Inter-compartment interaction in multi-impeller mixing

Part II. Experiments, sliding mesh and large Eddy simulations

Journal Article (2018)
Author(s)

Cees Haringa (TU Delft - ChemE/Transport Phenomena)

Ruben Vandewijer (Student TU Delft)

R.F. Mudde (TU Delft - ImPhys/Imaging Physics, TU Delft - Executive board)

Research Group
ChemE/Transport Phenomena
Copyright
© 2018 C. Haringa, Ruben Vandewijer, R.F. Mudde
DOI related publication
https://doi.org/10.1016/j.cherd.2018.06.007
More Info
expand_more
Publication Year
2018
Language
English
Copyright
© 2018 C. Haringa, Ruben Vandewijer, R.F. Mudde
Research Group
ChemE/Transport Phenomena
Volume number
136
Pages (from-to)
886-899
Reuse Rights

Other than for strictly personal use, it is not permitted to download, forward or distribute the text or part of it, without the consent of the author(s) and/or copyright holder(s), unless the work is under an open content license such as Creative Commons.

Abstract

Steady state multiple reference frame-RANS (MRF-RANS) simulations frequently show strong over-predictions of the mixing time in single-phase, multi-impeller mixing tanks, which is sometimes patched by ad hoc tuning of the turbulent Schmidt-number. In Part I of this work, we experimentally revealed the presence of macro-instabilities in the region between the impellers, as well as a peak in the turbulent kinetic energy in the region where the flow from the individual impellers converges. The MRF-RANS method was found unable to capture both. In this second paper, we show that the sliding-mesh RANS (SM-RANS) approach does capture the effect of macro-instabilities, while still underestimating the turbulent kinetic energy. Consequently, the SM-RANS method mildly over-estimates the mixing time, while being less sensitive to the exact mesh geometry. Large eddy simulations with the dynamic Smagorinsky model reasonably capture the kinetic energy contained in macro-instabilities, and properly assess the turbulent kinetic energy in the region between the impellers, even for crude meshes. Consequently, the mixing time is reasonably assessed, and even under-predicted at the crudest meshes. However, the turbulent kinetic energy and energy dissipation in the impeller discharge stream are poorly assessed by the dynamic Smagorinsky model.

Files

1_s2.0_S0263876218302922.pdf
(pdf | 5.29 Mb)
- Embargo expired in 13-12-2018
License info not available