• Journal of Korean Society of Environmental Engineers
• /
• v.28 no.2
• /
• pp.216-222
• /
• 2006

A flexile fiber filter developed in Korea was operated to evaluate the effect of packing density and filtration velocity on particle removal. The pilot-scale fiber filter with 40 cm of diameter and 2 m of height was packed with polyamide fibers of which mean diameter was approximately 0.93 mm. While the filtration velocity was maintained at 325 m/hr, the particle removal efficiency was compared with various of packing density from $70kg/m^3\;to\;100kg/m^3$. On the contrary, when the packing density was maintained at $70kg/m^3$, the particle removal efficiency was examined with various filtration velocity from 65 m/hr to 400 m/hr. The filtration pressure increased with the packing-density increase. Below $80kg/m^3$ of packing density, the removal efficiencies of turbidity ad SS were less than 30% and 50%, respectively. At $100kg/m^3$ of packing density, the removal efficiencies of them were nearly 45% and 60% respectively. The filtration pressure increased with the filtration-velocity increase. A better removal efficiency was obtained at a lower filtration velocity, removal efficiency of them were 73% at 65 m/hr. Consequently, The filtration velocity was the more important factor to enhance the particle removal efficiency compared with the packing density in fiber filter.

• Proceedings of the Korean Environmental Sciences Society Conference
• /
• 2003.05a
• /
• pp.81-82
• /
• 2003

육상수조식 양식장 수처리를 위한 순환여과 시스템으로서의 유연성 섬유사 필터 모듈의 적용성을 평가하기 위하여, 여과기의 운전주기에 따른 처리성능의 변화 추이 및 넙치사육조의 급이주기에 따른 여과성능의 변화를 검토한 결과, 유기물 농도의 경우 20~70%의 제거육을 보였으며, 탁도는 평균 50% 이상의 제거율을 보여주었다.

• Journal of Korean Society of Water and Wastewater
• /
• v.24 no.2
• /
• pp.231-236
• /
• 2010

A compressible media filtration process with synthetic fiber media was studied for combined sewer overflows (CSOs) treatment. Since the operation performance of fiber media filtration was dependent on the pattern of CSOs, the flow rate of CSOs was investigated and it was characterized by a big fluctuation. Thus, in this study, the fiber media filtration process was tested with wide range of filtration velocity. The removal efficiency was proportion to the increase in compressibility. As the filtration velocity was increased, the treatment efficiency was decreased and consequently leveled off when the velocity exceeded 750 $m^3/m^2$/d. An exponential equation was introduced to express the relationship between the removal efficiency and up-flow velocity. At columm test, six repetition of filtration and backwash cycle did not after the filtering velocity under the constant pressure condition.

• Bulletin of Korea Environmental Preservation Association
• /
• v.27 s.355
• /
• pp.53-58
• /
• 2005

• Journal of Energy Engineering
• /
• v.7 no.1
• /
• pp.57-64
• /
• 1998

A neutralized fabric filter of which major raw materials were polyester and stainless steel fibers was developed and its physiochemical properties and basic filter characteristics were investigated. Four finds of dusts generated in the typical domestic industry were used, which were coke dust from a steel manufacturing process, cement dust from a cement manufacturing process, flu ash from a fluidized-bed combustor, and incinerator ash from a waste plastics incinerator. The physicochemical properties of the neutralized fabric filter were analyzed in terms of changes in tensile strength and initial elastic modulus under $SO_2$ and $NO_2$ atmospheres, mean flow pore pressure, bubble point pore diameter, mean flow pore diameter, and pore size distribution. In addition, the pressure drop, dust penetration, and figure of merit for the fabric filter were investigated in a bench-scale filter testing unit. The pressure drop increased as the filtration velocity and dust loading increased, and its increasing shape depended on the type of dust. The dust penetration rapidly decreased as the dust loading increased irrespective of the type of dust. The figures of merit for the fabric filters increased in the early stage of filtration and then showed rapid decreases followed maintaining a constant level.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1995.03a
• /
• pp.85-111
• /
• 1995

P84 Fiber란 오스트리아 Lenzing 사에서 개발한 내열성 및 내화학성이 아주 뛰어난 Aromatic polyimide섬유로서, 향후 Filter bag 산업을 이끌어 나갈 첨단 Filter 소재이다.

