螺旋(铁路)
计算流体力学
重力分离
计算机科学
流利
机械工程
选矿厂
流体力学
工艺工程
工程类
模拟
机械
航空航天工程
物理
环境工程
电信
作者
Bw Matthews,Caj Fletcher,A. C. Partridge,T. Jancar
出处
期刊:Chemeca 96: Excellence in Chemical Engineering; 24th Australian and New Zealand Chemical Engineering Conference and Exhibition; Proceedings
日期:1996-01-01
卷期号:: 17-
被引量:10
摘要
Spiral separators are gravity concentrating devices that play an important role in the fine coal and mineral processing industries. Particles are separated on the basis of their density and size and, in an attempt to optimise the separation mechanisms, the spiral design has evolved almost exclusively through empirical analysis. To understand the underlying physical processes at a more fundamental level, the past decade has seen developments in theoretical considerations of spiral performance. The present paper is a continuation of this approach, and uses computational fluid dynamics (CFD) to examine the fluid flow behaviour of the LD9 spiral unit used for fine coal processing. Results are obtained using a commercially available CFD code, FLUENT, and are validated against an ongoing collaborative experimental research program. It is envisaged that the model will provide the basic framework for an ultimate parametric assessment of the spiral design.
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