The migration of neutrally buoyant finite sized particles in a Newtonian square channel flow is investigated in the limit of very low solid volumetric concentration, within a wide range of channel Reynolds numbers Re = [0.07-120]. In situ microscope measurements of particle distributions, taken far from the channel inlet (at a distance several thousand times the channel height), revealed that particles are preferentially located near the channel walls at Re > 10 and near the channel center at Re < 1. Whereas the cross-streamline particle motion is governed by inertia-induced lift forces at high inertia, it seems to be controlled by shear-induced particle interactions at low (but finite) Reynolds numbers, despite the low solid volume fraction (<1%). The transition between both regimes is observed in the range Re = [1-10]. In order to exclude the effect of multi-body interactions, the trajectories of single freely moving particles are calculated thanks to numerical simulations based on the force coupling method. With the deployed numerical tool, the complete particle trajectories are accessible within a reasonable computational time only in the inertial regime (Re > 10). In this regime, we show that (i) the particle undergoes cross-streamline migration followed by a cross-lateral migration (parallel to the wall) in agreement with previous observations, and (ii) the stable equilibrium positions are located at the midline of the channel faces while the diagonal equilibrium positions are unstable. At low flow inertia, the first instants of the numerical simulations (carried at Re = O(1)) reveal that the cross-streamline migration of a single particle is oriented towards the channel wall, suggesting that the particle preferential positions around the channel center, observed in the experiments, are rather due to multi-body interactions.

1.
G.
Segré
and
A.
Silberberg
, “
Behaviour of macroscopic rigid spheres in Poiseuille flow: Part 1, Part 2. Experimental results and interpretation
,”
J. Fluid Mech.
14
,
136
157
(
1962
).
2.
B. P.
Ho.
and
L. G.
Leal
, “
Inertial migration of rigid spheres in two-dimensional unidirectional flows
,”
J. Fluid Mech.
65
,
365
400
(
1974
).
3.
P.
Vasseur
and
R. G.
Cox
, “
The lateral migration of a spherical particle in two-dimensional shear flows
,”
J. Fluid Mech.
78
,
385
413
(
1976
).
4.
J. A.
Schonberg
and
E. J.
Hinch
, “
Inertial migration of a sphere in Poiseuille flow
,”
J. Fluid Mech.
203
,
517
524
(
1989
).
5.
E. S.
Asmolov
, “
The inertial lift on a spherical particle in a plane Poiseuille flow at large channel Reynolds number
,”
J. Fluid Mech.
381
,
63
87
(
1999
).
6.
J. P.
Matas
,
J. F.
Morris
, and
E.
Guazzelli
, “
Lateral force on a rigid sphere in large-inertia laminar pipe flow
,”
J. Fluid Mech.
621
,
59
67
(
2009
).
7.
D.
Di Carlo
, “
Inertial microfluidics
,”
Lab Chip
9
,
3038
3046
(
2009
).
8.
A. A. S.
Bhagat
,
S. S.
Kuntaegowdanahalli
, and
I.
Papautsky
, “
Enhanced particle filtration in straight microchannels using shear-modulated inertial migration
,”
Phys. Fluids
20
,
101702
(
2008
).
9.
Y.-S.
Choi
,
K.-W.
Seo
, and
S.-J.
Lee
, “
Lateral and cross-lateral focusing of spherical particles in a square microchannel
,”
Lab Chip
11
,
460
465
(
2011
).
10.
B.
Chun
and
A. J. C.
Ladd
, “
Inertial migration of neutrally buoyant particles in a square duct: An investigation of multiple equilibrium positions
,”
Phys. Fluids
18
,
031704
(
2006
).
11.
D.
Di Carlo
,
J. F.
Edd
,
K. J.
Humphry
,
H. A.
Stone
, and
M.
Toner
, “
Particle segregation and dynamics in confined flows
,”
Phys. Rev. Lett.
102
,
094503
(
2009
).
12.
S.
Lomholt
and
M. R.
Maxey
, “
Force-coupling method for particulate two-phase flow: Stokes flow
,”
J. Comput. Phys.
184
,
381
405
(
2003
).
13.
V.
Loisel
,
M.
Abbas
,
O.
Masbernat
, and
E.
Climent
, “
The effect of neutrally-buoyant finite-size particles on channel flows in the laminar-turbulent transition regime
,”
Phys. Fluids
25
,
123304-1
123304-18
(
2013
).
14.
D.
Mikulencak
and
J.
Morris
, “
Stationary shear flow around fixed and free bodies at finite Reynolds number
,”
J. Fluid Mech.
520
,
215
242
(
2004
).
15.
F. P.
Bretherton
, “
The motion of rigid particles in a shear flow at low Reynolds number
,”
J. Fluid Mech.
14
,
284
304
(
1962
).
16.
R.
Phillips
,
R.
Armstrong
,
R.
Brown
,
A.
Graham
, and
J.
Abbott
, “
A constitutive equation for concentrated suspensions that accounts for shear induced particle migration
,”
Phys. Fluids
4
,
30
40
(
1992
).
17.
M.
Han
,
C.
Kim
,
M.
Kim
, and
S.
Lee
, “
Particle migration in tube flow of suspensions
,”
J. Rheol.
43
(
5
),
1157
1174
(
1999
).
18.
D.
Semwogerere
,
J. F.
Morris
, and
E.
Weeks
, “
Development of particle migration in pressure-driven flow of a Brownian suspension
,”
J. Fluid Mech.
581
,
437
451
(
2007
).
19.

Note that in the concentrated case, the particle distribution in the channel center is thicker than a Dirac delta function. Some particle aggregation was observed (doublets or triplets formation) after the particles traveled towards the center, knowing that we checked the absence of aggregation in the region at the vicinity of the channel inlet for all run cases.

20.
X.
Shao
,
Z.
Yu
, and
B.
Sun
, “
Inertial migration of spherical particles in circular Poiseuille flow at moderately high Reynolds numbers
,”
Phys. Fluids
20
,
103307-1
103307-11
(
2008
).
21.
J. P.
Matas
,
V.
Glezer
,
E.
Guazzelli
, and
J. F.
Morris
, “
Trains of particles in finite-Reynolds-number pipe flow
,”
Phys. Fluids
16
(
11
),
4192
4195
(
1994
).
22.
Y. W.
Kim
and
J. Y.
Yoo
, “
The lateral migration of neutrally buoyant spheres transported through square microchannels
,”
J. Micromech. Microeng.
18
,
065015
(
2008
).
You do not currently have access to this content.