-
- Saomoto Kenjiro
- Department of Chemical Science and Engineering, Kobe University
-
- Horie Takafumi
- Department of Chemical Science and Engineering, Kobe University
-
- Kumagai Norihisa
- Department of Chemical Science and Engineering, Kobe University
-
- Takigawa Teiji
- Process Research Laboratories, Kashima Plant, Eisai Co. Ltd.
-
- Noui-Mehidi Mohamed Nabil
- Thermal and Fluid Engineering, CSIRO
-
- Ohmura Naoto
- Department of Chemical Science and Engineering, Kobe University
この論文をさがす
抄録
The present study investigated the dispersion of floating particles in a Taylor vortex flow reactor experimentally and numerically. The working fluid was glycerin solution and had a density (ρf) of 1210 kg·m-3 and a viscosity (μ) of 0.1 Pa·s. Floating particles of an acrylic resin had a density (ρp) of 1190 kg·m-3.Two groups of particles with mean diameters of 710 and 974μm were discerned. Although particles penetrated the Taylor vortex flow region in the axial direction at different rotational Reynolds numbers, particle segregation was observed. It was confirmed that the smaller particles penetrated deeper in the axial direction. Numerical simulations were also conducted to elucidate the mechanism of particle segregation. Numerical results of a particle-tracking method indicate that the small particles moved on the outermost orbit of a torus. Results of a distinct element method suggest that interparticle collision affected particle transference between vortices.
収録刊行物
-
- JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
-
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 43 (4), 319-325, 2010
公益社団法人 化学工学会
- Tweet
詳細情報 詳細情報について
-
- CRID
- 1390001204569195776
-
- NII論文ID
- 10027372487
-
- NII書誌ID
- AA00709658
-
- ISSN
- 18811299
- 00219592
-
- NDL書誌ID
- 10755803
-
- 本文言語コード
- en
-
- データソース種別
-
- JaLC
- NDL
- Crossref
- CiNii Articles
-
- 抄録ライセンスフラグ
- 使用不可