4.7 Article

CFD modeling and analysis of dense phase pneumatic conveying of fine particles including particle size distribution

期刊

POWDER TECHNOLOGY
卷 244, 期 -, 页码 30-37

出版社

ELSEVIER
DOI: 10.1016/j.powtec.2013.04.005

关键词

CFD; Fluidized dense; Particle size distribution; Pressure drop

向作者/读者索取更多资源

The process of pneumatic conveying is widely used in industries for conveying materials such as cement, fly ash, alumina etc. Modeling of dense phase or non-suspension flow of fine particles is complex due to several interactions among the carrier gas, particles and the pipe wall. In the present study, dense phase conveying experiment was conducted using alumina as conveying material. The pressure data were recorded at the inlet and the outlet section of the pipeline under different flow conditions. A model of section of pneumatic conveying pipeline was developed in the commercial CFD software Fluent 6.3 Particle size distribution of conveying material has been included in the model in terms of number of solid phases of different mean particle diameters. Simulations were performed by means of Fluent software using the Euler-Euler approach, accounting for four-way coupling. The predicted pressure drop values were found to be in good agreement with the experimental data. Variations of important parameters such as solids volume fraction, gas/solids velocity across the pipe cross-section were analyzed. (C) 2013 Elsevier B.V. All rights reserved.

作者

我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。

评论

主要评分

4.7
评分不足

次要评分

新颖性
-
重要性
-
科学严谨性
-
评价这篇论文

推荐

暂无数据
暂无数据