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Kármán-Howarth closure equation on the basis of a universal eddy viscosity
F. Thiesset, R. A. Antonia, L. Danaila, L. Djenidi
To cite this version:
F. Thiesset, R. A. Antonia, L. Danaila, L. Djenidi. Kármán-Howarth closure equation on the basis
of a universal eddy viscosity. Physical Review E : Statistical, Nonlinear, and Soft Matter Physics,
American Physical Society, 2013, 88 (1), pp.011003. �10.1103/PhysRevE.88.011003�. �hal-01660256�
F. Thiesset, 1 R. A. Antonia, 1 L. Danaila, 2 and L. Djenidi 1
2
1
School of Engineering, University of Newcastle, NSW 2308 Callaghan, Australia
3
2
CORIA, UMR 6614, Avenue de l’Universit´ e, BP 12, 76801 Saint Etienne du Rouvray, France
4
The K´ arm´ an-Howarth equation [1] can be written in
5
terms of velocity structure functions [2]
6
3∂ t (∆u) 2 = 1 r 4 ∂ r
h r 4
6ν∂ r (∆u) 2 − (∆u) 3 i
− 4. (1)
∆u = u(x + r) − u(x) is the longitudinal velocity incre-
7
ment between two points separated by a distance r and
8
∂ α • = ∂•/ ∂α. Further, = 15ν(∂ x u) 2 , is the mean dissi-
9
pation rate with ν the kinematic viscosity and the over-
10
bar denotes averaging. Second- and third-order struc-
11
ture functions (∆u) 2 and (∆u) 3 appearing in Eq.(1) are
12
usually interpreted as the kinetic energy and the kinetic
13
energy transfer at a given scale respectively, two crucial
14
quantities for modelling turbulent flows.
15
In spectral space, the equivalent equation known as
16
Lin’s equation [3] reads
17
∂ t E(k) = T (k) − 2νk 2 E(k), (2) in which E(k) is the 3D energy spectrum, k the wavenum-
18
ber and T (k) the spectral energy transfer function.
19
Eq.(2) describes essentially the same physical mechanism
20
as Eq.(1), i.e. the decay, the transfer and the dissipation
21
of energy at a given scale or wavenumber.
22
In the last fifty years, several closures of Eq.(2)
23
have been developed and are still extensively employed.
24
Among others, we can cite the Direct Interaction Ap-
25
proximation model (DIA) proposed by Kraichnan [4] or
26
the Eddy Damped Quasi Normal Markovian (EDQNM)
27
closure [5].
28
On the contrary, closures of Eq.(1) have not received
29
the same attention. To our knowledge, Millionshchikov
30
[6] (in Russian), Domaradzki & Mellor [7], Effinger
31
& Grossmann [8], Oberlack & Peters [9] and Baev &
32
Chernykh ([10] and references therein) are the only au-
33
thors who proposed a model (sometimes identical) for
34
(∆u) 3 . All of them are based on the concept of an eddy-
35
viscosity ν t , i.e. Eq.(1) is then formally rewritten as
36
3∂ t (∆u) 2 = 1 r 4 ∂ r
h r 4 6 (ν + ν t ) ∂ r (∆u) 2 i
− 4. (3) The third-order structure function is thus related to ν t
37
and (∆u) 2 through
38
(∆u) 3 = −6ν t ∂ r (∆u) 2 , (4) where ν t is a function of the separation r. Domaradzki
39
& Mellor [7] proposed an expression for ν t on the basis
40
of inertial range asymptotic relations (R λ → ∞, where
41
R λ = p
u 2 λ / ν is the Reynolds number based on the
42
Taylor microscale λ ≡ q
15νu 2 /). However, as men-
43
tioned by the authors, the latter expression was not con-
44
sistent with the scaling (∆u) 3 ∝ r 3 as r goes to zero. This
45
constraint led Oberlack & Peters [9] to handle another ex-
46
pression for ν t , consistent with both dissipative and iner-
47
tial range scaling laws. Here again, ν t was parametrized
48
through a constant (called κ 0 in their paper) the value of
49
which relies on asymptotic inertial laws. Even though the
50
use of asymptotic relations may be questionable in the
51
context of finite Reynolds numbers flows (for instance,
52
see [11] and references therein), both models were in sat-
53
isfactory agreement with the third-order correlation func-
54
tions measured by Stewart & Townsend [12] at (very) low
55
Reynolds numbers (R λ < 60).
