Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach

The present contribution summarizes research related to the numerical computation of pneumatic conveying systems applying the Euler/Lagrange approach. For that purpose, a rigorous modelling of the particulate phase was aspired, including the relevant fluid dynamic forces, particle‐wall collisions wi...

Full description

Autores:
Laín Beatove, Santiago
Sommerfeld, Martin
Tipo de recurso:
Article of journal
Fecha de publicación:
2014
Institución:
Universidad Autónoma de Occidente
Repositorio:
RED: Repositorio Educativo Digital UAO
Idioma:
eng
OAI Identifier:
oai:red.uao.edu.co:10614/12166
Acceso en línea:
http://hdl.handle.net/10614/12166
https://doi.org/10.1002/cjce.22105
Palabra clave:
Control neumático
Pneumatic control
Pneumatic conveying
Numerical calculation (CFD)
Euler/Lagrange approach
Horizontal pipe/bend/vertical pipe
Rights
openAccess
License
Derechos Reservados - Canadian Society for Chemical Engineering, 2015
Description
Summary:The present contribution summarizes research related to the numerical computation of pneumatic conveying systems applying the Euler/Lagrange approach. For that purpose, a rigorous modelling of the particulate phase was aspired, including the relevant fluid dynamic forces, particle‐wall collisions with wall roughness and inter‐particle collisions. For the validation of the computations, experiments of Huber and Sommerfeld were selected for the conveying through a 80 mm stainless steel pipe with 5 m horizontal pipe, bend and 5 m vertical pipe. The majority of the computations were done for the same pipe system; however, in this instance, consisting of 150 mm stainless steel pipes. In these cases the average conveying velocity was 27 m/s and the particle mass loading was 0.3 (mass flow rate of particles/mass flow rate of air). For this configuration the influence of wall roughness, inter‐particle collisions, particle size, and mass loading on the resulting particle concentration distribution, the secondary flow as well as the pressure drop in the different pipe elements was analyzed. Moreover, a segregation parameter was defined which describes the location of the maximum particle concentration throughout the pipe system. The secondary flow intensity (SFI) was used to characterize the influence of the particle phase on the developing structure of the secondary flow