کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
234991 465625 2016 11 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Application of parallel distributed Lagrange multiplier technique to simulate coupled Fluid-Granular flows in pipes with varying Cross-Sectional area
ترجمه فارسی عنوان
استفاده از تکنیک تکثیر لاگرانژ موازی توزیع شده برای شبیه سازی جریان سیال گرانولا شده در لوله های با مساحت متقاطع مختلف
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


• The paper addresses the physics of pneumatic conveying in pipes with varying cross-sectional area.
• Correlations between pressure losses and solid mass fluxes are derived.
• The comparison of the simulations with existing experimental and theoretical results from the literature is discussed.

Fluid-granular flows are common phenomena in nature and industry. Here, an efficient computational technique based on the distributed Lagrange multiplier method is utilized to simulate complex fluid-granular flows. Each particle is explicitly resolved on an Eulerian grid as a separate domain, using solid volume fractions. The fluid equations are solved through the entire computational domain, however, Lagrange multiplier constrains are applied inside the particle domain such that the fluid within any volume associated with a solid particle moves as an incompressible rigid body. The particle–particle interactions are implemented using explicit force-displacement interactions for frictional inelastic particles similar to the DEM method (Cundall and Strack, 1979) with some modifications using the volume of an overlapping region as an input to the contact forces. A parallel implementation of the method is based on the SAMRAI (Structured Adaptive Mesh Refinement Application Infrastructure) library.Application of this method to simulate fluid-granular flows in pipes with a step decrease in cross-sectional area is discussed. Correlations between pressure losses and solid mass fluxes in a pipe for different particle concentrations, pipe diameters and particle sizes are studied. Results of the simulations agree well with available experimental data for the mass flow ratio vs pressure drop during conveying.

Particle conveying of 180 μm particles through the orifice of diameter 3 mm. Fluid velocity field is shown by color. The white line shows flow separation and stagnation regions.Figure optionsDownload as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Powder Technology - Volume 291, April 2016, Pages 35–45
نویسندگان
, ,