56
This intriguing feature indicates that the assumption
57
of infinite Reynolds numbers is not a necessary condition
58
for asymptotic expressions of ν t to be employed. There-
59
fore, there is matter for investigating the approach to-
60
wards the asymptote and the universal properties, i.e.
61
the flow and R λ -dependence, of the turbulent eddy-
62
viscosity, with the goal of providing an efficient simple
63
closure scheme in physical space.
64
The results presented in this paper highlight that the
65
Kolmogorov normalized eddy-viscosity reveals a remark-
66
able degree of universality over a wide range of scales.
67
An analytical expression for ν t is provided revealing the
68
existence of two universal parameters, the skewness of
69
velocity derivative S and a new scale of turbulence called
70
r c . In the inertial range and beyond, ν t closely follows the
71
asymptotic scaling even though neither (∆u) 2 nor (∆u) 3
72
indicate any unambiguous scaling. We then take advan-
73
tage of these properties to model the third-order struc-
74
ture functions in different decaying flows, for Reynolds
75
numbers R λ lying between 50 and 1100. Finally, the
76
model is numerically time-integrated to predict the decay
77
of second-order structure functions and compared to ex-
78
periments in grid turbulence (R λ ≈ 50) for downstream
79
distances up to 80M (M is the grid mesh size).
80
In order to derive an analytical expression for ν t , we
81
first recall that at small scales, (∆u) 2 = r 2
15ν and
82
(∆u) 3 = −S r 2 / 15ν 3/2
. S = − (∂ x u) 3 . h
(∂ x u) 2 i 3/2
83
is the skewness of the longitudinal velocity derivative
84
with respect to the longitudinal direction x. It follows
85
that in the dissipative range
86
ν t
ν = S 12 √
15 r ∗ 2 . (5)
Hereafter, the asterisk denotes normalization by the Kol-
87
mogorov scales, i.e. r ∗ = r/η with η = ν 3 / 1/4
. Sec-
88
ond, in the context of infinite Reynolds numbers and for
89
2 scales in the range η r L (L is the integral length-
90
scale), (∆u) 2 = C u (r) 2/3 and (∆u) 3 = −A u r (C u = 2,
91
A u = 4/5 [13]). Hence, in the inertial range
92
ν t
ν = 1
5C u r ∗ 4/3 . (6)
Equation (6) was already proposed by Domaradzki &
93
Mellor [7], even though we became aware of this after we
94
derived it. Following e.g. [14], we match Eqs.(5) and (6)
95
into a single expression
96
ν t
ν = Sr ∗ 2 12 √
15
1 + γr ∗ 2 1/3 . (7) Equation (7) generalizes the expression of [7] by covering
97
both dissipative and inertial ranges. In Eq.(7), the cross-
98
over length-scale between dissipative and inertial range
99
r 2 c = 1/γ is determined by equating Eqs.(5) and (6),
100
yielding r c ∗ = 12 √ 15
5C u S 3/2
. As for the EDQNM
101
spectral closure, dissipative and inertial range intermit-
102
tency effects are not taken into account in the present
103
analysis. According to the Kolmogorov theory [13], S,
104
C u and consequently r ∗ c are universal. However, in the
105
context of finite Reynolds number flows, S and r c ∗ are (a
106
priori) two free parameters. In the following, we turn our
107
attention to their evolution with respect to the Reynolds
108
number.
109
The analytical expression for ν t (Eq.(7)) is thus com-
110
pared to the one inferred from experiments in grid, wake,
111
round and plane jet turbulence. The Reynolds number
112
is in the range 50 ≤ R λ ≤ 1100. The grid turbulence
113
experiments are described in [15]. The wake flow facility
114
is described in [15] while experiments in the round and
115
plane jets are outlined in [15]. For the wake, round and
116
plane jet experiments, the measurements were made at
117
the centerline, thus avoiding to account for any additive
118
production terms in Eq.(1) due to the mean shear.
