CA2224041A1

CA2224041A1 - Method of and apparatus for controlling turbulence in boundary layer and other wall-bounded fluid flow fields

Info

Publication number: CA2224041A1
Application number: CA002224041A
Authority: CA
Inventors: Lawrence Sirovich; Lucien Y. Bronicki; Eugene Levich; Sture Karlsson
Original assignee: Lawrence Sirovich; Lucien Y. Bronicki; Eugene Levich; Sture Karlsson; Orlev Scientific Computing Ltd.
Current assignee: Orlev Scientific Computing Ltd
Priority date: 1996-12-09
Filing date: 1997-12-08
Publication date: 1998-06-09
Also published as: RU2191931C2; JPH10183557A; CN1186268A; US5833389A; EP0850832A1; IL122505A0; KR19980063904A; IL122505A

Abstract

Turbulence is controlled in boundary layer or wall-bounded fluid flow fields having a turbulent wall region which under natural conditions, has an average system of roll pairs or streaks adjacent the surface, and extending in the direction of flow, by locally introducing into the turbulent wall region, by passive means, a disturbance that enhances or inhibits the roll pairs thereby locally increasing or decreasing the turbulence in the flow field.

Description

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DESCRIPTION
M~l~.OV OF AND APPARATUS FOR CONTROLLING TURBULENCE
IN BOUNDARY LAYER AND OTHER WALL-BOUNDED FLUID FLOW FIELDS
Technical Field This invention relates to a method of and apparatus for controlling turbulence in boundary layer and other wall-bounded fluid flow fields.
Background Art U.S. Patent No. 5,263,793 issued November 23, 1993, and 10 U.S. Patent No. 5,354,017 issued October 11, 1994, the disclosures of which are hereby incorporated by reference, view turbulence as having coherent patterns of activity in the midst of apparent chaos. Specifically, these patents and the publications cited therein, describe turbulent flow 15 as being characterized by a system of roll pairs extending in the direction of flow, and obliquely propagating structures interacting with the system of roll pairs. These structures apparently propagate at a constant group speed, and are described as being triggers for the bursting of the 20 roll pairs which give rise to drag. The most important of the propagating modes, are apparently those that propagate at an angle of about 65~ from the streamwise direction; and those in the range 50-80~ appear to contain the dominant energy content of the propagating modes.
These roll pairs, which are sometimes referred to as streaks, counter-rotate and lie adjacent the bounding walls at the outer edge and beyond the sublayer. They show considerable meander and variation in their dynamic activity. Of great importance is their sudden contortion or 30 kinking, resulting in a sudden bursting forth of slow moving fluid from near the wall into the fast moving main body of fluid motion. This bursting results in a net drag on the walls. It has been estimated that these bursts, which account for 80~ of the drag on a wall, occur only roughly 35 20~ of the time. Again, a study of the patterns of such flow shows that the contortion of the rolls undergoes a stereotypical coherence pattern through temporal change that is typical of all wall-bounded turbulence.
To specify the size of the streaks, it is first necessary to recognize that the streaks are a manifestation 5 of local conditions beyond the sublayer of the flow adjacent to a wall, and not of the nature of the wall, nor of the flow field significantly spaced from the wall. Local conditions are fully specified by the average frictional stress at a wall, s, the density of the fluid, r, and the viscosity of 10 the fluid, m. These quantities define a local size dimension, or length scale l* which is usually referred to as a wall unit and is equal to m/(sr) . The dominant roll diameter is nominally 50 to 100 wall units, or 100 1* to 200 l* per pair.
The term "dominant", in referring to the roll diameter, means that the greatest amount of turbulent energy (of the fluctuating velocity) resides in modes of activity of this size. There is, in addition, other modes of the same roll type, having a range of sizes and which also contain 20 significant amounts of turbulent energy.
According to the two patents cited above, turbulence in a medium is controlled by locally introducing into the turbulent wall region two separate disturbances that are effective to produce, in a local region, a composite 25 disturbance field that is strongly coupled to and modifies the obliquely propagating structures in a manner that increases or decreases the interaction of the propagating structures with the system of roll pairs thereby locally increasing or decreasing the turbulence in the flow field.
30 One of the disturbances may be caused by passive means such as the interaction of the fluid with an array of strips of delta-shaped protrusions positioned spanwise on the wall (i.e., transverse to the flow direction) with the apices of the protrusions pointed upstream of the flow; and the second 35 disturbance may be caused by active means such as injecting energy into the local region by active mechanical, electrical, or hydrodynamical means.
It is an object of the present invention to provide a method of and apparatus for simplifying the management of turbulent flow using certain types of passively created 5 disturbances. These disturbances may also be created by active means.
