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摘要:
The feeding of coarse particles (>0.5 mm diameter) directly into a riser operating at positive pressure is important for drying and pre-heating applications. The presence of the feeding device can lead to heterogeneity of drying and heating, and is the main factor responsible for pressure loss in short conveying systems. However, there is a lack of information concerning the axial and radial distributions of coarse particles in this type of configuration, despite the recent advances when dealing with fine particles (FCC catalyst). The present work therefore investigates a vertical venturi feeder with the conveying system operating in dilute-phase regime with 1 mm spherical glass particles. Experimental assays revealed the behavior of the mass flow rate of solids in the system, and pressure measurements were made along the riser in order to evaluate the accuracy of simulations. Euler-Euler simulations provided close estimation of the experimental pressure drop and the pressure drop according to distance in the linear region. Simulation of the fluid dynamics in the riser showed that solids clusters were formed at low concentrations near the feeding device, reflecting heterogeneity in the solid phase volume fraction.
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篇名 Gas-Solid Flow Behavior in a Pneumatic Conveying System for Drying Applications: Coarse Particles Feeding with a Venturi Device
来源期刊 化学工程与科学期刊(英文) 学科 医学
关键词 Pneumatic CONVEYING VENTURI FEEDER Coarse Particles DRYING CFD
年,卷(期) 2015,(3) 所属期刊栏目
研究方向 页码范围 225-238
页数 14页 分类号 R73
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研究主题发展历程
节点文献
Pneumatic
CONVEYING
VENTURI
FEEDER
Coarse
Particles
DRYING
CFD
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期刊影响力
化学工程与科学期刊(英文)
季刊
2160-0392
武汉市江夏区汤逊湖北路38号光谷总部空间
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386
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0
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