• Proceedings of the Korea Air Pollution Research Association Conference
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• 2003.05b
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• pp.405-406
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• 2003

분진여과시 형성되는 분진 케이크는 궁극적인 여과 성능을 좌우하며, 필터의 구조, 분진 입자의 형태나 크기, 분진농도, 여과속도 등에 의해 영향을 받는다 특히 필터의 표면 구조나 기공 크기는 여과 초기 단계의 케이크 층의 구조를 결정하며, 연속적인 여과시 초기 케이크 층은 다음에 쌓이는 케이크 형성과 비저항에 영향을 주므로 필터 medium 구조 또한 분진여과 과정에서 중요한 영향 요인이 된다. 본 연구에서는 필터 medium의 구조가 서로 다른 고온가스정화용 복합 세라믹 필터, metal fiber mat, 스테인레스 필터를 이용하여 분진농도와 여과속도를 변수로 하여 분진 여과 실험을 함으로써 각각의 필터에 대한 케이크 비저항과 기공율을 실험과 이론식으로부터 추정하였다. (중략)

• Journal of Korean Society of Environmental Engineers
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• v.29 no.1
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• pp.74-81
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• 2007

Using the new experimental method named "filtration-permeation", the average specific resistances which plays an important role in designing cake filtration apparatus and the development of cake filtration theory were measured in this study. By this new experimental method, two kinds of average specific resistances are measured. The one from the filtration is named 'filtration average specific resistance $\alpha_{avf}$, and the other from the permeation of particle eliminated water through the pre-formed cake is named 'permeation average specific resistance $\alpha_{avf}$. The "filtration-permeation" method is applied to three different kind of suspensions(i.e. particulate suspension, pre-flocculated suspension and macro-molecule suspension) to obtain filtration and permeation average specific resistances. A theoretical procedure of cake filtration is studied based on the values of permeation average specific resistance. With the study it was concluded that the influence of the sedimentation during particlulate filtration operation could not be ignored as commonly used. And the solid content of suspension, S, which also regarded usually as constant, changes during filtration of particles. It is also verified that the exact value of solid content of cake for floe filtration could not be obtained. These significant problems are all solved by our new "filtration-permeation" experimental method.

• Journal of the Korean Society of Food Science and Nutrition
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• v.30 no.4
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• pp.623-629
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• 2001

This study was investigated the quality characteristics of sponge cakes which were prepared b replacing 30% of flour with raw starch and resistant starches, such as, 4 cycled autoclaved-cooled RS 3 maize starch(RS 3), cross-linked RS 4 maize starch (RS 4) was superior to control cake( 100% flour cake). Addition of starches except RS 3 made crust and crumb color lighter and decreased hardness. Especially, cake containing RS 4 had the softest texture. For the adhesiveness and cohesiveness, cake containing RS 4 showed the least changes during 5 storage days. In DSC measurement, cakes containing RS 4 and ARS 4 showed high enthalpy in despite of low hardness. Sensory evaluation showed that cakes containing RS 4 and ARS 4 were significantly moist and soft compared to others. Overall acceptability of cakes containing starch, RS 4 and ARS 4 were evaluated excellent. Therefore, it can be suggested that RS 4 and ARS 4 can be added to the sponge cake for the quality improvement and functional element.

• Korean Chemical Engineering Research
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• v.50 no.2
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• pp.317-327
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• 2012

The average specific cake resistance, the most important indicator for cake filtration and solid-liquid separation, is measured by filtration experiment. But the exact value is difficult to measure because of the other influences such as sedimentation during filtration. This study, a little more stable method named filtration-permeation is proposed for measuring average specific cake resistance. The filtration-permeation is composed of permeation of particle eliminated water through pre-formed cake by filtration. Using 1 wt% calcium carbonate suspension, the filtration-permeation experiments were performed for 8 kinds of filter media at the conditions of 0.5 atm and 0.2 atm, 1 and 3 sheets of filter media. At each specific condition, three to five times filtration-permeation were accomplished. As a result, stable permeation speed is measured. According to this experimental result, the characteristics of permeation and the effect of sedimentation are analyzed with Ruth's equation. The one way analysis of variance (one way ANOVA) is applied to the average specific cake resistances of filtration and permeation obtained with the selected three kinds of filter media. The average specific cake resistances between 0.5 atm and 0.2 atm by filtration do not distinguished, but those by permeation is perfectly distinguished. The experimental results during permeation have a very narrow distribution than that measured during filtration. The analysis of filtration experiments, it was verified that the resistance of filter medium by traditional method is of no significance. Finally, the migration of small particles through the medium composed of fiber glass at low pressure was studied.