BRIEF DESCRIPTION OF THE INVENTION
According to the present invention, turbulent drag may be reduced in boundary layer or other wall-bounded fluid 10 flow fields having a turbulent wall region characterized by the natural system of average roll pairs or steaks adjacent to the surface of a wall, by introducing into the wall region by passive means, a disturbance that inhibits the creation of, or breaks up, the roll pairs utilizing a two-15 dimensional array of protrusions on, or cavities in, thewall surface. Preferably, the array includes a plurality of protrusions arranged in successive rows perpendicular to the direction of fluid flow, the protrusions of a succeeding row being staggered relative to the protrusions of a preceding 20 row, either in a regular or random manner. The elements of a row may be uniformly placed, or randomly advanced or retarded within a row.
Preferably, the protrusions project into the flow a distance in the range 5 to 15 wall units, where a wall unit 25 (l*) is as defined above; and the protrusions are V-shaped with apices directed upstream to the direction of flow (i.e., pointing in the direction from which the flow comes).
The apex angle of the protrusions is preferably in the range 50-9C¦. The pitch of the protrusions in a row preferably is 30 in the range of one protrusion per 100-300 wall units, and the pitch of the protrusions in the direction of flow is in the range of one row per 200-400 wall units. Preferably, the dimension of the protrusions in the direction of flow is in the range 150-250 wall units.
Increased mixing (i.e., increased drag) is achieved with the same type of protrusions, but placed in an unstaggered manner, with uniform columns and rows.
BRIEF DESCRIPTION OF DRAWINGS
Embodiments of the present invention are described by way of example with reference to the accompanying drawings 5 wherein:
Fig. 1 is a cross-section showing wall-bounded fluid flow, where the cross-section is taken perpendicular to the direction of flow;
Fig. 2 is a schematic plan view of the fluid flow 10 field shown in Fig. 1 showing streaks or rolls adjacent a wall boundary having herring-bone undulations;
Fig. 3 is a cross-section through the wall showing the undulations;
Fig. 4 is a modified version of the undulations;
Fig. 5 is a portion of a wall containing protrusions according to the present invention; and Fig. 6 is a sectional view of the wall taken along the line 6-6 of Fig. 5.
Detailed Description Referring now to the drawings, reference numeral 10 designates a wall-bounded turbulent flow field including wall 12 restraining fluid 13 containing local statistical structures in the form of counter-rotating rolls 14, 16 of fluid. The axes of these rolls, or streaks as they are 25 sometimes called, lie, on the average, in the direction of fluid flow which is into the paper showing Fig. 1, and as indicated by arrow 17 in Fig. 2. Briefly, the counter rotating rolls have, on the average, a length much greater than their diameters (approximately 1000 l*). As indicated 30 above, the dominant roll size is roughly 100 l*, to 200 l*
per pair.
In fully developed turbulent flow, these local roll structures travel downstream throughout the near wall region, are disrupted, contort, and finally burst (i.e., are 35 ejected from the wall region). In the patents cited above, the interaction between the coherent structure of propagating modes present in the flow and the coherent structure of the rolls was considered to be the basis for the bursting of the rolls, and the consequent mixing of slow moving fluid near the boundary with rapidly moving fluid in 5 the main flow and vice versa. These patents provided both passive and active mechanisms for controlling the triggering aspects of the wave propagating modes which were alleged to participate in the bursting of the roll-modes in turbulent wall-bounded flows.
A passive mechanism, according to the invention in the cited patents, for controlling the wave propagation modes is the presence of shaped modifications, such as grooves, undulations, etc. on the walls containing the turbulent flow. For example, the shape modifications can be achieved 15 by actually grooving the walls, or by applying to the walls an adhesive layer which contains the required shapes. When the shape modification is in the form of undulations, their amplitude should be in the range 5-20 wall units in order to include the location of peak turbulence production. The 20 wavelength or pitch of typical undulations will depend on the objective of the turbulence management. The orientation of the undulations, i.e., the direction of the troughs between the peaks of the undulations, should be inclined at about 15-30~ off the streamwise direction. That is to say, 25 the "propagation" direction of the undulations should be about 60-75~ from the streamwise direction.
Fig. 2 shows a plan view of rolls 14, 16; and superimposed on these rolls are waves that propagate (the propagating modes) in the direction indicated by arrow 18 30 making an angle +~ with the flow direction 17. As indicated above, ~ lies in the range 50-80~ for the waves having the dominant energy content. To account for the possible bi-directional angle of the propagating modes, the undulations would be in the form of herring-bone-like pattern 20 as 35 shown in Fig. 2, or a cross-hatched-like, or "knurled"
pattern.

