Chen Gang, Le Jing, Xu Lianfeng, Shao
Jianbin, Jin Shanghai and Li Jianzhong
Xi’an
University of Technology, China
Address
for correspondence: Professor GANG CHEN, The Institute of Hydraulics,
Xi’an
University of Technology, Xian, Shaanxi Province, 710048, China
Tel/Fax:
+86-29-3283506, E-mail: chen_g@mail.xaut.edu.cn
Abstract: Particle Image Velocimetry (PIV) and its image measurement techniques have been rapidly developed with the drastic development of image processing method and computers. As a tool for measuring the whole instantaneous flow field without contacting the flow, PIV and related image measurement techniques have been extensively applied to automated measurements of multiphase flows, turbulence and thermal flows with reliable accuracy. Related techniques and their applications are briefly reviewed in this paper.
Keywords: image measurement, Particle Image Velocimetry (PIV), multiphase
flow
It is well known that particles and dye materials seeded in a flow
can visualize the fluid flow. Pathline lengths or moving distances of all
particles in a whole flow field can be measured with particle images at a time
interval to derive velocity vector field. With this simple concept, an advanced
tool for automated measurement of fluid flow, called Particle Imaging
Velocimetry (PIV in acronym) has been developed with the noticeable development
of modern computer techniques. PIV has been used to measure instantaneous
velocity vector fields from slow flows to supersonic flows during the past ten
years (Adrian, 1991, Raffel & Kompenhans, 1995, Willert, et al, 1996, Dracos, 1996, Raffel,
et al, 1998). In contrast to the conventional methods
for one point measurement such as the Pitot tube, the hot wire anemometer and
the laser Doppler velocimeter, PIV can carry out two-dimensional and
three-dimensional instantaneous velocity measurement with contact free. The
velocity vector map obtained by PIV enables extraction of physical information
such as pressure field, vorticity field, etc.
Combining PIV algorithm and other image processing techniques, PIV measurement can be extended to research on the moving-boundary flows, multiphase flows and atomization in high-speed flows. A survey article of particle velocimetry confirms that PIV has been rapidly advanced in its fundamentals and applications to multiphase flows, thermal flows, turbulence structures, etc (Adrian, 1996). In the present paper, PIV with image measurement techniques is concisely reviewed.
In the previous researches, the method acquiring
velocities at grids using high-density distribution patterns of particle images
is referred to PIV, and the method using each particle tracking for low particle
number density is referred to PTV. In this paper, PIV is used as a general term
of the velocimetry using particle images. When particles have a good behavior of
traceability to a fluid flow, the particle velocities usually represent the
local fluid velocities. If the particles do not follow a flow, the particle
velocities do not represent the local fluid velocities.
It is known that there is not a general-use type of standard PIV system. Each type of PIV needs the fittest hardware and software to measure a flow field. Even though many types of PIV work in the present days, they include the common processes as the following operations: seeding the flow of fluid for visualization, illuminating the measurement space, photographing the visualized flow or recording the flow images digitally using a video system, and finally processing the recorded images to calculate flow velocity vectors. These operations consist of the following elements: tracer particles whose size is small enough to follow the concerning fluid flow with or without turbulence (several microns in diameters), light source for which a high power laser is usually used to illuminate the two-dimensional flow space as a thin light sheet, a charge-coupled device camera, i.e., CCD camera for recording the images and a digital image processor consisting of computer and its software. According to principles of flow velocity calculation based on the image processing, a classification of PIV is shown in Table 1.
Besides the PIV systems in Table 1, Holographic PIV (HPIV) (Meinhart,
et al, 1993, Barnhart, et al, 1995, Sheng & Meng, 1997, Meng, et al, 1997)
and Image-shifting PIV (IPIV) (Raffel & Kompenhans, 1995), both
of which belong to the optical method, have made an important contribution to
the recent flow measurement field. HPIV can track millions of particles in
three-dimensional space, which is much more than several hundred particles
seeded in other PIV techniques. The particle size for HPIV and IPIV must be
restricted to a few microns to avoid overloading the fluid. An advanced
algorithm is proposed to process larger set of data in HPIV at high speed than
the cross-correlation methods (Sheng & Meng, 1997). IPIV techniques are
especially effective for high-speed flows, which demand short time intervals of
the order of a few microseconds between the exposures. This may overcome the
demerit of high-framing-speed video techniques, which drastically impair the
spatial resolution in the PIV recordings. Most widely used image-shifting method
adopts a rotating mirror system (Raffel & Kompenhans, 1995). It permits
shift velocities exceeding 500m/s without any noticeable reduction in the
optical quality of the images (Raffel & Kompenhans, 1995).
