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이산화탄소(CO<sub>2</sub>) 가스에 의한 케이크 여과속도의 향상
임성삼,송연민,Yim, Sung Sam,Song, Yun Min 한국화학공학회 2006 Korean Chemical Engineering Research(HWAHAK KONGHA Vol. No.
압축성이 큰 케이크에 의한 여과에서는 압력의 증가가 여과속도를 거의 향상시키지 못한다. 이 경우 높은 압력은 여과매체 옆의 케이크 공간률을 급격히 감소시켜 dense skin(치밀층, 緻密層)을 형성하여 이 층이 물의 통과속도를 매우 느리게 하기 때문이다. 실제로 압축성이 큰 케이크의 여과에서 여과속도를 향상시키기 위한 특별한 방법이 없었다. 본 연구에서는 여과 대상액을 여과조작 전에 $CO_2$ 가스로 포화시켜 용액에 녹아 있던 $CO_2$ 가스가 압력이 급격히 변하는 치밀층에서 기체 상태로 변화하여 치밀층 내에 작은 공간을 확보하고, 그 공간이 물길을 형성하여 여과속도를 향상시 킬 수 있는 가능성에 대해 연구하였다. For the filtration of super compactible cake, the high filtration pressure can not improve filtration rate. As the high pressure, in this case, decreases the cake porosity adjacent to filter medium and thus forms 'dense skin' which decreases the rate of liquid flow in a great extent. Actually, there was no method to improve filtration rate for the filtration with super compactible cake. We propose the saturation of $CO_2$ gas into the suspension before the filtration operation for improving the filtration rate. The dissolved $CO_2$ gas transforms itself into gas phase in the dense skin through which the pressure changes dramatically. The gas secures its space inside the dense skin, and finally forms the flow passages which improve the filtration rate.
여과-투과에 대한 실험적 분석: 여과매체의 종류, 여과매체의 매수, 여과압력의 영향
임성삼 ( Sung Sam Yim ),송연민 ( Yun Min Song ) 한국화학공학회 2012 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.50 No.2
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.
고액분리 통합이론에서 pd의 역할: 간섭침전, 케이크 여과, 압착에서 케이크 두께를 중심으로
임성삼 ( Sung Sam Yim ),송연민 ( Yun Min Song ) 한국화학공학회 2012 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.50 No.2
To know the role of ``the solid compressive pressure to the first solid layer of a cake, pd`` in the ``unified theory on solid-liquid separation``, we analyzed extremely compressible cake formed with floc for the following three operations with our new concepts, First, the role of pd was studied in calculating the sediment thickness of floc, and in calculating the cake thickness in cake filtration performed with floc sediment. Second, we calculated the expression procedure using pd, Finally, the influence of pd on cake thickness in hindered sedimentation, and on the calculation of the procedure of hindered sedimentation pd was verified, Thus the possibility of application of ``unified theory on solid-liquid separation`` and the importance of pd was verified, Through these processes, new theoretical definitions of the cake filtration, expression and hindered sedimentation was established.
보문 : 분리기술·열역학·멤브레인기술·초임계기술·이은용액 ; 침전이 수반되는 케이크 여과 II: 새로운 분석과 케이크에 도입되는 현탁액의 고체 질량분율
임성삼 ( Sung Sam Yim ) 한국화학공학회 2012 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.50 No.3
수평 여과매체를 사용한 케이크 여과에서는 침전이 수반된다. 이 침전 현상을 고려하지 않을 경우 여과기간의 케이크 평균비저항 값이 두 배 이상까지도 잘못 측정될 수 있다. 저자의 전번 논문에서는 여과기간에 침전으로 인해 케이크에 들어가는 현탁액의 고체분율이 변화한다는 것을 이론적으로 주장하였으나, 그 변화가 어느 정도인지를 알아내지 못하였다. 이 논문에서는 먼저 여과-투과 실험방법에 대한 분석에서 투과기간에 측정된 케이크 평균비저항 값이 옳다 는 것을 여러 방법으로 증명하고, 여과기간에 통상적인 방법으로 측정된 평균비저항 값은 여과가 진행되는 순간의 현 탁액의 고체분율 대신 초기 고체분율을 사용하므로 정확하지 못하다는 것을 입증하였다. 여과와 투과에서 측정된 실험값을 사용하여, 여과 진행 동안 침전에 의해 변화한 현탁액의 고체분율을 계산하였다. 그 후 여과 진행 동안 측정한 현탁액의 높이 변화 값과 이 논문에서 새로 만든 수식을 사용하여 여과 진행 중의 현탁액 고체분율을 결정하였다. 두 가지 방법으로 결정된 현탁액의 고체분율을 비교하여 두 가지가 거의 일치함을 입증하였다. 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.
송연민(Yun Min Song),임성삼(Sung Sam Yim) 大韓環境工學會 2008 대한환경공학회지 Vol.30 No.2
본 연구에서는 새로운 여과-투과(filtration-permeation) 실험 방법을 사용하여 여과실험에 영향을 미치는 인자 중 침전에 대한 영향을 입자현탁액과 플럭현탁액에 대해 각각 수행하였다. 그 결과 여과실험으로는 정확한 평균 비저항값을 예측할 수 없었으나, 투과실험으로 정확한 평균 비저항값을 측정할 수 있었다. 투과기간을 연장하였을 때 입자현탁액에서 형성된 케이크에서는 투과속도에 별다른 영향이 없었으나 플럭현탁액의 경우는 응집제의 쓸려나감 현상을 보였다. 또한 여과-투과 실험을 사용하여 투과시에 단계적으로 압력을 증가시킴으로써 단 한번의 실험에 의해 케이크의 압축성이 측정되어 질 수 있음을 보였으며, 이 방법을 응용하여 평균 비저항값이 큰 활성슬러지의 긴 여과시간을 짧게 줄여 측정하는 새로운 방법을 제안하였다. 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 filtration- permeation is also proposed.