According to the cited patents, in order to enhance mixing and, for example, increase heat transport, (i.e., increase turbulence), and therefore to encourage the eruption of bursts, the undulations should be ordered in a 5 strictly sinusoidal pattern as indicated in Fig. 3. The wavelength ~ is preferably in the range 100-300 wall units in order to achieve resonance with the triggering modes, and the amplitude a is preferably in the range 15-20 wall units.
In order to reduce drag, the undulations should be 10 given a pattern that introduces phase interference in the waves in a manner that is analogous to the above-mentioned phase randomization. One method for achieving this is by creating a "chaotic" pattern modulation by the resonant wavelength, and containing a suitable sum of incommensurate 15 sinusoids ranging down in wavelength. A model cross-sectional plot is given in Fig. 4.
According to the present invention, turbulent drag on a bounding surface can be controlled by introducing into a bounding wall region, by passive means, a disturbance that 20 enhances or inhibits the creation of roll pairs thereby increasing or decreasing the turbulence in the flow field.
When the disturbance enhances the creation of roll pairs, drag is increased; and when the disturbance inhibits the creation of roll pairs~ drag is decreased.
The preferred manner of introducing disturbances of this type is by applying to the bounding walls a pattern of protrusions on, or cavities in, an otherwise smooth surface.
The sizes of the protrusions or cavities, and the nature of the pattern of such protrusions or cavities, inhibits or 30 enhances creation of roll pairs.
Referring now to Fig. 5, reference numeral 50 designates apparatus according to the present invention for inhibiting creation of roll pairs in a boundary layer or other wall-bounded fluid flow field whose direction is 35 indicated by arrow 53, and which has a turbulent wall region adjacent surface 51 of wall 52. The direction of which is indicated by arrow 53. Applied to surface 51 are means for introducing into the wall region, by passive means, a disturbance that inhibits the creation of roll pairs. Such means, preferably, are in the form of a two-dimensional 5 array 54 of protrusions 55 on surface 51. Alternatively, such means can be in the form of cavities in surface 51.
Preferably, array 54 is in the form of a plurality of protrusions arranged in successive rows perpendicular to the direction of fluid flow, the protrusions of a succeeding row 10 being staggered, regularly, or randomly, relative to the protrusions of a preceding row. Preferably, the protrusions are V-shaped and have their apices directed opposite to the direction of flow. That is to say, apex 56 of a protrusion faces into the flow. While the sides that trail from the 15 apex of a protrusion are shown as being straight, the sides may be curved either in a concave or convex manner.
Furthermore, the apex angle a of the protrusions preferably is in the range 50-90~.
The application of a pattern of protrusions according 20 to the present invention may require changes in scale. Such is the case for turbulent boundary layers, as might be found on a wing of an aircraft or its fuselage. For growing boundary layers, scale sizes change slowing as the 1/10 power of the streamwise distance.
As shown in Fig. 5, the pitch of the protrusions in the direction of flow (i.e., the row pitch of the pattern) is designated "a", and the dimension of the protrusions in the direction of flow is designated "b". The dimension of the protrusions in the direction perpendicular to the flow 30 (i.e., in the spanwise direction) is designated "c". The pitch of the protrusions in a direction transverse to the direction of flow (i.e., in the row direction) is designated "d"; and the offset between protrusions of a succeeding row and the protrusions of a preceding row (i.e., the stagger 35 between columns) is designated "e". Finally, the height or thickness of the protrusions is designated "f".

