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Mixing of high-Schmidt number scalar in regular/fractal grid turbulence: Experiments by PIV and PLIF. Y. Sakai*, K. Nagata*, H. Suzuki*, and R. Ukai* * Department of Mechanical Science and Engineering, Nagoya University. - PowerPoint PPT Presentation
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Mixing of high-Schmidt number scalarin regular/fractal grid turbulence: Experiments by PIV and PLIF
Y. Sakai*, K. Nagata*, H. Suzuki*, and R. Ukai** Department of Mechanical Science and Engineering, Nagoya University
<Contents>1. Introduction --- Background, Motivation and Purpose
2. Experimental apparatus and conditions
PIV (Particle Image Velocimetry)
PLIF (Planer Laser-Induced Fluorescence
3. Results and Discussions
4. Conclusions
1. Introduction (1)
The turbulent mixing phenomena can be observed in many industrial and natural flows
e.g. chemical reactor, combustion chamber, pollutant diffusion, etc.
(Hill, 1976)
(Fantasy of Flow, 1993)(Tominaga, et.al., 1976)
The understanding the physics of turbulence and mixing phenomena is very important to the engineering application, e.g., the design of high efficient inner mixer.
Recently, a research group of Imperial college has discovered a “new” turbulence, so called a “fractal/multiscale-generated turbulence”.
D.Hurst & J.C. Vassilicos, Phys. Fluids, vol.19, 035103 (2007)
R.E. Seoud, J.C. Vassilicos, Phys. Fluids, vol.19, 1015108 (2007)
N. Mazellier & J.C. Vassilicos, Phys. Fluids, vol.22, 075101 (2010)
J.C. Vassilicos, Phys. Letters A, vol.375 (2010), pp.1010-1013.
P.C. Valente & J.C. Vassilicos, J.Fluid Mech., submitted
which can be described by the self-preserving single-length scale theory (W.K. George & H.Wang, Phys. Fluids, vol.21, 025108 (2008)).
1. Introduction (2)
1. Introduction (3)
The low-blockage space-filling fractal turbulence has the following properties
(1) very much higher turbulence intensities u’/U and Reynolds number Reλ than regular grid turbulence
(2)Exponential decay law of turbulence intensity
N. Mazellier & J.C. Vassilicos, Phys. Fluids, vol.22, 075101 (2010), Fig.5
: wake-interaction length scale
L0: biggest bar length of the grid
t0: the biggest bar thickness of the grid
L0
t0
L0
t0
x*
1. Introduction (4)
(3) Integral length scale Lu and the Taylor length scale λ are independent
of the downstream position x and also Reλ
R.E. Seoud & J.C. Vassilicos, Phys. Fluids, vol.19, 105108 (2007), Fig.2 and Fig.9
Lu ~ L0, λ ~ L0Re0-1/2 , Lu/λ ~ Re0
1/2
where Re0=U∞t 0 /ν
Lu and λ are determined only by the initial conditions
1. Introduction (5)
(4) Kinematic dissipation rate εis proportional to u’2 rather than u’3 !
R.E. Seoud & J.C. Vassilicos, Phys. Fluids, vol.19, 105108 (2007), Fig.10.
32*
1 0 0
~ 3 ~ ,
~ Re ~
uu U x C u Lt LCu U
This characteristic means the lower dissipation with the same turbulence intensityas compared with the normal regular grid turbulence.
These properties (1) ~ (4) lead to the possibility of “high efficient industrial mixer”“to generate an intense turbulence with the reduced dissipation and even design the level of turbulence fluctuation” (Mazellier & Vassilicos, 2010)”
1. Introduction (6) : purpose of this study Page 8
Note : all the data processing systems of PIV and PLIF have been developed in our laboratory by my collaborators and students.
In order to develop the innovative industrial mixer (Fractal super mixer), we investigate the diffusion and mixing process of high-Schmidt number scalar in regular/fractal grid turbulence of the liquid phase by the PIV and PLIF technique.
