tracer particles and seeding for piv. seeding particles for piv proper tracer must be small enough...
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Tracer Particles and Seeding for PIV
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 by the camera.
Uniform seeding is critical to the success of obtaining velocity field. No seed particles, no data. The seeding source must be placed cleverly so that the
particles mix with the flow well. Particles with finite inertia are known to disperse non-
uniformly in a turbulent flow, preferential concentration
Seeding particles for PIV (cont’d)
The tracing ability and the dispersion characteristics depends on the aerodynamical characteristics of particles and the continuous medium; The visibility depends on the scattering
characteristics of particles. The choice of optimal diameter for seeding
particles is a compromise between two aspects.
Scattering characteristics of particles
Laser sheet leads to a low energy density – particle scattering efficiency is important;
Light scattering capability - scattering cross section Cs is defined as the ratio of the total scattered power Ps, to the laser intensity I0 incident on the particle
0IPC s
s
Example of scattering cross section (1)
The scattering cross section as a function of the particle size (refractive index m=1.6).
Example of scattering cross section (2)
Diameter dp Scattering cross section Cs
Molecule 10-33m2
1m Cs(dp/)4 10-12m2
10m Cs( dp/)2 10-9m2
Scattering cross section as a function of the particle size
Mie scattering of small particle (1)
Light Scattering by an oil particle in air when refractive index m ~ 1.4. Left: 1m diameter, right: 10m diameter
Mie scattering of small particle (2)
Light scattering by a 1 m, 10 m, and 30 m glass particle in water. Refractive index m = 1.52
Summary of particle light scattering for PIV
The ratio Is90/Is0 decreases with increasing size parameter dp/, with values roughly in the range 10-1-10-3 for scattering particles useful in PIV.
The resulting intensity of the scattered light for a given light sheet intensity will depend on the combined influences of Cs and Is90/Is0, which exhibit opposing tendencies with increasing particle size. In general, larger particles will still give stronger signals.
The ratio Is90/Is0 increases with increasing refractive index m. Hence particles in air gives stronger 90o scattering than in water.
Tracking characteristics of particles
The tracking ability depends on Particle shape – assumed spherical –
aerodynamically equivalent diameter - dp
Particle density p
Fluid density f and fluid dynamic viscosity or kinematic viscosity = /f
Newton’s Law governing the motion of a single particle:
ii
ppp F
dt
Udd
6
3
General governing equation
Meaning of each term:I. Viscous drag according to the Stokes’ lawII. Acceleration forceIII. Force due to a pressure gradient in the vicinity of the
particleIV. Resistance of an inviscid fluid to the acceleration of the
sphere (“added mass”)V. Basset history integral – resistance caused by the
unsteadiness of the flow field.
t
tfpp
ffp
fppp
pt
d
d
Vdd
dt
Vdd
dt
UddVd
dt
Udd
0
21
)(2
3
62
1
63
62
333
Stokes’ drag law
The Stokes’ drag law is considered to apply when the particle Reynolds number Rep is smaller than unity, where Rep is defined as
In a typical PIV experiment with 10m particles and 20 cm/s mean velocity,Rep=10x10-6 x 0.2 / 1.46x10-5 = 0.13 (air);Rep=10x10-6 x 0.2/1.0x10-6 = 2 (water).
ppf
p
VdVdRe
Particle parameter - the particle response time p
Velocity lag of a particle in a continuously accelerating fluid:
The particle velocity response to the fluid velocity if heavy particles (p>>f) in a continuously
accelerating flow is:
Particle response time:
dt
dUdUUV ffp
pfp
18
)(2
pfp
tUtU
exp1)(
18
2 ppp d
Particle parameter- the Stokes number St
Stokes number St as the ratio of the particle response time to the Kolmogorov time scale:
St: the degree of coupling between the particle phase and the fluid. St0 the particles behave like tracers
St the particles are completely unresponsive to the fluid flow.
kpSt /
Particle parameter- the characteristic frequency C
In the case of gas flow where p>>f,
characteristic frequency of the particle motion
Tracing ability in turbulence, c=2fc
218 ppdC
)/1(
12
2
Cu
u
cf
p
Figure of characteristic frequency
The response of particles in turbulence flow. (From Haetig J, Introductory on particle behavior ISL/AGRAD workshop on laser anemometry (Institute Saint Louis) report R 117/76, 1976)
Particle size 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 Kolmogorov length scale, and it is related to the size of the smallest eddy.
Additional Considerations
Particle seeding uniformity
Additional Considerations (cont’d)
Secure sufficient spatial detail in the flow field a higher concentration of particles is generally needed with PIV than with LDV, with which it is possible to wait indefinitely for the arrival of a scattering particle in the probe volume.
A uniform particle size is desirable in order to avoid excessive intensity from larger particles and background noise, decreasing the accuracy, from small particles.
Particles that naturally exist in the flow seldom meet the above requirements. Hence, in PIV applications, it is often necessary to seed the flow with a chosen tracer particle. The particles are either premixed with the whole fluid (e.g., stirred ) or released in situ by a seeding source.
