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复合移动床电石反应器中颗粒运动的离散单元法模拟

黄迪 曾剑桥 刘辉

化工进展Issue(10):2576-2582,7.
化工进展Issue(10):2576-2582,7.DOI:10.3969/j.issn.1000-6613.2014.10.010

复合移动床电石反应器中颗粒运动的离散单元法模拟

Discrete element method simulation of particle flow in a combined-moving bed reactor for carbide production

黄迪 1曾剑桥 1刘辉1

作者信息

  • 1. 北京化工大学化工资源有效利用国家重点实验室,北京 100029
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摘要

Abstract

In this paper,the particle flow in a combined-moving bed reactor was simulated using the discrete element method(DEM),and the accuracy of DEM simulation was verified by a comparison with the literature results. The effects of rotational speed and open-hole size of two kinds of distributing devices were analyzed. The results showed that:①There are two kinds of flow patterns for the two distributing devices,i.e.,plug flow and funnel flow;②particle mass fluxes increased non-linearly with the increase of rotational speed and open-hole size of the distributing devices;③along the radial direction,particles were distributed more uniformly with increasing the rotational speed and open-hole size,and the distribution showed U and M shapes for the two kinds of distributing devices;④the radial distribution of particles were more uniformly downwardly along the axial direction,with values of the variance coefficient exceeding 1.0 for the fan-shaped hole distributing plate,and 0.5 for another distributing plate.

关键词

离散单元法/数值模拟/颗粒流/移动床/布料器

Key words

discrete element method/numerical simulation/granular flow/moving bed/distributing device

分类

化学化工

引用本文复制引用

黄迪,曾剑桥,刘辉..复合移动床电石反应器中颗粒运动的离散单元法模拟[J].化工进展,2014,(10):2576-2582,7.

基金项目

国家973计划项目(2011CB201306)。 ()

化工进展

OA北大核心CSCDCSTPCD

1000-6613

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