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Received July 29, 2004
Accepted January 10, 2005
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기-액 향류 흐름 기포탑 생물 반응기에서 기포 흐름 거동 특성
Characteristics of Bubble Flow Behavior in a Gas-liquid Countercurrent Bubble Column Bioreactor
충남대학교 화학공학과, 305-764 대전시 유성구 궁동 220 1한국과학기술원 생명화학공학과, 305-701 대전시 유성구 구성동 373-1
School of Chemical Engineering, Chungnam National University, 220, Gung-dong, Yuseong-gu, Daejeon 305-764, Korea 1Department of Biomolecular & Chemical Engineering, KAIST, 373-1, Guseong-dong, Yuseong-gu, Daejeon 305-701, Korea
Korean Chemical Engineering Research, April 2005, 43(2), 272-277(6), NONE Epub 9 May 2005
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Abstract
직경이 0.152 m이고 높이가 3.5 m인 기-액 향류 흐름 기포탑에서 기포의 물성과 흐름의 거동을 고찰하고 진단하였다. 기체와 액체의 유속 그리고 기포의 분산형태(even, wall-side, central or asymmetric distribution)가 반응기 내부에 서 기포의 크기, 빈도수, 상승속도와 체류량 등 기포특성에 미치는 영향을 이중 전기 저항 탐침법을 이용하여 측정 검토하였다. 기포의 크기, 빈도수와 체류량은 기체나 액체 유속의 증가에 따라 증가하였다. 기포의 상승속도는 기체 유속의 증가에 따라 증가하였지만, 액체 유속의 증가에 따라서는 감소하였다. 기포 크기 분포의 균일성이나 체류량은 기포 분산판에서 기포의 분산형태가 균일분포에서 벽면, 중앙 그리고 비대칭 분산으로 변화함에 따라 감소하였다. 기포의 체류량과 분포에 대한 균일성을 고려하면, 기포의 중앙 분산 형태가 비대칭 분산 형태보다는 유리하며, 벽면 분산 형태분산보다는 좋지 않았다.
Characteristics of bubbling behavior and bubble properties were investigated in a gas-liquid countercurrent bubble column of in diameter 0.152 m and 3.5 m in height, respectively. Effects of gas and liquid velocities and bubble distribution mode(even, wall-side, central or asymmetric distribution) on the bubble properties such as chord length, frequency, rising velocity and holdup in the reactor were measured and examined by means of dual resistivity probe method. The bubble size, frequency and holdup increased with increasing gas(UG) or liquid velocity(UL). The rising velocity of bubbles increased with increasing UG, whereas decreased with increasing UL. The uniformity of bubble size distribution and bubble holdup decreased when the distribution mode of bubbles at the gas distributor was changed from even to wall-side, central or asymmetric. The central distribution of bubbles was better than asymmetric mode but worse than wall-side distribution, in considering the bubble holdup and uniformity of distribution.
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Ibrahim YA, Briens CL, Margaritis A, Bergongnou MA, AIChE J., 42(7), 1889 (1996)
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Lee DH, Epstein N, Grace JR, Korean J. Chem. Eng., 17(6), 684 (2000)
Garcia-Calderon D, Buffiere P, Moletta R, Elmaleh S, Water Res., 32(12), 3593 (1998)
Buffiere P, Moletta R, Chem. Eng. Sci., 54(9), 1233 (1999)
Son SM, Song PS, Lee CG, Kang SH, Kang Y, Kusakabe K, "Bubbling Behavior in Gas-Liquid Countercurrent Bubble Column Bioreactors", J. Chem. Eng. Japan, in press (2004)
Kang Y, Cho YJ, Woo KJ, Kim KI, Kim SD, Chem. Eng. Sci., 55(2), 411 (2000)
Nam SH, Cho YJ, Kang Y, Choi HS, Kim SD, HWAHAK KONGHAK, 38(6), 859 (2000)
Kang Y, Cho YJ, Woo KJ, Kim SD, Chem. Eng. Sci., 54(21), 4887 (1999)