• Membrane Journal
• /
• v.19 no.2
• /
• pp.165-171
• /
• 2009

This study was for the evaluation of adaptability of the fiber filter as the pre-treatment of the RO membrane through SDI (Silt Density Index) measurement. The turbidity of raw waters were $0.76{\sim}1.6$ NTU for the effluent of sewer treatment plants (STP) and $2.2{\sim}3.3$ NTU for sea waters and 100 NTU for the surface water. The turbidity of the $2^{nd}$ filtrate of the serially connected two fiber filters was $0.07{\sim}0.25$ NTU and $SDI_{15}$ was $1.4{\sim}2.8$ when the 17% PAC was dosed $10{\sim}30ppm$. Results of the turbidity and $SDI_{15}$ of the $2^{nd}$ filtrate of the fiber filter which were compared with them of the lab scale MF/UF disc filter for the same STP's effluents showed that filtrate quality were enhanced with a little on the order of two stage fiber filter>MF>UF, the difference in $SDI_{15}$ was only $0.7{\sim}1.0$. So, the filtrate of the serially connected two stage fiber filter could satisfy $SDI_{15}$ 5.0 safely which was normally required for the feed water by the RO membrane supplier and it means the serially connected two stage fiber filter could be applied as the pre-treatment process of the RO membrane.

• Proceedings of the Korean Fiber Society Conference
• /
• 2003.10b
• /
• pp.185-186
• /
• 2003

막을 이용한 분리기술은 다양한 종류의 혼합물에서 원하는 물질을 분리 정제하는 기술로 여기에는 고-액, 액-액, 기-액분리가 모두 포함된다 현재까지 분리공정은 주로 여과, 증류, 추출, 흡착등 방법이 있으나 에너지소비가 많고, 설비투자비가 많이 들며 효율이 낮아 비경제적이라는 문제점을 가지고 있고 이와 같은 문제점을 해결하기 위하여 최근 주목받고 있는 기술이 막을 이용한 분리기술이다. 막을 이용한 분리기술의 장점은 앞서 언급한 바와 같이 에너지소비와 설비비를 최소화하면서도 고효율의 분리효과를 얻을 수 있다는 점에 있다. (중략)

• Journal of Korean Society of Water and Wastewater
• /
• v.33 no.6
• /
• pp.437-446
• /
• 2019

Reverse osmosis seawater desalination facilities can extend the cleaning cycle and replacement time of the reverse osmosis membrane by pretreatment process. Selection of pretreatment process depends on water quality. It was attempted in this study to select approriate pretreatment process for the Masan bay, which was high in particles and organic content. For this purpose, performances of pretreatment processes such as filter adsorber (FA), pore controllable fiber (PCF), and ultrafiltration (UF) were compared based on the silt density index (SDI). The SDI value of the filtrate should be less than 3. The study results showed that UF can produce the filtrate quality satisfying the requirement. However, the transmembrane pressure (TMP) of UF increased quickly, reaching 0.6 bar within 4 days. In order to secure stable operation, FA and PCF were combined with UF. The study results showed that combination of PCF and UF was able to extend the filtration duration (more than 2 months) until to reach TMP of 0.6 bar.

• Proceedings of the Korean Society of Coastal and Ocean Engineers Conference
• /
• 2002.08a
• /
• pp.144-147
• /
• 2002

오탁방지막은 해상이나 하천에서 준설 및 매립공사등으로 인한 부유사 확산을 방지하는 막체구조로서 부력이 우수한 Polystyrene계로 원통형 부체를 이루는 부체부, 고장력 합성섬유를 사용하여 외력에 대하여 저항하고 여과기능이 있는 막체부,그리고 막체부의 이동을 막기 위해 해저면에 고정시키는 계류라인(Mooring Line) 및 블록(Anchor Block)부로 이루어져 있다 특히 계류라인은 와이어로프 또는 체인 등으로 부체부와 앵커블럭을 연결시켜 주는 역할을 한다. (중략)