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Tracer Particles and Seeding for PIV
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Seeding particles for PIV
Proper tracer must be small enough to follow (trace)fluid motion and should not alter fluid or flow properties.
Proper tracer must be large enough to be visible bythe camera.
Uniform seeding is critical to the success ofobtaining velocity field. o seed particles! no data.
The seeding source must be placed cleverly so that the particles mi" with the flow well.
Particles with finite inertia are #nown to disperse non$uniformly in a turbulent flow! preferential concentration
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Seeding particles for PIV (cont%d)
The tracing ability and the dispersioncharacteristics depends on theaerodynamical characteristics of particles
and the continuous medium&
The visibility depends on the scatteringcharacteristics of particles.
The choice of optimal diameter for seeding particles is a compromise between twoaspects.
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Scattering characteristics of particles
'aser sheet leads to a low energy density
particle scattering efficiency is important&
'ight scattering capability $ scattering crosssection C s is defined as the ratio of the total
scattered power P s! to the laser intensity I 0
incident on the particle
I P
C s s =
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*"ample of scattering cross section (+)
The scattering cross section as a function of
the particle si,e (refractive inde" m-+.).
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*"ample of scattering cross section (/)
Diameter d p
Scattering cross section C s
Molecule
≈10-33m2
1µm C s≈(d
p /λ )4 ≈10-12m2
10µm C s
≈( d p
/λ )2 ≈10-9m2
Scattering cross section as a function of the
particle si,e
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0ie scattering of small particle (/)
'ight scattering by a + µm!
+ µm! and 4 µm glass
particle in water.
5efractive inde" m - +.6/
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Summary of particle light scattering
for PIV The ratio I s907 I s0 decreases with increasing si,e parameterd p7λ ! with values roughly in the range +$+$+$4 for scattering
particles useful in PIV.
The resulting intensity of the scattered light for a given lightsheet intensity will depend on the combined influences of C s
and I s907 I s0! which e"hibit opposing tendencies with
increasing particle si,e. In general! larger particles will still
give stronger signals.
The ratio I s907 I s0 increases with increasing refractive inde" m.
8ence particles in air gives stronger 9o scattering than in
water.
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Trac#ing characteristics of particles
The trac#ing ability depends on• Particle shape assumed spherical
aerodynamically e:uivalent diameter $ d p
• Particle density ρ p
• ;luid density ρ f and fluid dynamic viscosity µ or
#inematic viscosity ν - µ 7 ρ f
ewton%s 'aw governing the motion of a
single particle3 ∑=i
i
p p
p F dt
U d d
.
4π ρ
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added mass?)
V. @asset history integral resistance caused by theunsteadiness of the flow field.
∫ −+−−+−= t
t f p
p
f
f p
f p
p p
pt
d
d
V d d
dt
V d d
dt
U d d V d
dt
U d d
/+
)(/
4
./
+
.4
.
/
444
ξ
ξ
ξ πµρ
π ρ
π ρ πµ
π ρ
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Sto#es% drag law
The Sto#es% drag law is considered to apply when the
particle Reynolds number Re p is smaller than unity!
where Re p is defined as
In a typical PIV e"periment with +µm particles and
/ cm7s mean velocity!
Re p-+"+$ " ./ 7 +.2"+$6 - .+4 (air)&
Re p-+"+$ " ./7+."+$ - / (water).
ν µ
ρ p p f p
Vd Vd ==5e
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Particle parameter$ the particle response time τ p
Velocity lag of a particle in a continuously accelerating
fluid3
The particle velocity response to the fluid velocity if heavy
particles ( ρ pAA ρ f ) in a continuously accelerating flow is3
Particle response time3
dt
dU d U U V
f f p
p f p µ
ρ ρ
+B
)(/
−
=−=
−−=
p
f p t U t U τ
e"p+)(
µ
ρ τ
+B
/ p
p p d =
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Particle parameter
$ the Sto#es number St Sto#es number St as the ratio of the particle responsetime to the Colmogorov time scale3
St 3 the degree of coupling between the particle phase
and the fluid.
St → the particles behave li#e tracers
St →∞ the particles are completely unresponsive to the fluid
flow.
k pSt τ τ 7=
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Particle parameter
$ the characteristic fre:uency C In the case of gas flow where ρ pAA ρ f !
characteristic fre:uency of the particle
motion
Tracing ability in turbulence! ω c-/π f c
/+B p pd C ρ µ =
)7+(
+/
/
C u
u
c f
p
ω +=
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;igure of characteristic fre:uency
The response of particles in turbulence flow. (;rom 8aetig D!
Introductory on particle behavior IS'7=
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Particle si,e vs. Turbulence scale
Seeding particles need to be smaller than the
smallest turbulence scale if one wants to
identify all the structures in the vicinity of
the flow. The smallest fluid length scale is
called the Colmogorov length scale! and it is
related to the si,e of the smallest eddy.
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=dditional Gonsiderations
Particle seeding uniformity
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=dditional Gonsiderations (cont%d)
• Secure sufficient spatial detail in the flow field a higherconcentration of particles is generally needed with PIV thanwith 'EV! with which it is possible to wait indefinitely forthe arrival of a scattering particle in the probe volume.
• = uniform particle size is desirable in order to avoide"cessive intensity from larger particles and bac#groundnoise! decreasing the accuracy! from small particles.
• Particles that naturally e"ist in the flow seldom meet the
above re:uirements. 8ence! in PIV applications! it is oftennecessary to seed the flow with a chosen tracer particle. The particles are either premi"ed with the whole fluid (e.g.!
stirred ) or released in situ by a seeding source.
