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The analysis of a chaotic mixing method with a Taylor vortex flow and the possibility to a blood filtration system and a photo-bioreactor.

The analysis of a chaotic mixing method with a Taylor vortex flow and the possibility to a blood filtration system and a photo-bioreactor.
泰勒涡流混沌混合方法的分析以及血液过滤系统和光生物反应器的可能性。
批准号:
17560133
负责人:
KAWAI Hideki
金额:
$1.98万
依托单位国家:
日本
项目类别:
Grant-in-Aid for Scientific Research (C)
财政年份:
2005
资助国家:
日本
项目状态:
已结题
起止时间:
2005 至 2006

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中文摘要
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英文摘要
Chaotic mixing method and its application to the filtration system for solid-1iquid multipnase flowThe main vortex mode with the extra smaller vortex has occurred at the aspect ratio (Γ) of 1.0 and the radius ratio(η)of 0.375 under the rigid boundary layer (Ekman boundary layer), which exists near the vertical boundary ends. This vortex keeps its original shape even in the high Reynolds number (Re) of 20,000 in the region of the turbulence. In the filtration system with Γ=3 and η=0.375, the nylon particle (mean diameter is about 80 μm and the specific gravity of 1.2) is used, and at Re=0, most particle is accumulated on the filter surface in a few minutes, but the pressure drop is confirmed to keep in lower level when the rotating Re is increased. This fact shows the clear effect on reducing the pressure drop of the filtration process. However, the pulsating suction of the flow would sometimes cause the instability in filtration, which is not clarified yet.Cultivation of microorganism … More With Taylor vortex flowSince it is difficult to use a blood cell directly in the engineering laboratory, the similar vegetable photosynthesis microorganisms are used and the fluid dynamic effect on cultivation by the Taylor vortex is investigated at Γ=1. As for the actual size, the diameter of the inner cylinder is 28mm, and the one of the outer 75mm, are selected respectively. The cultivation time is about ten days. As the result, a specific growth rate (p) increases with the increase of Re. But in the very limited region of 6000<Re<8250, μ takes a steep sloop, and after then, it turns to sharp decline in 8250<Re<9600. In Re>9600, μ increases again with a gentle gradient curve. p shows the maximum value at Re=8250, but not becomes the same value at Re=18000, although the sedimentation rate is same at Re=18000 as Re=8250. This fact indicates the flow structure is different between both Reynolds numbers. This flow pattern is measured using Ultrasound Doppler Profiler and shows the averaged velocity profiles are quite different between Re=8000 and 26000. Each flow is more turbulent, but it is well observed that the flow at Re=8000 has one vortex with an extra vortex in the bottom region and the one at Re=26000 has pair vortices in upper and lower regions. This difference would influence the specific growth rate. In this reactor, Spirulina is alive until Re=40000 without disturbing from the share flow. Less
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Visualization of Rotating Filtration System with Taylor-Couette Flow for Particle-liquid Separation or Water-purification
用于颗粒-液体分离或水净化的泰勒-库埃特流旋转过滤系统的可视化
DOI: --
发表时间: 2006
期刊: Abstracts of 5th International Conference on Unsteady-state Process in Catalysis
影响因子: --
作者: [Hideki Kawai, Hiroshi Takahashi, Hiroshige Kikura, Hajime Yamashita]
通讯作者: Hajime Yamashita
DOI: --
发表时间: 2006
期刊: Abstracts of fifth International Conference on Unsteady-state Process in Catalysis
影响因子: --
作者: [Hideki Kawai, Fumitake Tanaka, Hiroshi Takahashi]
通讯作者: Hiroshi Takahashi
DOI: --
发表时间: 2007
期刊: Journal of Chemical Engineering of Japan Vol.40No.11
影响因子: --
作者: [Kawai, H., Kudo, H. and Takahashi, H.]
通讯作者: H.
高炉低還元材比操業を模擬した二次元コーノレドモデルによる固体不安定降下挙動の解析
使用二维 Konoredo 模型模拟高炉低还原材料比操作的固体不稳定下降行为分析
DOI: --
发表时间: 2006
期刊: 鉄と鋼 Vol.92・No 12
影响因子: --
作者: [高橋洋志, 河合秀樹, 小林基史, 福井俊史]
通讯作者: 福井俊史
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