119
The dependence on Reynolds number of the measured
120
the eddy-viscosity is presented in Fig.1(a). At small
121
scales (r ∗ . 10), all experimental points converge onto
122
a single curve which is well represented by Eq.(5) with
123
S = 0.424 (Fig.1(a)). The value of S used here is the
124
mean value between the five experiments. S varies by
125
only 5% from one experiment to another. This indicates
126
that the skewness of the velocity derivative S remains
127
constant in agreement with the Kolmogorov theory [13].
128
For the range of Reynolds numbers investigated, the ef-
129
fect of internal intermittency on S [16] is not discernible.
130
Both the constancy and the value itself of S are quite
131
consistent with all experimental values compiled by [17],
132
at least for the same range of Reynolds numbers. Fur-
133
ther, it is in perfect agreement with EDQNM [16].
134
As we progress through to the larger scales (10 . r ∗ .
135
10 2 ), even though second-(not shown) and third-order
136
structure functions (Fig.1(b)) become R λ -dependent, the
137
eddy-viscosity ν t follows the same evolution indepen-
138
dently of the Reynolds number. In other words, the
139
Kolmogorov normalized eddy-viscosity collapse over a
140
10
010
110
210
310
410
−210
010
210
4r
∗= r/η ν
t/ ν
Grid R
λ= 50 Grid R
λ= 100 Wake R
λ= 230 Rd Jet R
λ= 495 Pl Jet R
λ= 1100 Asymptotic relation r
∗c= 25 10
010
110
210
30,05 0.1
(a)
10
010
110
210
310
40 0.2 0.4 0.6 0.8 1
r
∗= r/η
(∆ u )
∗3/ r
∗4/5
(b)
FIG. 1. (a) ν
t/ν as a function of r
∗measured in dif- ferent flows (50 ≤ R
λ≤ 1100). Eq.(7) (dashed line), Eq.(7) with r
c∗= 25 (solid line). The inset depicts the compensated eddy-viscosity (ν
t/ν)/r
∗4/3. (b) Kolmogorov- normalized third-order structure functions. Symbols are the same as in Fig.1(a), solid lines represent the present model using r
∗c= 25
wider range of separations by comparison to (∆u ∗ ) 2 and
141
(∆u ∗ ) 3 .
142
Then, for separations r ∗ & 10 2 , the effect of Reynolds
143
number becomes discernible and the r ∗ 4/3 scaling range
144
extends as the Reynolds number increases. Note that
145
the separation beyond which the measured eddy-viscosity
146
differs from the prediction of Eq.(7) in Fig.1(a) corre-
147
sponds to the scale beyond which (∆u) 3 ∗ /r ∗ is almost
148
zero in Fig.1(b). Therefore, ν t remains universal in the
149
range of separations over which the third-order structure
150
function has to be modelled. We further observe that,
151
though very close to the asymptotic relation Eq.(7), a
152
constant value of r ∗ c = 25.0 (instead of 36.3 providing
153
C u = 2) is more suitable to parametrize ν t over the whole
154
range of Reynolds numbers. This supports a universal
155
value for r c ∗ , although weaker than the expected (Kol-
156
mogorov) value. This is in agreement with the observa-
157
tions of [7] revealing that the prefactor in Eq.(6) varies
158
by only a few percent in the range 50 ≤ R λ ≤ 10 4 and re-
159
mains always smaller than the expected asymptotic value
160
even at a very high Reynolds number.
161
Finally, the last observation that one can make is that
162
at the highest Reynolds number (R λ = 1100), the scaling
163
ν t ∝ r ∗ 4/3 is accurately satisfied over almost two decades
164
of separations (10 2 . r ∗ . 10 4 ) whilst there is no un-
165
ambiguous scaling range for neither (∆u) 2 (not shown)
166
nor (∆u) 3 (Fig.1(b)). The scaling range of ν t does not
167
appear to be sensitive to any intermittency effect and is
168
also much more extended than that of second- and third-
169
order structure functions.
