It is widely believed that at high Reynolds number (Re) all turbulent flows approach a limiting state of “fully developed turbulence" in which the statistics of the velocity fluctuations are independent of Re. Nevertheless, direct measurements of the velocity fluctuations have failed to yield firm empirical evidence that even the second-order structure function becomes independent of Re at high Re, let alone structure functions of higher order. Here we relate the friction coefficient (f) of rough-pipe flows to the second-order structure function. Then we show that in light of experimental measurements of f our results yield unequivocal evidence that the second-order structure function becomes independent of Re at high Re, compatible with the existence of fully developed turbulence.

1.
Reprinted in
A. N.
Kolmogórov
, “
The local structure of turbulence in incompressible viscous fluid for very large Reynolds numbers
,”
Proc. R. Soc. London, Ser. A
434
,
9
(
1991
).
2.
A.
Praskovsky
and
S.
Oncley
, “
Measurements of the Kolmogorov constant and intermittency exponent at very high Reynolds numbers
,”
Phys. Fluids
6
,
2886
(
1994
).
3.
L.
Mydlarski
and
Z.
Warhaft
, “
On the onset of high Reynolds number grid generated wind tunnel turbulence
,”
J. Fluid Mech.
320
,
331
(
1996
)
and
L.
Mydlarski
and
Z.
Warhaft
, “
Passive scalar statistics in high-Péclet-number grid turbulence
,”
J. Fluid Mech.
358
,
135
(
1998
).
4.
G. I.
Barenblatt
and
N.
Goldenfeld
, “
Does Fully-Developed Turbulence Exist? Reynolds Number Independence versus Asymptotic Covariance
,”
Phys. Fluids
7
,
3078
(
1995
).
5.
K. R.
Sreenivasan
, “
On the universality of the Kolmogorov constant
,”
Phys. Fluids
7
,
2778
(
1995
).
6.

A similar expression holds for the structure function of order n, (ul)n¯=Pn[Re,lL](εl)n3.

7.
G. I.
Barenblatt
,
Scaling, Self-similarity, and Intermediate Asymptotics
(
Cambridge University Press
,
Cambridge, UK
,
1986
), Chap. 10.
8.

“The mathematical expression of the assumption of a limiting state of fully developed turbulence is that statistical averages of the flow exhibit complete similarity with respect to Re” (Ref. 4). Therefore, in fully developed turbulence the leading term of (ul)n¯ is independent of Re for all n2. Here we concern ourselves only with n=2.

9.
U.
Frisch
,
Turbulence
(
Cambridge University Press
,
Cambridge, UK
,
1995
).
10.
A. N.
Kolmogórov
, “
A refinement of previous hypotheses concerning the local structure of turbulence in a viscous incompressible fluid at high Reynolds number
,”
J. Fluid Mech.
13
,
82
(
1962
).
11.

For example, the form of the structure function should not change if we used Reλ in lieu of a global Re.

12.

Barenblatt and Goldenfeld also assumed a general type of incomplete similarity with respect to lL in which the intermittency exponent, α, may depend on Re (Ref. 7). Then, in keeping with the principle of asymptotic covariance, they wrote α(lnRe)=α0+α1lnRe+o(1lnRe), and pointed out that the experimental data of Praskovsky and Oncley (Ref. 2) favor α0=0 (or α0 at high Re). Since α is of slight concern here, we continue to represent it as a constant. Nevertheless, in all our equations α may be substituted by α0+α1lnRe+o(1lnRe).

13.

Italics in the original.

14.
The scatter may stem from simplifications variously used in processing hot-wire data; see
S. T.
Thoroddsen
, “
Reevaluation of the experimental support for the Kolmogorov refined similarity hypothesis
,”
Phys. Fluids
7
,
691
(
1995
).
15.
Reprinted in
J.
Nikuradse
, “
Laws of flow in rough pipes
,” NACA Technical Memorandum 1292 (
1950
).
16.
For similar data on channel flows see
O.
Kirshmer
, “
Pertes de charge dans les conduites forcées et les canaux décou-verts
,”
Revue générale de l’hydraulique
51
,
115
(
1949
).
17.
G.
Gioia
and
F. A.
Bombardelli
, “
Scaling and similarity in rough channel flows
,”
Phys. Rev. Lett.
88
,
014501
(
2002
).
18.
B.
Knight
and
L.
Sirovich
, “
Kolmogorov inertial range for inhomogeneous turbulent flows
,”
Phys. Rev. Lett.
65
,
1356
(
1990
);
[PubMed]
R. D.
Moser
, “
Kolmogorov inertial range spectra for inhomogeneous turbulence
,”
Phys. Fluids
6
,
794
(
1994
).
19.
Our conclusions would still hold if we adopted one of several expressions that are similar to (2) but do not satisfy the principle of asymptotic covariance—e.g., p(Re)=p0+p1Reβ, an expression that can be derived without assuming isotropy or homogeneity;
see
T. S.
Lundgren
, “
Kolmogorov turbulence by the method of matched asymptotic expansions
,”
Phys. Fluids
15
,
1074
(
2003
).
For experiments that support the principle of asymptotic covariance see
A.
Arneodo
,
S.
Manneville
,
J. F.
Muzy
, and
S. G.
Roux
, “
Revealing a lognormal cascading process in turbulent velocity statistics with wavelet analysis
,”
Philos. Trans. R. Soc. London, Ser. A
357
,
2415
(
1999
).
20.
For experimental results relevant to this scaling see
B.
Hofland
,
J. A.
Battjes
, and
R.
Booij
, “
Measurement of Fluctuating Pressures on Coarse Bed Material
,”
J. Hydraul. Eng.
131
,
770
(
2005
).
21.
L. D.
Landau
and
E. M.
Lifshitz
,
Fluid Mechanics
, 2nd ed. (
Butterworth
,
Oxford, UK
,
2000
), Chap. III, p.
130
.
22.
Reprinted in
A.
Strickler
,
Contribution to the question of a velocity formula and roughness data for streams, channels and close pipelines
, translation by
T.
Roesgen
and
W. R.
Brownlie
(
Caltech
,
Pasadena
,
1981
).
23.
By “smooth” we mean “mathematically smooth.” Whether an actual pipe may be considered smooth appears to be a question that grants no easy answers;
see
G. I.
Barenblatt
and
A. J.
Chorin
, “
Scaling of the intermediate region in wall-bounded turbulence: The power law
,”
Phys. Fluids
10
,
1043
(
1998
);
A. J.
Smits
and
M. V.
Zagarola
, “
Response to “Scaling of the intermediate region in wall-bounded turbulence: The power law
,”
Phys. Fluids
10
,
1045
(
1998
);
B. J.
McKeon
,
M. V.
Zagarola
,
A. J.
Smits
, “
A new friction factor relationship for fully developed pipe flow
,”
J. Fluid Mech.
538
,
429
(
2005
).
24.
For example, the normalized dissipation in the experiments of
D. P.
Lathrop
,
J.
Fineberg
, and
H. L.
Swinney
, “
Turbulent flow between concentric rotating cylinders at large Reynolds number
,”
Phys. Rev. Lett.
68
,
1515
(
1992
) and
[PubMed]
O.
Cadot
,
Y.
Couder
,
A.
Daerr
,
S.
Douady
, and
A.
Tsinober
, “
Energy injection in closed turbulent flows: Stirring through boundary layers versus inertial stirring
,”
Phys. Rev. E
56
,
427
(
1997
).
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