2. Experimental apparatus and conditions
Page. 9
100 mm
1500 mm
100 mmHigh-Sc-number scalar
Contraction
Splitter plate
Flow
Grid
xz
y
Laser
Camera
PC
Lens
Optical filter
Regular grid
Fractal grid
PIV PLIF
Camera
Measuring area [mm2]
High speed camera(Ametek Phanton V210)
7.5(x) x 40(y)
Single-lens reflex camera (Nikon D700)
25(x) x 100(y)
Sampling frequency [Hz] 2,000 ---Sampling resolution [mm2]Thickness of sheet [mm]
0.4(x) x 0.4(y)1.0
0.03(x) x 0.03(y)0.5
Rohdamine B
Sc 2,100
Schmidt Number
effRe 2,500M
Configurations of Regular/Fractal Grids Page. 10
Parameters for regular/fractal grids are as follows,
N : number of fractal iterations Df : fractal dimension
s : blockage ratio tr : thickness ratio of the largest to the smallest barMeff : effective mesh size
T 2 : Area of the tunnel’s cross section [m2]PM: Fractal perimeter’s length [m]
12
34
フラクタル次元
Df = 1.5 Df = 2.0
minmax tttr tmaxtmin
Parameter Regular grid
Fractal grid
N 1 4
Df 2.0 2.0
s 0.36 0.36
tr 1 9.76
Meff 10[mm] 5.68[mm]
24 1effM
TMP
s
ReMeff=U0Meff/ν =
2,500
Image processing for PIV Page. 11
Taking images
Digitizing
Removing back ground level
Fourier interpolation to obtain 16 times number of pixcels
1st stage
Offset cross-correlation analysisRemoving error vectors
2nd stage (in the smaller interrogation region)
Recursive cross-correlation procedure × 2 stages
Obtain velocity vectorsGradient method(sub pixel analysis)
Polyester particles: Mean diameter 50mm Specific gravity 1.03 over 7 particles in the interrogation region
ReM = 2500x/Meff = 20
Checking accuracy of data-processing by comparison of thepresent data with the LDV result
100 101 102 10310-5
10-4
10-3
10-2
10-1
Present LDV
k [1/m]E u
u
x 3 times
Offset cross-correlation analysisRemoving error vectors x 3 times
Image processing for PLIF Page. 12
PLIF processing
1. Digitizing2. Correction by the back ground image3. Applying the improved algorithm*
Measured image back ground image Non-dimensional images
Camera
Bit depth : 14bitsSensor : full size CMOS sensor
Single-lens reflex camera (Nikon D700)
Time variations of quantum yield and laser intensitySpatial decay of laser intensity
Reference: * Suzuki,H., Nagata,K., Sakai,Y., Ukai,R., Experiments in Fluids, submitted
Good S/N ratioLarge dynamic rangeHigh sensitivity
1
0
t1 t2
Change of luminance atdifferent times
Page. 13
3. Results and Discussions
3.1 Results by PIV
Page. 14
-2 -1 0 1 20.4
0.6
0.8
1
1.2
1.4
y/M
U/U
0
x/M= 40 x/M= 60 x/M= 80 x/M=100 x/M=120
-1 0 10.4
0.6
0.8
1
1.2
1.4
x/M=10 x/M=15 x/M=20 x/M=30 x/M=40
y/M
U/U
0
Regular grid Fractal grid
Vertical profiles of mean streamwise velocity U
M=Meff M=Meff
For fractal grid turbulence, x/Meff >40
The profile becomes uniform
Instantaneous fluctuating velocity vector fields Page. 15
y/Meff
-2
0
2
y/Meff
-2
0
2
Regular grid turbulence x/Meff = 40
Fractal grid turbulence x/Meff = 40
tU0/Meff
tU0/Meff
Fluctuating velocities in the fractal grid turbulence are much larger than in the regular grid turbulence
0.00.15
101 10210-4
10-3
10-2
10-1
x/Meff
u rm
s2 /Uo2
Run RGT (PIV: present) Run FGT (PIV: present) regular grid turbulence (DNS: Suzuki, et al., 2009) fractal grid turbulence (DNS: Suzuki, et al., 2009)
Downstream variations of turbulent fluctuation relative intensity urms2/U0
2
Fluctuation intensity of fractal grid turbulence is much largerthan that of regular grid turbulence
Decay law for turbulence relative intensity
10110-4
10-3
10-2
10-1
x/Meff
u rm
s2 /U02
2 20
n
rms effu U a x M
1.19n 0.077a
0.2 0.4 0.6 0.8 1 1.210-3
10-2
x / x*
u rm
s2 / Uo2
Run FGT (PIV: present)
urms2/ Uo
2 = A exp{- B(x/x*)} A = 0.037 B = 2.16
Regular grid Fractal grid
Power decay law
exponential decay law
: wake-interaction length scale (N. Mazellier & J.C. Vassilicos, 2010)
Page. 20
101 102
10-1
100
x/M
x /
M
RegularFractal
101 10210-1
100
101
x/M
L u /
M
RegularFractal
101 102100
101
RegularFractal
x/Meff
L u / x
Downstream variations of the length scales, Lu, λx and their ratio Lu/λx
x/Meff x/Meff
L u/Mef
f
λ x/Mef
f
For regular grid, Lu,λx and Lu/λx
gradually increase in the downstream direction.
