turbulent particle-laden and droplet-laden flows: anadvancededdy...

2
ISROMAC International Symposium on Transport Phenomena and Dynamics of Rotating Machinery Maui, Hawaii December -, S Y M P O S I A O N R O T A T I N G M A C H I N E R Y [Extended Abstract] Turbulent particle-laden and droplet-laden flows: An advanced eddy-resolving simulation methodology with de- terministic collision, agglomeration and coalescence models Michael Breuer, Naser Almohammed, Department of Fluid Mechanics, Helmut-Schmidt University Hamburg, Germany Introduction e increase of the computational resources in the last decade has a strong impact on the prospects of numerical simulations for turbulent disperse multiphase ows. On the one hand, it allows to replace classical Reynolds-Averaged Navier-Stokes (RANS) predictions by more advanced eddy-resolving approaches such as large-eddy simulations (LES) or hybrid LES-RANS approaches. On the other hand, it paves the way to include more physical phenomena in the simulation of the particular phase. Relying on an Euler-Lagrange concept, these eects can be described based on rst principles and not on empirical correlations as typically done in the Euler-Euler concept. at is extremely benecial for the setup of appropriate models. e present contribution gives an overview of recent developments related to the prediction of inter-particle or inter-droplet collisions, the agglomeration of particles, the adhesion of particles at walls and the coalescence of droplets in complex turbulent ows. Methodology of LES with agglomeration, coalescence and adhesion models Relying on a four-way coupled Euler-Lagrange approach, the continuous phase is solved in an Eulerian frame of reference taking the conservation equations of the ltered quantities used in LES into account. e solution is based on a -D nite-volume method for arbitrary non-orthogonal and block-structured grids, which is fully parallelized based on the domain decomposition technique. e disperse phase is solved in a Lagrangian frame of reference [, , ]. e equation of motion is given by Newton’s second law, where the uid forces are derived from the displacement of a sphere in a non-uniform ow. For particles or droplets with a density much higher than the carrier uid, only the drag, li, gravity and buoyancy forces have to be considered. e ordinary dierential equation for the particles is integrated in physical space. To avoid time-consuming search algorithms, the second integration to determine the particle position on the grid is done in the computational space. Here an explicit relation between the position of the particle and the cell index containing the particle exists [], which is required to calculate the uid forces on the particle. us, a highly ecient particle tracking scheme results allowing to predict the paths of millions of particles, i.e., ows with high mass loadings where inter-particle or inter-droplet collisions are occurring. e collisions between particles or droplets within the four-way coupled simulation are predicted deterministically by a recently developed and highly ecient collision algorithm []. Inter-particle or inter-droplet collisions are a prerequisite for additional important physical phenomena, i.e., the agglomeration of particles and the coalescence of droplets. For the former an energy-based and a

Upload: others

Post on 21-Feb-2021

0 views

Category:

Documents


0 download

TRANSCRIPT

Page 1: Turbulent particle-laden and droplet-laden flows: Anadvancededdy ...isromac-isimet.univ-lille1.fr/upload_dir/abstract17/36... · 2017. 2. 11. · into account. „e solution is based

ISROMAC 2017International Symposium on Transport Phenomena

and Dynamics of Rotating MachineryMaui, Hawaii

December 16-21, 2017

SYM

POSI

A

ON ROTATING MACHIN

ERY

[Extended Abstract]

Turbulent particle-laden and droplet-laden flows:An advanced eddy-resolving simulationmethodologywith de-terministic collision, agglomeration and coalescence modelsMichael Breuer, Naser Almohammed, Department of Fluid Mechanics, Helmut-Schmidt UniversityHamburg, Germany

Introduction�e increase of the computational resources in the last decade has a strong impact on the prospects ofnumerical simulations for turbulent disperse multiphase �ows. On the one hand, it allows to replaceclassical Reynolds-Averaged Navier-Stokes (RANS) predictions by more advanced eddy-resolvingapproaches such as large-eddy simulations (LES) or hybrid LES-RANS approaches. On the otherhand, it paves the way to include more physical phenomena in the simulation of the particular phase.Relying on an Euler-Lagrange concept, these e�ects can be described based on �rst principles and noton empirical correlations as typically done in the Euler-Euler concept. �at is extremely bene�cial forthe setup of appropriate models. �e present contribution gives an overview of recent developmentsrelated to the prediction of inter-particle or inter-droplet collisions, the agglomeration of particles,the adhesion of particles at walls and the coalescence of droplets in complex turbulent �ows.

Methodology of LES with agglomeration, coalescence and adhesion modelsRelying on a four-way coupled Euler-Lagrange approach, the continuous phase is solved in anEulerian frame of reference taking the conservation equations of the �ltered quantities used in LESinto account. �e solution is based on a 3-D �nite-volume method for arbitrary non-orthogonal andblock-structured grids, which is fully parallelized based on the domain decomposition technique.