Table 1 Some current PIV techniques
|
Classifications |
Principles |
Features, limits and Remarks |
|
Pathline (Dimotakis,
et al, 1981, Khalighi, 1989) |
Measurement of
particle pathline length |
Simple; High cost for ambiguity removal;Low image
density;Not suitable to automatic measurement of
large scale data |
|
Laser Speckle
Velocimetry(LSV) (Simpkins &
Dudderar, 1978, Kawahashi & Yamamoto, 1995) |
Young's fringe
in optical specklegram |
Small
computation in automatic evaluation system; Applicable to
high speed flow; More particles are needed
(Adrian, 1991); Direction ambiguity (Raffel
& Kompenhans, 1995); Difficult in
three-dimensional flow |
|
Particle
Brightness- distribution Pattern Tracking |
Maximum value of
cross-correlation coefficient (Adrian, 1991) |
Two frames; High image density; 2-D; Large computation; Most popular |
|
Minimum
quadratic difference (Gui & Merzkirch, 1996) |
Two-frames; High image density; 2-D |
|
|
Minimum sum of
absolute value of brightness difference (Kaga, et
al, 1994) |
Two-frames; High image density; 2-D |
|
|
Particle
Distribution Pattern Tracking |
Maximum value of
binary image cross-correlation coefficient (Uemura, et al, 1990, Yamamoto, et
al, 1996a, Yamamoto, et al, 1996b) |
Two frames; High-speed algorithm; 2-D and 3-D; Low image density |
|
Maximum value of
Delaunay triangle similarity coefficient (Song, et al, 1997) |
Two frames; High-speed algorithm; Applicable to
rotation; Low image density; 2-D; Delaunay tessellation is
unique and optimal triangular formation |
|
|
Spring Model |
Minimum force in
imaginary spring systems (Okamoto, 1995) |
Two frames; 2-D and 3-D; Applicable to
shear and rotation; Low image density |
|
Velocity
Gradient Tensor Method |
Minimum value of
a sum of squared particle distance (Ishikawa, et al, 1997) |
Two frames; 2-D and 3-D; Applicable to
shear and rotation; Low image density |
|
Particle
Trajectory Tracking |
Matching
probability (particles in a small region moving towards nearly the same
direction) (Baek & Lee, 1996) |
2 frames; Low image density; 2-D |
|
Smooth
trajectories (Nishino, et al, 1989) |
4 frames; 2-D and 3-D; Low image
density; Less spurious vectors |
|
|
Minimum change
in acceleration (Malik, et al, 1993) |
4 frames; 3-D; Low image density |
It is necessary to
extract physical information from velocity data. Velocity vectors are obtained
at particle positions when the tracking techniques are applied. They are
rearranged at needed grid points in order to calculate physical properties such
as stream function, vorticity and pressure. Three methods have been proposed by
Yamamoto et al (1996a), who introduced some numerical methods used in modern
computational fluid dynamics (CFD) to the rearrangement processing. Recently a
hybrid system combining PIV and CFD has also been reported by his group (Ido, et
al, 1997). Their hybrid system was developed to restore the velocity vectors in
the flow regions in which velocity information lacks. The original velocity
vectors obtained from PIV measurement are not changed in this disposal process.
For this purpose, any basic relations and models in fluid dynamics, such as
continuity equation and Laplace equation, and some numerical methods in CFD can
be adopted justifiably in the hybrid system.
Visualization techniques are often concerned in image
measurement. Visualization techniques, such as the methods using oil film, dye
materials and tracer particles, are often utilized to show physical structures
of flows including vortex sizes, separation positions on solid walls, and also
distributions of bubbles and particles. Visualized images can be analyzed using
image processing techniques to obtain some quantitative information.
Multiphase
flows can be diagnosed by video cameras and image processing. Flow images may be
recorded by ordinary charge coupled digital cameras and high-speed video cameras
with frame rates up to several thousands fps, and the
recorded images can be analyzed by PIV and image
processing techniques (Hewitt, et al, 1990, Reese, et al,
1995, Crowe et al, 1998). Multiphase
flow parameters, such as void fraction in gas-liquid flow, particle
concentration in gas-solid and liquid-solid flow can be extracted by PIV
techniques. For instance, a paper on simultaneous velocity measurements of both
components of a gas-liquid two-phase flow by PIV was reported (Hassan, et al,
1992). This process contains a separation treatment of overlapped deformable
bubbles and drops with edge detection (Yamamoto, et al, 1997, Canny, 1986), and
also includes separation between tracer particles and bubbles (drops and
particles) in multiphase systems (Song, et al, 1996). PIV measurement of
three-dimensional distribution of void fraction in bubble plume flow was
reported by Murai et al (1997). Yamamoto et al (1997) also investigated particle
number flow rate measurement with PIV. Recently, PIV and image measurement
techniques were also used to investigate high-efficiency sand transportation
with spiral air flows in pipeline. Particle moving behaviors and sand plug
features can be analyzed by image measurement techniques (Miyazaki, et al,
1999a and 1999b).
