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多出口稀相气力输送过程分析与计算

刘甜甜 王振南 王国刚 李世鹏 黄继鑫 朱丽云 王振波

化学工程2026,Vol.54Issue(5):57-62,6.
化学工程2026,Vol.54Issue(5):57-62,6.DOI:10.3969/j.issn.1005-9954.2026.05.010

多出口稀相气力输送过程分析与计算

Analysis and calculation of multi-outlet dilute phase pneumatic conveying process

刘甜甜 1王振南 1王国刚 1李世鹏 1黄继鑫 1朱丽云 2王振波2

作者信息

  • 1. 青岛惠城环保科技集团股份有限公司,山东青岛 266520
  • 2. 中国石油大学(华东)新能源学院,山东青岛 266580
  • 折叠

摘要

Abstract

In order to optimize the structure of multi-outlet dilute phase pneumatic conveying pipeline and realize multi-point uniform discharge,the flow characteristics of dilute phase pneumatic conveying in four-outlet branch pipeline with two structural forms were simulated and studied by using the particle fluid dynamics simulation software Barracuda and Wen-Yu drag force model.Taking the partial flow coefficient as the evaluation index,the degree of partial flow of the two structures was compared,and the influence of conveying conditions and fluidization distributor structure on the uniformity of discharge was analyzed.The results show that the discharge quantity of each outlet is more uniform in the pipeline with fluidization distributor.Both the conveying volume and the conveying gas velocity affect the flow characteristics in the pipe.The deviation coefficient increases continuously with the conveying volume increasing,and the deviation coefficient decreases continuously with the inlet gas velocity increasing.With the increase of the diameter-height ratio of the cylindrical part of the fluidization distributor,the deviation coefficient increases first and then decreases,and the deviation coefficient is the largest when the diameter-height ratio is 10∶7.With the increase of the volume of the fluidization distributor,the deviation coefficient increases continuously.For the pipeline with four outlets,the recommended diameter is 300-600 mm.The research results provide a basis for the design and optimization of industrial multi-export dilute-phase pneumatic conveying pipelines.

关键词

多出口/稀相/气力输送/偏流/模拟计算

Key words

multiple exports/rare phase/pneumatic conveying/partial flow/simulation calculation

分类

化学化工

引用本文复制引用

刘甜甜,王振南,王国刚,李世鹏,黄继鑫,朱丽云,王振波..多出口稀相气力输送过程分析与计算[J].化学工程,2026,54(5):57-62,6.

基金项目

青岛市技术创新重点项目(LX202303.0030) (LX202303.0030)

化学工程

1005-9954

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