• Korean Chemical Engineering Research
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• v.50 no.3
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• pp.535-544
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• 2012

Filtration on horizontal filter medium facing upward is accompanied by sedimentation. When sedimentation phenomenon is not considered, the average specific cake resistance by filtration could be in error more than two times. In the previous paper on this subject, it was insisted that the solid mass fraction of suspension changes in filtration period by sedimentation. But we could not find out the degree of change. At the first half of this paper, the average specific cake resistance measured by permeation will be proved to be exact in several means. The average specific cake resistance conventionally measured by filtration does not give correct results because it uses initial solid mass fraction of suspension. Then we calculated the changed solid mass fraction of suspension due to sedimentation during filtration by the experimental values obtained "filtration-permeation" method. We also determined the solid mass fraction at a certain moment of filtration from the suspension height and a new equation derived in this study. The two results were compared and proven that they almost matched.

• Journal of Korean Society of Environmental Engineers
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• v.30 no.2
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• pp.161-167
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• 2008

Using an experimental method named filtration-permeation, the influence of sedimentation during filtration was studied for the suspensions composed of particles and that of flocs. The average specific cake resistances measured by filtration do not give accurate values because of the sedimentations during filtration, but the permeation data give quite accurate values. The prolonged permeation rates for the cake formed from particulate suspension do not change, but that rate from the floc filtration changes by the sweeping of flocculant. It is proposed that the cake compressibility can be measured with one set of filtration-permeation experiment by step increase of pressure during permeation period. The another experimental method which can shorten experimental time for floc filtration using filtrationpermeation is also proposed.

• Proceedings of the KIEE Conference
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• summer
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• pp.773-775
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• 2004

최근 높은 임계전류를 지닌 고온초전도선재를 이용한 초전도 전력기기의 개발이 활발히 이루어지고 있다. 고온초전도선재의 임계전류는 자장에 대한 의존성을 지니고 있으며 이로 인해 고온초전도선재가 코일의 형태로써 초전도 전력기기의 개발에 이용되는 경우, 권선 방식에 따라 다른 전기적 특성을 지니게 된다. 이러한 특성은 초전도선재의 전력기기의 효율에 큰 영향을 미치므로 권선 방식에 따른 코일의 특성을 연구하는 것은 초전도선재를 이용한 전력기기의 효율을 높이는데 있어서 중요한 의미를 갖는다. 본 논문에서는 권선 방식에 따른 코일의 특성을 비교하기 위해 동일한 턴 수와 사용 선재길이를 가진 팬케이크 코일과 솔레노이드 코일을 설계, 제작하고 두 코일의 임계전류를 측정하였다. 또한 인가전류에 대한 두 코일의 전압, 저항특성과 교류손실 특성을 측정하고 비교하였다. 측정결과, 두 코일의 임계전류는 솔레노이드 코일이 109A로 팬케이크 코일에 비해 약 $36\%$ 더 높았다. 코일에 가해준 인가전류가 증가함에 따라 코일에서 발생하는 전압 중 손실에 관련된 저항성 성분의 전압이 변화하고 있음을 확인하였다. 또한 교류손실은 인가 전류의 피크값이 팬케이크 코일의 임계전류 이하인 구간에서 팬케이크 코일이 솔레노이드 코일의 교류손실보다 9배 크며, 팬케이크와 솔레노이드의 임계전류 사이에서는 8.3배 컸다.

