Extension of the compressed interferometric particle sizing technique for three

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13th Int. Symp on Appl. Laser Techniques to Fluid Mechanics, Lisbon, Portugal, June 26 – 29, 2006
Extension of the compressed interferometric particle sizing technique for three
component velocity measurements
Daisuke Sugimoto1, Konstantinos Zarogoulidis2, Tatsuya Kawaguchi3, Kazuaki Matsuura4,
Yannis Hardalupas2, Alex M.K.P. Taylor2, Koichi Hishida1
1: Department of System Design Engineering , Keio University, Yokohama, Japan, sugimoto@mh.sd.keio.ac.jp
2: Department of Mechanical Engineering, Imperial College, London, UK, konstantinos zarogouldis@imperial.ac.uk
3: Department of Mechanical and Control Engineering, Tokyo Institute of Technology, Tokyo, Japan, kawat@mep.titech.ac.jp
4: Japanese Aerospace Exploration Agency, Tokyo, Japan, matsuura.kazuaki@jaxa.jp
Keywords: Interferometric laser imaging technique, Sprays, Three–component velocity, particle sizing
The present contribution extends the presently planar
advanced interferometric laser imaging Droplet sizing
(ILIDS) with compression optics [1] to measure the
third–velocity component of particles in two phase flows.
Two different methodologies are examined to measure
the depth velocity, one employing just one camera and the
other a two–camera stereoscopic arrangement. For the
one–camera arrangement, the position of the droplet in the
laser sheet can be determined by the size of the fringe
pattern, since its size is dependant on the distance of the
droplet from the imaging lens and the size of the receiving
aperture. To correlate between the depth position and the
fringe pattern length, a monodisperse droplet generator is
traversed along the measurement volume and the particle
fringe patterns length in various positions in space is used to
interpolate a simple relationship function. In the stereoscopic
arrangement system, the physical space is mapped in image
space for both cameras by interpolating the nodes of a plain
two–sided calibration plate in simple mapping model
functions. Each particle is found in the two camera views by
validating the particle size information and the position
information that results from the calibration mapping models
of each individual camera.
Fig. 1 shows the schematic of measurement system for
the two-camera arrangement. It consists of two CCD
cameras positioned on Sheimpflug mounts, objective lens
with aperture mask and pair of cylindrical lenses. Since the
fringe length at one side of the image is longer than that at
the other side due to scattering angle, which is different than
90°, the Sheimpflug condition is applied. This condition
allows for rotation of the field of view, making the plane
imaged to be parallel to the central plane of the laser sheet
instead of parallel to the imaging array. The same system
was employed for the one-camera arrangement.
To validate the depth position calculation for both the
aforementioned methodologies, a monodisperse droplet
generator was positioned with a 75° inclination in respect to
the horizontal axis. For the one–camera case, a simple
second–order polynomial relation was fitted between the
depth and the fringe length. The fringe pattern length
changed from the one edge of the laser sheet to the other
smoothly, but the resulting depth resolution was found to be
low given the uncertainty fringe length pattern estimation. In
addition, the inclination of the particle stream was found to
be erroneous by 3.9%. For the stereoscopic case, this error
was 1.5% (Fig. 2). For both cases, the droplet sizing error
was 2.6% compared to the calculated theoretical size (Fig. 3).
The stereoscopic arrangement was also applied to a spray.
The results (Fig.4 and Fig. 5) showed that the method
enables us to apply to the measurements of size and
three-component velocity for the spray.
References
[1] Maeda et al. (2000), Meas. Sci. Technol., 11, L13-L18
Nd:YAG laser
Objective lens
y
z
Compression
optics
x
CCD camera
Sheimpflug condition
Fig. 1 Schematic of the measurement system
0.35
0.35
5(m/s)
0.3
y(mm)
6
Probability
2
0.25
0.25
0.2
0.15
0.15
0.1
0.05
0.05
10
0
100
6
100
120
140
140
160
180
180
200
Droplet diameter (μm)
m)
x( m
8
10
-1.5
0
z(mm)
14
1.5
Mean diameter = 163.2μm
Fig. 2 The instantaneous
three components velocity of
a 75° inclined monodisperse
droplet generator
Fig. 3 Probability density
function of the monodisperse
droplet generator
42
1(m/s)
46
54
58
12
16
1.5
z(m 0 -1
m) .5 28
20
24
m)
x(m
Fig. 4 The average three
components velocity of the
spray (d >40μm).
7.4
10
Probability
y(mm)
50
12
0.12
0.88
6
0.44
2
00
00
20
40
60
80
100
20
40
60
80
100
Droplet diameter (μm)
Fig. 5 Probability density
function of the spray
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