170
At this stage, we can draw the overall conclusion that,
171
at least over the range of Reynolds numbers investigated
172
here, S and r c ∗ can be reasonably considered as univer-
173
sal. The constancy of S relies on the validity of the Kol-
174
mogorov normalization in the dissipative range, which
175
holds even at low Reynolds numbers [18]. In contrast,
176
the constancy of r ∗ c is quite intriguing since it is now
177
well known that the Kolmogorov ’constant’ C u and the
178
scaling exponent of (∆u) 2 are sensitive to the Reynolds
179
number variations (at least for R λ < 10 4 [11]). To a large
180
extent, the observed universality of r ∗ c is thus most likely
181
due to some compensating effects that occur between C u ,
182
A u , and the scaling exponent of both (∆u) 2 and (∆u) 3
183
involved in Eq.(6). The consequence is that r ∗ c remains
184
constant with respect to the Reynolds number.
185
The universality of ν t can be further justified recalling
186
that ν t (r) ∝ r 2
τ (r) (see Eq.(19) in [19]), in which the
187
characteristic time-scale τ (r) is representative of the cas-
188
cade mechanism. In spectral space, one possible expres-
189
sion for τ(k) is that of Batchelor and Kraichnan [20] that
190
was recently invoked by [21] as a closure for the passive
191
scalar spectral equation. In [20], τ(k) was interpreted as
192
the time-scale of the strain at a given wavenumber due
193
to all larger scales. Using Kolmogorov scaling, τ(k) can
194
be expressed as
195
τ ∗ (k ∗ ) ∝
"
Z k
∗0
p ∗ 2 E ∗ (p ∗ )dp ∗
# − 1/2
, (8)
where p is a dummy integration variable. In Eq.(8), the
196
normalized spectrum is multiplied by p ∗ 2 so that the
197
contribution to the integral of the largest scales (low
198
wavenumbers) is weak. On the contrary, contributions
199
from the smallest scales are magnified and the range of
200
scales over which the Kolmogorov scaling is observed is
201
extended [18]. In other words, the integrand p ∗ 2 E ∗ (p ∗ ) in
202
Eq.(8) always satisfies Kolmogorov scaling over a larger
203
range of scales compared to E ∗ (p ∗ ) [18]. Therefore, since
204
ν t is intimately related to τ via ν t (r) ∝ r 2
τ (r), the
205
same conclusions can be drawn for the eddy-viscosity.
206
The idea of invoking a set of scales which yields a col-
207
lapse of velocity statistics over a wider range of scales
208
was already used in [22] for which the relevant scales are
209
λ and q 2 = u i u i (twice the total kinetic energy). Fur-
210
ther, in the energy-containing and inertial ranges, [23]
211
demonstrated that the use of u 2 and the von K´ arm´ an
212
length-scale (≡ u 2 3/2 /) leads to a satisfactory collapse of
213
energy spectra. As far as the eddy-viscosity is concerned,
214
it appears that the relevant normalization is given by the
215
Kolmogorov scales.
216
We now take advantage of this extended universality to
217
develop a simple closure equation for Eq.(1). Third-order
218
structure functions are thus calculated from measured
219
second-order structure functions using Eqs.(4) and (7).
220
The comparison between modelled and measured third-
221
order structure functions is shown in Fig.1(b).
222
Since Eq.(7) accurately represents the measured eddy-
223
viscosity, it is not surprising to observe that modelled
224
and measured third-order structure functions are in ex-
225
cellent agreement (Fig.1(b)). The shape and evolution
226
of (∆u) 3 ∗ /r ∗ with respect to the Reynolds number are
227
very well reproduced. The minor differences that may be
228
observed are rather due to some slight errors in evalu-
229
ating the derivative of measured second-order structure
230
functions.
231
A much more stringent test of the validity of the
232
present closure is the following. Starting with an ini-
233
tial condition at a particular position in the flow, can
234
we reliably predict the decay of second-order structure
235
functions downstream? To this end, Eq.(3) has to be
236
time-integrated.