• Membrane Journal
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• v.8 no.3
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• pp.130-137
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• 1998

Membrane fouling characteristics in the membrane-coupled activated sludge system were investigated. The influence of the floc size variation on the filtration resistance was analyzed using resistance-in-series model and mixed liquor was fractionated into three components to verify which component would give rise to a major contribution to the total resistance. The microbial floc size was rapidly reduced during the initial 4~6 hours of operation, and then decreased slightly but steadily, followed by leveling off at the size of 20 $\mu$m. The specific resistance of activated sludge increased with operation time, and measured values of specific resistance were matched well with the values estimated on the basis of the mean particle size in the mixed liquor. The contribution of soluble organics and cells to the total resistance was relativdy small compared with that of the supematant. Colloidal particles in the supematant showed much higher specific resistance than that of microbial floc, and played the most important role in the cake resistance.

• Proceedings of the KIEE Conference
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• 2011.07a
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• pp.1288-1289
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• 2011

세계가 점차적으로 "전화(電化)"됨에 따라 전기 에너지의 효과적인 분배와 사용이 급격히 중요하게 되었다. 일반 도체를 통한 전류의 흐름은 도체의 저항에 의해 줄열을 발생시켜 전기 에너지의 손실을 일으키고 결국은 에너지와 경제적 자원의 낭비를 초래하게 된다. 초전도체의 저항은 직류 전류에서는 0, 교류 전류에서는 거의 0이기 때문에 초전도체를 이용하면 전력 소자 및 기기의 부피와 무게를 현저히 줄일 수 있는 반면에 모든 전기 시스템의 효율을 향상시킬 수 있고, 에너지 사용의 절감에 따라 환경 문제에 도움을 줄 수 있다. 사고 전류 제한기의 설계에 있어서, 권선형태에 따른 솔레노이드 마그네트와 팬케이크 마그네트를 설계, 제작하여 자장 특성 및 한류 특성을 비교 하였다. 2세대 고온 초전도 선재로 불리는 YBCO 박막형 초전도 선재를 이용하여 동작 전류 증대를 위한 다병렬 솔레노이드 마그네트와 다병렬 팬케이크 마그네트를 제작하였다. 이를 이용하여 440 V/ 630 A급 초전도 사고 전류 제한기와 2 kA 급 대전류 통전 사고 전류 제한 모듈을 설계, 제작하여 단락 특성 시험을 수행하였다. 한편, 자장 응용 기기에 적용 가능한 더블 팬케이크 마그네트를 제 2 세대 초전도선재를 이용하여 설계, 시작하였다. 2세대 선재는 1세대 선재에 비하여 20 T 이상의 외부 자장에 대한 특성이 우수하여 고자장 마그네트 시스템에 더욱 적합하다. 이에 초전도 마그네트 보호를 위한 상전도 영역 전파 실험을 수행하여 CC 선재의 안정도를 측정하였다. 또한 영구전류모드 운전과 플럭스 펌프를 통한 전류 충전에 대한 연구도 병행하였다.

• Membrane Journal
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• v.30 no.2
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• pp.131-137
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• 2020

In this study, effect of inorganic particles on organic fouling was investigated by a laboratory-scaled pressurized membrane filtration. In order to cause organic fouling, sodium alginate (SA) was used as a feed solution. Regardless of the presence of inorganic SiO₂ particles, the complete pore blocking played an important role in determining the fouling rate during the initial period of membrane filtration. However, the formation of cake layer resulted in the membrane fouling more dominantly as filtration time progressed. In the presence of inorganic particles, both specific cake resistance and compressibility associated with the membrane fouling formed were relatively lower than that without SiO₂ particles. Membrane fouling was more severe at constant flux mode of filtration than that observed at constant pressure mode probably due to the concomitant increase of compressibility of fouling layer with transmembrane pressure (TMP). It was found that the presence of SA and SiO₂ particles in feed solution provided the synergistic effect on the hydraulic backwashing to reduce membrane fouling as compared to the SA solution alone without the inorganic particles.