For fractal grid, Lu, λx and Lu/λx are almost constant.
101 1020
50
100
x/M
Re
RegularFractal
Downstream variations of the Taylor scale turbulence Reynolds number Reλ
Reλ in the fractal grid turbulence is around 60-120,
whereas Reλ in the regular grid turbulence is around 20-30.
High Reλcan be realized by the fractal grid.
3.2 Results by PLIF
Checking of accuracy of PLIF data-processing system Page. 23
(1) Ito, Y., et al., The effects of high-frequency ultrasound on turbulent liquid mixing with a rapid chemical reaction, Physics of fluids , 2002, 14, pp. 4362-4371
ref.
The present results by the improved data-processing system show a good agreement with the results by the single-point LIF results.
Regular gridMeff= 20mm
-2 -1 0 1 2
0
0.5
1 本研究 背景画像の処理のみ Ito et al.(1)
〈C〉
y/M-2 -1 0 1 2
10-3
10-2
10-1
y/Mk c
本研究 背景画像の処理のみ Ito et al.(1) Present
only back-ground correction Ito et al.(1)
Present only back- ground correction Ito et al.(1)
y/Meff y/Meff kc=(1/2)<c2>
Instantaneous fluctuating concentration field
Grid turbulence Fractal grid turbulence
Red: c = 0.3, Blue: c = -0.3. Note: Meff = 10 mm for the regular grid Meff = 5.68 mm for the fractal grid
Downstream variation of vertical profile of mean scalar Page. 25
Fractal
Regular
The gradient of mean scalar profile for fractal grid is smaller than the one for regular grid turbulence
0.5
0.25
0.75
M=Meff
M=Meff
M=Meff
Half-width hm show the much larger values for fractal grid than ones for regular grid.
Eddy diffusivity is about 4 times!
Downstream variation of vertical profile of scalar variance: kc=1/2<c2>
The widths of vertical profile for FG are much larger than the ones of RG.
Notice that in case of FG, from x/Meff=100 to 120, kc decreases rapidly.
Fractal
Regular
0 50 1000
2
4
6
8
x/M
h f /
M
RegularFractal
M=Meff
M=Meff
M=Meff
Mixing has been enhanced at around x/Meff=100
Meff L0[mm] t0[mm] x*[mm]Regular 10 10 2 50
Fractal 5.68 53.1 4.9 575.43
10-1 100 10110-2
10-1k c
x/x*
Regular Fractal
Downstream variations of kc on the centerline of mixing layer
x*: the wake-interaction length scale
* 101 effx M
What happensat around x*?
Fractal dimension of iso-scalar surface
100 101 102 103100
101
102
103
104
[pixel]
N(
)
Ct=0.1 Ct=0.2 Ct=0.3 Ct=0.4 Ct=0.5 Ct=0.6 Ct=0.7
-1.45
tshm
100 101 102 103100
101
102
103
104
105
Ct=0.1 Ct=0.2 Ct=0.3 Ct=0.4 Ct=0.5 Ct=0.6 Ct=0.7
ts
hm
-1.55
[pixel]
N(
)
Regular grid Fractal gridx/Meff=10 x/Meff=80
fDN k Df : fractal dimension
ts: thickness of the laser sheet, hm: half-width of the mean scalar profile
Ct: threshold of the scalar value
Downstream variation of Df
0 0.2 0.4 0.6 0.8 10
1
2
Ct
Df
x/M=10 x/M=20 x/M=30 x/M=40
0 0.2 0.4 0.6 0.8 10
1
2
x/M= 20 x/M= 40 x/M= 60 x/M= 80 x/M=100 x/M=120
Ct
Df
Regular grid Fractal grid
Regular grid: Df does not change in the downstream direction
M=MeffM=Meff
Fractal grid: Df becomes large in the downstream direction
Mixing is progressing in the downstream direction in the Fractal grid turbulence
Conclusions
1. We could develop the reliable data-processing system of PIV and PLIF in our laboratory.
In this research,
2. It is reconfirmed that the fractal grid turbulence is much stronger as compared with the classical grid turbulence at the same mesh Reynolds number.
3. Diffusion and mixing of passive scalar in the fractal grid turbulence is extensively enhanced in comparison with that in the regular grid turbulence
the fractal grid turbulence : Reλ= 60-120.the classical turbulence. : Reλ= 20-30 .
Re 2,500effM
Eddy diffusivity of FGT is about 4 times as large as the one of RGT
These results are useful to the design of Fractal Super Mixer with high turbulence and low dissipation
Thank you very much for your attention !