237
Since theory is compared to a spatially decaying tur-
238
bulence (in this case grid turbulence [15]), we relate the
239
final time of integration to the downstream distance by
240
means of Taylor’s hypothesis, i.e. x ≡ U t (U is the mean
241
flow velocity). The time-integration of Eq.(3) is handled
242
using a fourth-order Runge-Kutta algorithm. Derivatives
243
∂ r • are approximated by a central second-order finite dif-
244
ference scheme. Boundary conditions are set as follows,
245
(∆u) 2 (r = 0) = 0 and ∂ r (∆u) 2 (r → ∞) = 0.
246
Results are given in Fig.2(a). The initial conditions are
247
set at x = 20M behind the grid (M = 24.76mm is the
248
grid mesh size) and predictions are compared with mea-
249
surements at x = 40, 60 and 80M . The initial Reynolds
250
number R λ is about 50 and decreases slightly with x.
251
Measured and predicted second-order structure func-
252
tions are in good agreement (Fig.2(a)). Minor differ-
253
ences can be observed at large separations where the
254
model very slightly overestimates (∆u) 2 . From the de-
255
cay of second-order structure functions, one can obtain
256
the evolution of one-point statistics, i.e. the longitudinal
257
velocity variance 2u 2 = (∆u) 2 (r → ∞), the mean dis-
258
sipation rate = 15ν lim r → 0 (∆u) 2 / r 2 , the Taylor and
259
Kolmogorov length scales (λ and η) and the Reynolds
260
number R λ . The mean dissipation rate can also be eval-
261
uated though the one point energy budget
262
= − 1
2 ∂ t q 2 , (9)
where q 2 = u 2 + v 2 + w 2 is twice the total kinetic en-
263
ergy. The evolution of one-point statistics is depicted in
264
Fig.2(b). The variation with respect to the downstream
265
distance of all these quantities is globally very well repro-
266
duced by the present model. One can further note that
267
4
10
010
110
210
310
410
−310
−210
−1r
∗= r/η (∆ u )
2(m
2s
−2)
Exp. x = 20M Exp. x = 40M Exp. x = 60M Exp. x = 80M Model x = 40M Model x = 60M Model x = 80M
(a)
30 40 50 60 70 80
10
−310
−210
−110
0x/M
u
2ǫ λ η R
λ(b)
FIG. 2. (a) Comparison between measured and predicted second-order structure functions in grid turbulence (R
λ≈ 50). The time-integration is started at x = 20M. (b) Evolu- tion of u
2/U
2, M/U
3(10
2), λ/M(10
−2), η/M and R
λ(10
−3) with x/M. U = 6.4m.s
−1is the mean flow velocity. Symbols represent measured values whilst solid lines are the predicted values. The mean dissipation rate is estimated from the relation = 15ν(∂
xu)
2( B ) and from Eq.(9) ( C ). The mea- sured Taylor and Kolmogorov length-scales were inferred from computed from Eq.(9).
the magnitude of the measured mean dissipation rate in-
268
ferred from = 15ν (∂ x u) 2 is smaller (≈ 15%) than that
269
predicted by the model. This discrepancy may be due to
270
the smallest scales not being sufficiently resolved by the
271
hot wire measurements. Indeed, values of using Eq.(9)
272
are only ≈ 10% smaller than those predicted.
273
The idea of predicting the decay of one-point statis-
274
tics from a two-point closure equation was also tackled
275
by Lohse [8], with a closure scheme based on the vari-
276
able range mean field theory. In the latter study, the
277
prediction of basic quantities, such as the normalized
278
energy dissipation and enstrophy decay rates, compared
279
favourably with experimental results in a particular type
280
of decaying flow where the integral length scale does not
281
vary with time. Obviously, this type of analytical treat-
282
ment cannot be applied to decaying grid turbulence where
283
the integral length scale grows continuously with time (or
284
distance from the grid).