Specific wall patterns have been tested in a close-return, low speed channel wind tunnel. The dimensions of the test section of the tunnel are: 5.5 cm high, 75 cm wide, and 850 cm long. A settling chamber 150 cm precedes the 5 test section. Typical experimental Reynolds' numbers were in the range 10,800 to 18,000 corresponding to centerline velocities of 6-10 m/sec. The pattern was applied only to a portion of the floor of the test section.
Table A lists the dimensions, in millimeters, of a 10 pattern tested which yielded drag reductions; and Table B
lists the dimensions tested which yielded drag increases.
Design 2 was evaluated with offset "e" fixed, or regular, and with the offset being random, in which case the value "e" represents the average value. Designs 3 and 4 were 15 evaluated with offset "e" fixed.
TABLE A (Dimensions in millimeters) Dimension Des. 2 a 13.9 b 10 c 9.1 d 13.5 e 6.75 f 0.25 TABLE B (Dimensions in millimeters) 25 Dimen. Des. 3 Des. 4 Des. 5 Des. 6 Des. 7 a 36.5 31.3 10.0 10.1 18.3 b 15.0 10.0 15.0 7.3 7.3 c 12.5 7.7 12.5 6.6 6.6 d 19.7 10.5 19.7 9.8 9.8 30 e 0 0 0 0 0 f 0.25 0.25 0.25 0.25 0.25 The following results were achieved for drag reduction using Design 2 with the offset being random (i.e., a randomly staggered pattern) for the flow velocities 35 indicated (at 7m/sec, one wall unit is approximately equal to 0.05mm.):
V(m/sec) Draq chanqe 5.86 -9.95 7.03 -13.5 8.39 -8.1 9.48 -6.7 10.05 -6.5~
When the offset was fixed (i.e., a uniformly staggered pattern as shown in Fig. 6), drag reduction resulted, but under identical experimental conditions, it was significantly less than when the offset was random.
Randomization also can be applied to the height of the protrusions as well as to the vee-shapes of a pattern.
The following results were achieved for mixing (i.e., drag increase) are:
Vel. (m/sec) 6 7 8 Drag (~) +42.5 +45.0 +47.0 Des. 3 +41.2 +42.7 +43.5 Des. 4 In the case of mixing, offset "e" between protrusions of a succeeding row and the protrusions of a preceding row (i.e., the stagger between columns), is zero. In other words, mixing is enhanced when the protrusions are not staggered. Patterns of this nature are suitable for heat 15 exchange surfaces, etc.
When the protrusions are staggered, the invention is applicable to arbitrary fluid devices such as pipes and ducts of any cross-section, to vessels such as aircraft fuselages. boats, ships, etc., and to airfoils, as well as 20 to channel flow which is illustrated in the above described experiments. Moreover, the invention is also applicable to active disturbances achieved through the use of MEMS, piezoelectric, and electohydrodynamic means of corresponding size and placement to the end that the disturbance interacts 25 with the roll pairs.
The position of the V-shaped elements in a row may also be randomized. That is to say, the position of elements in a row relative to the row centerline elements may be advanced or retarded randomly. For both sorts of 30 randomizations, practical considerations can force the pattern to be repeated after some number of randomizations.
The results given above for drag reductions are a consequence of applying a patterned material to only the floor of the test section of the wind tunnel. If patterned 35 material were applied to all of wall of ducts and pipes, for example, the drag reduction achieved (based on non-linear considerations) should exceed the simple intuitive doubling of the drag decrease. At optimal conditions, (7m/sec for the example given), a drag reduction in excess of 30~ may be expected. A similar enhancement of mixing can be expected when the appropriate pattern is supplied to all walls.
The advantages and improved results furnished by the method and apparatus of the present invention are apparent from the foregoing description of the preferred embodiment of the invention. Various changes and modifications may be made Without departing from the spirit and scope of the 10 invention as described in the appended claims.

