Resumo (PT):
Abstract (EN):
Slug flow is one of the most frequently occurring multiphase flow patterns in industrial processes. A
deep knowledge of its fundamentals is necessary to accurately model not only the fluid flow but also reaction and
heat and mass transfer in several operation units. A
numerical study is reported on the dynamics of slug
flow, under laminar regime, in vertical columns of stagnant and co-current Newtonian and non-Newtonian
liquids (shear-thickening and shear-thinning). A CFD
package (Ansys FLUENT) with the VOF methodology
was applied to simulate the flow of individual and pairs
of consecutive Taylor bubbles. The behaviour of the most
relevant hydrodynamic features with the approach of the
trailing bubble towards the leading one is addressed,
with particular emphasis to the role of the liquid rheology
and flow configuration. The main results presented are
the velocity ratio curves between consecutive bubbles,
the variation of the bubbles shape, and the axial velocity
and viscosity fields in the surrounding liquid. This bubble-bubble interaction data can be a keystone to improve
and complement continuous slug flow simulators used
for very long columns.
Idioma:
Inglês
Tipo (Avaliação Docente):
Científica
Nº de páginas:
9