285
In summary, the universal facets of the eddy-viscosity
286
for the closure of the K´ arm´ an-Howarth equation are ex-
287
amined in detail. It is highlighted that ν t remains impres-
288
sively universal over a remarkable range of scales. An an-
289
alytical expression for ν t is further proposed, based on the
290
observed constancy of the skewness of velocity derivatives
291
and highlights the existence of a new scale of turbulence
292
called r c . The model is in good agreement with measure-
293
ments in different types of decaying flows, over a wide
294
range of Reynolds numbers. The closure scheme is finally
295
time-integrated and reproduces measured second-order
296
structure functions in grid turbulence quite favourably.
297
The financial support of the ’Agence Nationale de la
298
Recherche’ (ANR), under the project ’ANISO’, is grate-
299
fully acknowledged. RAA and LD acknowledge the sup-
300
port of the Australian Research Council.
301
[1] T. von K´ arm´ an and L. Howarth, Proc. Roy. Soc. Lond.
302
A 164 (917), 192 (1938).
303
[2] G. K. Batchelor, Proc. Camb. Phi. Soc. 43, 533 (1947);
304
L. Danaila, F. Anselmet, T. Zhou, and R. A. Antonia,
305
J. Fluid Mech. 391, 359 (1999).
306
[3] T. von K´ arm´ an and C. C. Lin, Advances in Applied Me-
307
chanics 2, 1 (1951).
308
[4] R. Kraichnan, J. Fluid Mech. 4, 497 (1959).
309
[5] S. Orszag, J. Fluid Mech. 41, 363 (1970).
310
[6] M. Millionshchikov, Pis’ma Zh. Exp. Teor. Fiz. 10(8),
311
406 (1969); Pis’ma Zh. Exp. Teor. Fiz. 11(3), 203 (1970).
312
[7] J. A. Domaradzki and G. L. Mellor, J. Fluid Mech. 140,
313
45 (1984).
314
[8] H. Effinger and S. Grossmann, Z. Phys. B 66, 289 (1987);
315
D. Lohse, Phys. Rev. Lett. 73(24), 3223 (1994).
316
[9] M. Oberlack and N. Peters, Applied Scientific Research
317
51, 533 (1993).
318
[10] M. K. Baev and G. G. Chernykh, J. of Engineering Ther-
319
mophysics 19(3), 154 (2010).
320
[11] R. A. Antonia and P. Burattini, J. Fluid Mech. 550, 175
321
(2006).
322
[12] R. W. Stewart and A. A. Townsend, Phil. Trans. R. Soc.
323
Lond. A 243, 359 (1951).
324
[13] A. Kolmogorov, Dokl. Akad. Nauk. SSSR 30, 299 (1941);
325
Dokl. Akad. Nauk. SSSR 125, 15 (1941).
326
[14] G. K. Batchelor, Proc. Camb. Phi. Soc. 47, 359 (1951).
327
[15] T. Zhou, R. A. Antonia, L. Danaila, and F. Anselmet,
328
Exp. Fluids 28, 143 (2000); R. A. Antonia, B. R. Pear-
329
son, and T. Zhou, Phys. Fluids 12, 3000 (2000); R. A.
330
Antonia, M. Ould-Rouis, F. Anselmet, and Y. Zhu, J.
331
Fluid Mech. 332, 395 (1997).
332
[16] W. J. T. Bos, L. Chevillard, J. Scott, and R. Rubinstein,
333
Phys. Fluids 24, 015108 (2012).
334
[17] K. R. Sreenivasan and R. A. Antonia, Ann. Rev. Fluid
335
Mech. 29, 435 (1997).
336
[18] R. A. Antonia, L. Djenidi, and L. Danaila, to be sub-
337
mitted to Phys. Fluids (2013).
338
[19] L. Danaila, R. A. Antonia, and P. Burattini, Physica D
339
241, 224 (2012).
340
[20] G. K. Batchelor, J. Fluid Mech. 5, 113 (1959); R. H.
341
Kraichnan, J. Fluid Mech. 47, 525 (1971).
342
[21] L. Danaila and R. A. Antonia, Phys. Fluids 21, 111702
343
(2009).
344
[22] W. George, Phys. Fluids 4, 1492 (1992).
345
[23] L. T. Adzhemyan, M. Hnatich, D. Horvath, and
346
M. Stehlik, Phys. Rev. E 58(4), 4511 (1998).
347