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Development of Reactors and Dialysis Devices without Damaging Fragile Emulsion

Development of Reactors and Dialysis Devices without Damaging Fragile Emulsion
不破坏易碎乳液的反应器和透析装置的开发
批准号:
14350410
负责人:
OHMURA Naoto
金额:
$9.09万
依托单位:
依托单位国家:
日本
项目类别:
Grant-in-Aid for Scientific Research (B)
财政年份:
2002
资助国家:
日本
项目状态:
已结题
起止时间:
2002 至 2003

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中文摘要
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英文摘要
This research aimed to develop new reactors and dialysis devices without damaging fragile materials. A low shear and laminar flow is required for the fragile materials. Hence, chaotic mixing in a laminar flow field is suitable for development of such reactors. First, this research proposed a new design method of mixing field by means of a constructive approach and to discuss applicability of this method to a two-dimensional laminar mixing field. The presented method consisted of an estimation method based on the information entropy theory and a optimization method using a genetic algorithm. A very simple rotating flow is assigned for a basic component. This method successfully searched the very near optimal configuration of the rotating flow for obtaining a well-mixing state. Next, effect of mixing on chemical reactions in circular Taylor vortex flow reactor was experimentally investigated by using a second-order reaction system. The mixing behaviors in the inside of Taylor vortex cell … More s were also observed by a flow-visualization technique. The flow-visualization experiment clearly revealed the existence of two mixing zones within a Taylor vortex cell at low Reynolds numbers. Namely, the fluid flowing near the cell boundary was axially well-mixed, while the fluid element confined to the vortex core region did not collide with cylindrical wall. This vortex, core region can be regarded as an isolated mixing region. It was found in the reaction experiment that the reaction rate was larger in laminar and singly periodic wavy Taylor vortex flow regimes having large isolated mixing region than in quasi-periodic and weakly turbulent Taylor vortex flow regimes. Mixing behaviors in a conical Taylor vortex flow reactor were investigated using flow visualization and salt-solution techniques. Three different flow modes were observed, i.e. a normal steady Taylor vortex flow, an upward motion of the Taylor vortices and helical vortex flow. In the case of the upward traveling motion, the tracer substance was transported with the traveling vortices in the main flow of cross-section and along the secondary flow streamlines at the outer-edge cell boundaries. Less
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M.N., Nouimehidi: "Mechanism of Mode Selection for Taylor Vortex Flow Mehidi between Coaxial Conical Rotating Cylinders"Journal of Fluid and Structures. 16-2. 247-262 (2002)
M.N.,Nouimehidi:“同轴锥形旋转圆柱体之间的泰勒涡流 Mehidi 模式选择机制”流体与结构杂志。
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通讯作者:
M.N.Noui-Mehidi: "Mechanism of Mode Selection for Taylor Vortex Flow between Coaxial Conical Rotating Cylinders"Journal of Fluid and Structures. 16-2. 247-262 (2002)
M.N.Noui-Mehidi:“同轴锥形旋转圆柱体之间泰勒涡流的模式选择机制”流体与结构杂志。
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发表时间:
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通讯作者:
Naoto, Ohmura: "Observation of Mixing Behaviors in a Conical Taylor-Couette Flow System at Low Reynolds Numbers"Proc.Int.Conf.Fluid and Thermal Energy Conversion 2003. (CD-ROM). 1-8 (2003)
Naoto, Ohmura:“低雷诺数锥形泰勒-库埃特流动系统中混合行为的观察”Proc.Int.Conf.流体和热能转换 2003。(CD-ROM)。
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M.N.Noui-Mehidi: "Numerical Computation of Apex Angle Effects on Taylor Vortices in Rotating Conical Cylinders Systems"Journal of Chemical Engineering of Japan. 35-1. 22-31 (2002)
M.N.Noui-Mehidi:“旋转锥形圆柱体系统中泰勒涡旋顶角效应的数值计算”日本化学工程杂志。
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18
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