Shockwave
in air-water flow can be shown by visualization. Photographs allow a comparison
between aerated and non-aerated flows across a shock, and show a detail of the
shock front in the direction of flow (Reinauer and Hager, 1996). For studying
the effects of surface disturbances on the entrainment of bubbles by a liquid
jet, a digital CCD camera with a resolution of 780X480 pixels for recording images
and a strobe for illumination were used, and bubble size distributions were
obtained by analyzing the recorded images using some image processing algorithms
(
, 1998). Turbulence generation due to breaking water waves was investigated
using the techniques of visualization and PIV. The periodicity of the breaking
waves, mean velocities and turbulence intensities based on repeated measurements
were obtained (Chang and Liu, 1999). The phenomenon of a liquid jet released
under gravity and falling through or impacting onto another liquid before
colliding with an obstructing solid surface can be studied with visualization
techniques, and the volume of air entrained can be estimated from photographs by
measuring the sizes of the air bubbles using image processing algorithms (Storr
and Behnia, 1999).
Thermo-sensitive tracer particles are usually
used for simultaneous measurement of velocity and temperature in a thermal flow.
Temperature field is obtained by calculating the intensity of colors on the same
particle images used to calculate velocity. Optical properties and time response
of the tracer particles should be checked beforehand. Sometimes two kinds of
particles are used in the same flow: one is for velocity tracking and the other
for temperature detection. A technique using thermo-sensitive micro-capsulated
liquid crystal particles suspended in liquid was proposed by Kobayashi et al
(1992). This technique was applied to a thermal buoyant water jet (Kobayashi, et
al, 1995). Kimura et al (1997) reported that three-dimensional temperature
distribution could be constructed by interpolating two-dimensional
distributions, which adopted a color-to-temperature transformation algorithm
using a multi-layer feed-forward neural network in investigating natural
convection in a rotating cylindrical cell. An analysis of buoyancy and
thermocapillary flow was made using PIV with liquid crystal tracers (Wozniak
& Wozniak, 1994). PIV application to natural convection in water heat
storage vessel was also reported (Dahl, et al, 1995).
In separation flows, particles must be carefully
seeded in a shear layer so that a separation region may contain a satisfactory
number of particles. Rearrangement of velocity vectors from particle points to
grid points becomes necessary for revealing some flow phenomena because of the
lack of effective particle images in these regions. An investigation into the
separation flow around airfoil shows that velocity data may miss from some
critical regions on the PIV pictures. But calculation of the out-of-plane
vorticity contours from the acquired PIV velocity fields allows details of the
structure and locations of the vortices involved in a thin reverse-flow layer on
the airfoil upperside (Wernert, 1996). Backward-facing-step flows were
successfully measured to determine vortex structure in the recirculating region
with hydrogen bubbles and oxygen bubbles as tracers (Ma, et al, 1995). Recently
microburst, which is modeled by releasing a small volume of heavy fluid into a
large tank filled with a lighter fluid, was measured with PIV including the
effect of the difference of refractive indices due to density differences up to
4%, and vortex structure was detected (Alahyari & Longmire, 1994).
Turbulence measurement is a challenge to PIV.
Particle traceability and measurement accuracy are important problems to be
solved in turbulence measurement. As one of the most fundamental flows,
turbulent boundary layer was measured by the PIV technique. About one hundred
frames were averaged to construct the velocity distribution in the logarithmic
region. Plots of the fluctuation quantities and Reynolds stresses demand over
one thousand of frames for reliable statistics (Willert, et al, 1996).
Feasibility of a PTV technique reported by Malik et al (1993) permits a change
of search radius in a target frame based on the turbulent velocity fluctuation
in rms (root mean square). In the measurement of turbulence in a channel,
accuracy of fluctuating velocity may reach 1% of the full-scale mean velocity,
and the encouraging good agreement of the accuracy with LDV measurements and
direct numerical simulations was reported (Adrian, 1991).
Image
measurement techniques also play an important role in the study of atomization
flows. By photographing the prototype flow patterns of
jet nappe atomization of a large hydropower station, images of flow patterns of
atomization can be obtained. The atomization images were analyzed with digital
image processing techniques. Assuming image brightness is proportional to
atomization intensity or density of droplet number, one can evaluate
distribution contours of atomization intensity by calculating brightness contour maps (Hu,
1994). It is also possible to evaluate distribution contours of
atomization intensity in a three-dimensional space by processing flow images
using the method of three-dimensional reconstruction (Zhou, et al, 1995). Instantaneous break-up process of a round
water jet by a high-speed annular air jet was visualized to study the underlying
physical mechanisms involved in the primary break-up of the water jet.
Visualization revealed that the break-up process consists of the stripping of
water sheets, or ligaments, which subsequently break into smaller lumps or drops
(Lasheras, Villermaux and Hopfinger, 1998).
It is
undoubted that PIV and image measurement techniques are extensively applied to
fluid dynamics, and contribute to modern experimental fluid mechanics.
Algorithms of PIV basically contains correlation method and particle tracking
method. It is also important to develop the techniques for delecting spurious velocity vectors and extracting physical
informations such as vorticity, pressure and stream function. The function of
PIV has been rapidly extended to measure multiphase flows using image processing
techniques in recent years. We can expect that PIV and image measurement method
will play an important role in the future development of modern hydraulics.
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* This research supported by the National Natural Science Foundation of China (Grant No:50079020 ) and the Education Office of Shaanxi Province (Grant No:00JK190).