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Imaging of small particles
5elation between real particles and particle image recorded
in the camera can be analy,ed by the diffraction limited
imaging of a small particle
;or a given aperturediameter Da and wavelength λ !
the =iry spot si,e
adiff D f d I
x I 722./)(
ma"
λ =⇒=
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Imaging of small particles (cont%s)
Hith an imaging lens! the
diffraction$limited si,e3
*stimate of the particle
image diameter3//)( diff p d Md d +=τ
λ )+(22./ += M f d diff
f Z z
+++
=+
Z z M =
d p3 original particle diameter
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Seeding particles for PIV (li:uid flow)
Type 0aterial 0ean diameter in µmPolystyrene +$+
=luminum / $ F
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Seeding particles for PIV (gas)
Type 0aterial 0ean diameter in µmPolystyrene 0.5- 10
=luminum / $ F0agnesium / $ 6
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Gommercial seeding particles $ TSI
(http377www.tsi.com) Silicon Carbide: Suitable for measurements in li:uids andgases! silicon carbide particles have a narrow particle si,edistribution (mean diameter of +.6µm). Their high refractiveinde" is useful for obtaining good signals in water! even in
bac#scatter operation. They can also be used in hightemperature flows. Supplied as a dry powder! they can bemi"ed in li:uid to form a suspension before dispersing.
Titanium Dioxide: Titanium dio"ide particles (mean
diameter of ./µm) are usually dispersed as a dry powderfor gas flow measurement applications. The smaller particlesi,e ma#es titanium dio"ide attractive for high$speed flows.It can also be used for high temperature flows.
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Gommercial seeding particles $ TSI (
http377www.tsi.com) (cont%d) Polystyrene Latex3 Hith an e"tremely narrow si,edistribution (nominal diameter of +.µm)! polystyrene late"
(PS') particles are useful in many different measurements.
Supplied in water! they are not recommended for high
temperature applications.
Metallic coated: 0etallic coated particles (mean diameter
of 9.µm) are normally used to seed water flows for 'EV
measurements due to their lower density and higher
reflectivity. They cannot be used where salt is present. Saltreacts with the metal coating! causing the particles to
agglomerate and drop out of the flow.
http://www.tsi.com/http://www.tsi.com/
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Gommercial seeding particles $ TSI (
http377www.tsi.com) (cont%d)Particle
Type
MeanDia.(µm)
SizeRange(µm) Shape
Density(g/cc)
RefractiveInde(real)
RefractiveInde
(imag.)
Silicon carbide 1.5 Std. dev.= 1.4 Irregular 3.2 2.65 ---
Silicon dioxide 2.7 --- Irregular 2.3 1.47 ---
Nlon 4 Std. dev.= 1.5 S!"erical 1.14 1.53 ---
#S$ 0.54 Std. dev.= 1.05 S!"erical 1.05 1.55-1.6 ---
%itanium dioxide 3-5 --- Irregular 4.2 2.6 ---
&etallic coated ' 4-12 S!"erical 2.6 0.21 2.62
(ollo) gla**
*!"ere*+-12
10, 3-5
'0, 14-17S!"erical 1.05-1.15 1.5 ---
&etallic coated
(ollo) gla**
*!"ere*
1410, 7
'0, 21S!"erical 1.65 .21 2.62
http://www.tsi.com/http://www.tsi.com/http://www.tsi.com/http://www.tsi.com/
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Gommercial seeding particles $ Eantec
(http377www.dantecmt.com) Polyamide seeding particles PSP!: These are produced by polymerisation processes and therefore have a round but not e"actlyspherical shape. They are microporous and strongly recommended forwater flow applications.
"ollo# glass spheres and sil$er%coated hollo# glass spheres "&S' S%"&S!: Intended primarily for li:uid flow applications! these are borosilicate glass particles with a spherical shape and a smooth surface. =thin silver coating further increases reflectivity.
(luorescent polymer particles (PP!: These particles are based onmelamine resin. ;luorescent dye (5hodamine @3) is homogeneously
distributed over the entire particle volume. In applications with a high bac#ground light level! fluorescent seeding particles can significantlyimprove the :uality of vector maps from PIV and 'EV measurements. Thereceiving optics must be e:uipped with a filter cantered on the emissionwavelength (e"citation ma".3 66 nm& emission ma".3 69 nm).
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Gommercial seeding particles $ Eantec
(http377www.dantecmt.com) (cont%d) PSP
P!lyamide
seeding
particles
"#S
"!ll!$ glass
spheres
S%"#S
Silver%c!ated
h!ll!$ glass
spheres
&PP
&l'!rescent
p!lymer particles
&ean !article *i/e m5 20 50 10 10 10 30 75
Si/e di*tribution 1 - 10 m
5 - 35 m
30 - 70 m
2 - 20 m 2 - 20 m 1 - 20 m
20 - 40 m
50 - 100 m
#article *"a!e non-*!"erical but
round
*!"erical *!"erical *!"erical
en*it gcm3 1.03 1.1 1.4 1.5
&elting !oint 175 740 740 250
e8ractive index 1.5 1.52 9 1.6+
&aterial #olamide 12 :oro*ilicate gla** :oro*ilicate gla** &elamine re*in
ba*ed !olmer
http://www.dantecmt.com/http://www.dantecmt.com/
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Particle generation
'i:uid flow Simple! select proper powder then mi" w7 li:uid
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'i:uid droplets
=dvantage Steady production rate& Inherently spherical shape& Cnown refractive inde"
Problem ;orm non uniform li:uid films‑ on window