�e disperse phase is solved in a Lagrangian frame of reference [1, 2, 3]. �e equation of motionis given by Newton’s second law, where the �uid forces are derived from the displacement of a spherein a non-uniform �ow. For particles or droplets with a density much higher than the carrier �uid,only the drag, li�, gravity and buoyancy forces have to be considered. �e ordinary di�erentialequation for the particles is integrated in physical space. To avoid time-consuming search algorithms,the second integration to determine the particle position on the grid is done in the computationalspace. Here an explicit relation between the position of the particle and the cell index containingthe particle exists [1], which is required to calculate the �uid forces on the particle. �us, a highlye�cient particle tracking scheme results allowing to predict the paths of millions of particles, i.e.,�ows with high mass loadings where inter-particle or inter-droplet collisions are occurring.

�e collisions between particles or droplets within the four-way coupled simulation are predicteddeterministically by a recently developed and highly e�cient collision algorithm [2]. Inter-particleor inter-droplet collisions are a prerequisite for additional important physical phenomena, i.e., theagglomeration of particles and the coalescence of droplets. For the former an energy-based and a

Page 2: Turbulent particle-laden and droplet-laden flows: Anadvancededdy ...isromac-isimet.univ-lille1.fr/upload_dir/abstract17/36... · 2017. 2. 11. · into account. „e solution is based

momentum-based agglomeration model for rigid, dry and electrostatically neutral particles weredeveloped in the framework of the hard-sphere model with deterministic collision detection [4, 5]. Forsurface-tension dominated droplets a similar methodology is proposed which evaluates the collisionevents of droplets based on the impact parameter and the Weber number. Based on experimentalobservations �ve di�erent regimes have to be distinguished for this purpose, i.e., slow coalescence,bouncing, fast coalescence and re�exive or stretching separation leading to di�erent outcomes of thecollision event. To identify these regimes, a composite collision outcome model has been developed.

Another physical phenomenon taken into account is the deposition of particles on boundingwalls due to the van-der-Waals force. Here, the physically relevant conditions for sticking andsliding inelastic collisions (normal restitution coe�cient en,w < 1) including friction were recentlydetermined. �e modeling assumptions are in accordance with the momentum-based agglomerationmodel and lead to a new adhesion model [6]. �is model was validated based on experiments in ahorizontal particle-laden channel �ow. Exemplarily, Fig. 1 depicts the side view of a stream of particlesaround a SD7003 airfoil. Note that this is not a contour plot but the particles are shown as sca�erpoints colored according to the velocity in mean �ow direction. Two di�erent particle diameters aretaken into account, i.e., small (10 µm) and large particles (50 µm). Obviously, there is a signi�cantdi�erence between both cases since small particles closely follow the continuous �uid, whereas largeparticles can not follow the curved surface of the airfoil at the suction side due to their higher inertia.�at leads to di�erent deposition pa�erns at the airfoil surface as shown below. A detailed summaryof these developments including di�erent applications will be provided in the full contribution.

dp = 10 µm dp = 50 µm

Figure 1. Stream of particles around the airfoil for two di�erent particle diameters colored by thestreamwise velocity and corresponding deposition pa�erns.

References[1] M. Breuer, H. T. Baytekin, and E. A. Matida. Prediction of aerosol deposition in 90 degrees bends using LES

and an e�cient Lagrangian tracking method. J. Aerosol Science, 37(11):1407–1428, 2006.

[2] M. Breuer and M. Alle�o. E�cient simulation of particle–laden turbulent �ows with high mass loadingsusing LES. Int. J. Heat Fluid Flow, 35:2–12, 2012.

[3] M. Alle�o and M. Breuer. One–way, two–way and four–way coupled LES predictions of a particle–ladenturbulent �ow at high mass loading downstream of a con�ned blu� body. Int. J. Multiphase Flow, 45:70–90,2012.

[4] M. Breuer and N. Almohammed. Modeling and simulation of particle agglomeration in turbulent �owsusing a hard–sphere model with deterministic collision detection and enhanced structure models. Int. J.Multiphase Flow, 73:171–206, 2015.

[5] N. Almohammed and M. Breuer. Modeling and simulation of agglomeration in turbulent particle–laden�ows: A comparison between energy–based and momentum–based agglomeration models. PowderTechnology, 294:373–402, 2016.

[6] N. Almohammed and M. Breuer. Modeling and simulation of particle–wall adhesion of aerosol particles inparticle–laden turbulent �ows. Int. J. Multiphase Flow, 85:142–156, 2016.