resulted in a satisfactory regeneration efficiency. According to the aforementioned test results, the cylinder-shaped filter is effective in reducing turbidity and would be suitable for practical application in construction sites and farms.

• 상하수도학회지
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• 제18권2호
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• pp.191-200
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• 2004

DAF process has been designed considering raw water quality characteristics in Korea. Although direct filtration is usually operated, DAF is operated when the freshwater blooms occut or raw water turbidity become high. Pre-sedimentation iS prepared in case when raw water turbidity is very high by rainstorms. A main feature of this plant is that the operation mode can be changed (controlled) based on the characteristics of raw water to optimize the effluent quality and the operation costs. Treatment capacity (surface loading rate) and efficiency of DAF was found to be better than conventional sedimentation process. Moreover, low-density particles (algae and alum flocs) are easily separated while it is difficult to remove in sedimentation. One of the main concerns in adoption of DAF (Dissolved Air-Flotation) process is a high raw water turbidity problem. That is, DAF is not adequate for raw water, which is more turbid than 100NTU. In order to avoid this problem, pre-sedimentation basins are prepared in DAF plant to decrease the turbidity of DAF influent. For simulation of the actual operation, bench and full-scale tests were performed for highly turbid water conditions. Consequently, DAF process coupled with sedimentation is suggested that pre-sedimentation with optimum coagulation prior to DAF would be appropriate.

• 상하수도학회지
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• 제20권2호
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• pp.289-294
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• 2006

A pilot scale non-woven fabric filter separation activated sludge system was investigated for practical application on domestic wastewater reclamation and reuse. The system was operated in A/O (Anaerobic/Oxic) process with submerged filter module in the aerobic compartment. In the test of two types of filter materials ($70g/m^2$ and $35g/m^2$), the initial flux (0.42m/d) could be maintained for about three months by regular air backwashing of $70g/m^2$ filter at 0.3m water head. The removal efficiency of organic matter by the system was BOD 93.3%, CODcr 96.3%, SS 96.7%. The effluent quality was 7.8mg/L, 12mg/L and 5mg/L for BOD, CODcr and SS, respectively. The water quality was enough to meet a standard for domestic reuse without human contact. T-N removal efficiency was 49.9% at internal recycle rate 2Q and C/N ratio 3.3. The removal efficiency of T-P was 50% with average effluent concentration, 2.6mg/L.

• 한국환경보건학회지
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• 제14권2호
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• pp.1-12
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• 1988

Airborne dust and asbestos fiber concentrations were determined in subway stations located in Seoul area. Two stations, such as Eulchiro 4-Ka Station of Line #2, constructed during a period of 1980-1984 and Hyehwa Station of Line #4, opened in 1985, were selected. The results of the study are as follows. 1. Daily time-weighted average (TWA) concentrations of airborne dusts from 07:00 to 20:00 hours in Line #2 and Line #4 were 0.43$\pm$0.08 mg/m$^3$ and 0.37$\pm$0.12 mg/m$^3$, respectively. Thus, the dust levels in Line #2 were significantly higher than the levels in Line #4 (p < 0.05). 2. Dust levels in the morning (07:00-11:00 hours), noon (11:00-16:00 hours) and in the evening (16:00-20:00 hours) in Line #2 were 0.47$\pm$0.17 mg/m$^3$, 0.37$\pm$0.08 mg/m$^3$, and 0.46$\pm$0.07 mg/m$^3$ respectively. Thus, dust levels in the morning and evening (i.e., during rush hours) were significantly higher than levels in the noon (p < 0.02). However, there was no such difference in dust levels by time in Line #4. 3. Airborne total dust concentrations were well below the occupational health standard of 10 mg/m$^3$, however, the levels were exceeding the ambient air standard recommended by the Korean Environment Administration. 4. All of airborne asbestos fiber concentrations were equal to or below 0.005 fibers/cc. The levels are within both occupational health standards and U.S. EPA criteria. 5. A consideration should be given to the improvements of cleaning methods (such as use of vacuum cleaning instead of brushing) and the existing ventilation (such as more air change and filtration of supply air) for a reduction of dust levels. 6. It is recommended that routine monitoring of airborne dusts and asbestos fibers be conducted because more dusts and asbestos fibers can be produced in the air due to the deterioration of facilities by age and water damage in future.