Imaging of small particles
Relation between real particles and particle image recorded in the camera can be analyzed by the diffraction limited imaging of a small particle
For a given aperture
diameter Da and wavelength , the Airy spot size
adiff DfdI
xI/44.20
)(
max
Imaging of small particles (cont’s)
With an imaging lens, the
diffraction-limited size:
Estimate of the particle image diameter:
22)( diffp dMdd
)1(#44.2 Mfddiff
fZz
111
00
0
0
Z
zM
dp: original particle diameter
Seeding particles for PIV (liquid flow)
Type Material Mean diameter in m Polystyrene 10-100 Aluminum 2 - 7 Glass spheres 10-100
Solid
Granules for synthetic coatings 10-500
Liquid Different oils 50 - 500 Gaseous Oxygen bubbles 50-1000
Seeding particles for PIV (gas)
Type Material Mean diameter in m Polystyrene 0.5- 10 Aluminum 2 - 7 Magnesium 2 - 5 Glass micro-balloons 30-100 Granules for synthetic coatings 10-50
Solid
Dioctylphathalate 1-10
Smoke <1 Liquid Different oils 0.5 - 10
Commercial seeding particles - TSI (http://www.tsi.com)
Silicon Carbide: Suitable for measurements in liquids and gases, silicon carbide particles have a narrow particle size distribution (mean diameter of 1.5m). Their high refractive index is useful for obtaining good signals in water, even in backscatter operation. They can also be used in high temperature flows. Supplied as a dry powder, they can be mixed in liquid to form a suspension before dispersing.
Titanium Dioxide: Titanium dioxide particles (mean diameter of 0.2m) are usually dispersed as a dry powder for gas flow measurement applications. The smaller particle size makes titanium dioxide attractive for high-speed flows. It can also be used for high temperature flows.
Commercial seeding particles - TSI (http://www.tsi.com) (cont’d)
Polystyrene Latex: With an extremely narrow size distribution (nominal diameter of 1.0m), polystyrene latex (PSL) particles are useful in many different measurements. Supplied in water, they are not recommended for high temperature applications.
Metallic coated: Metallic coated particles (mean diameter of 9.0m) are normally used to seed water flows for LDV measurements due to their lower density and higher reflectivity. They cannot be used where salt is present. Salt reacts with the metal coating, causing the particles to agglomerate and drop out of the flow.
Commercial seeding particles - TSI (http://www.tsi.com) (cont’d)
Particle Type
Mean Dia. (µm)
Size Range (µm) Shape
Density (g/cc)
Refractive Index (real)
Refractive Index
(imag.)
Silicon carbide 1.5 Std. dev.= 1.4 Irregular 3.2 2.65 ---
Silicon dioxide 2.7 --- Irregular 2.3 1.47 ---
Nylon 4 Std. dev.= 1.5 Spherical 1.14 1.53 ---
PSL 0.54 Std. dev.= 1.05 Spherical 1.05 1.55-1.6 ---
Titanium dioxide 3-5 --- Irregular 4.2 2.6 ---
Metallic coated 9 4-12 Spherical 2.6 0.21 2.62
Hollow glass spheres
8-12 10% < 3-5
90% < 14-17 Spherical 1.05-1.15 1.5 ---
Metallic coated, Hollow glass spheres
14 10% < 7
90% < 21 Spherical 1.65 .21 2.62
Commercial seeding particles - Dantec (http://www.dantecmt.com)
Polyamide seeding particles (PSP): These are produced by polymerisation processes and therefore have a round but not exactly spherical shape. They are microporous and strongly recommended for water flow applications.
Hollow glass spheres and silver-coated hollow glass spheres (HGS, S-HGS): Intended primarily for liquid flow applications, these are borosilicate glass particles with a spherical shape and a smooth surface. A thin silver coating further increases reflectivity.
Fluorescent polymer particles (FPP): These particles are based on melamine resin. Fluorescent dye (Rhodamine B:) is homogeneously distributed over the entire particle volume. In applications with a high background light level, fluorescent seeding particles can significantly improve the quality of vector maps from PIV and LDV measurements. The receiving optics must be equipped with a filter cantered on the emission wavelength (excitation max.: 550 nm; emission max.: 590 nm).
Commercial seeding particles - Dantec (http://www.dantecmt.com) (cont’d)
PSP
Polyamide
seeding
particles
HGS
Hollow glass
spheres
S-HGS
Silver-coated
hollow glass
spheres
FPP
Fluorescent
polymer particles
Mean particle size (µm) 5, 20, 50 10 10 10, 30, 75
Size distribution 1 - 10 µm
5 - 35 µm
30 - 70 µm
2 - 20 µm 2 - 20 µm 1 - 20 µm
20 - 40 µm
50 - 100 µm
Particle shape non-spherical but
round
spherical spherical spherical
Density (g/cm3) 1.03 1.1 1.4 1.5
Melting point (°C) 175 740 740 250
Refractive index 1.5 1.52 — 1.68
Material Polyamide 12 Borosilicate glass Borosilicate glass Melamine resin
based polymer
Particle generation
Liquid flow Simple, select proper powder then mix w/ liquid
Gas flow liquid droplets
Atomization or Condensation solid particles
Atomization or Fluidization
Requirement for PIV Nearly monodisperse size distribution High production rate
Liquid droplets
Advantage Steady production rate; Inherently spherical shape; Known refractive index
Problem Form non‑uniform liquid films on window
Generator Laskin atomizer Commercial atomizer (e.g., TSI)