Claims

WHAT IS CLAIMED IS:

1. A method for controlling turbulence in boundary layer or other wall-bounded fluid flow fields having a turbulent wall region adjacent the surface of a wall characterized by a system of roll pairs or steaks adjacent the surface and extending in the direction of flow, said method including introducing into said wall region, by passive means, a disturbance that enhances or inhibits the creation of said roll pairs thereby increasing or decreasing the turbulence in the flow field.

2. A method for increasing turbulence in boundary layer or other wall-bounded fluid flow fields having a turbulent wall region characterized by a system of roll pairs or steaks adjacent the wall, said roll pairs or streaks having a diameter functionally related to the strength of the flow, and which extend in the direction of flow, said method including introducing into said wall region a passive disturbance that enhances creation of said roll pairs.

3. Apparatus for decreasing turbulent drag in a turbulent wall region of a fluid flow field adjacent the surface of a wall, wherein said turbulent wall region is characterized by a system of roll pairs or steaks adjacent said surface, said roll pairs or streaks having a diameter functionally related to the strength of the flow, and apparatus including means for introducing into said wall region a passive disturbance that inhibits the creation of said roll pairs.

4. Apparatus according to claim 3 wherein said means is in the form of a two-dimensional array of protrusions on, or cavities in, said surface.

5. Apparatus according to claim 3 wherein said array includes a plurality of protrusions arranged in successive columns perpendicular to the direction of fluid flow, the protrusions of a succeeding row being staggered relative to the protrusions of a preceding row.

6. Apparatus according to claim 5 wherein said protrusions are staggered regularly.

7. Apparatus according to claim 3 wherein said protrusions are staggered randomly.

8. Apparatus according to claim 5 wherein said protrusions project into the flow a distance in the range 5 to 15 wall units, where a wall unit is the viscosity divided by the square root of the density and shear stress.

9. Apparatus according to claim 8 wherein said protrusions are V-shaped, the apices of the protrusions being directed upstream of the direction of flow.

10. Apparatus according to claim 9 wherein the apex angle of said protrusions is in the range 50-90¦.

11. Apparatus according to claim 9 wherein the pitch of the protrusions in rows is in the range one protrusion to about 200-300 wall units.

12. Operators according to claim 9 wherein the pitch of the protrusions in the direction of flow is in the range one row per 200-400 wall units.

13. Apparatus according to claim 9 wherein the dimension of the protrusions in the direction of flow is in the range 150-250 wall units.

14. Apparatus for increasing turbulence in boundary layer or other wall-bounded fluid flow fields having a turbulent wall region characterized by the natural system of roll pairs or steaks adjacent the wall, said roll pairs or streaks having a diameter functionally related to the strength of the flow, and which extend in the direction of flow, said apparatus including introducing into said wall region a passive disturbance that enhances creation of said roll pairs.

15. Apparatus for increasing turbulent drag in a turbulent wall region of a fluid flow field adjacent the surface of a wall, wherein said turbulent wall region is characterized by the natural system of roll pairs or steaks adjacent said surface, said roll pairs or streaks having a diameter functionally related to the strength of the flow, and apparatus including means for introducing into said wall region a passive disturbance that enhances the creation of said roll pairs.

16. Apparatus according to claim 15 wherein said means is in the form of a two-dimensional array of protrusions on, or cavities in, said surface.

17. Apparatus according to claim 15 wherein said array includes a plurality of protrusions arranged in successive rows perpendicular to the direction of fluid flow, the protrusions of a succeeding row being aligned with the protrusions of a preceding row.

18. Apparatus according to claim 17 wherein said protrusions project into the flow a distance in the range 5 to 15 wall units, where a wall unit is the viscosity divided by the square root of the density and shear stress.

19. Apparatus according to claim 18 wherein said protrusions are V-shaped, the apices of the protrusions being directed upstream of the direction of flow.

20. Apparatus according to claim 19 wherein the apex angle of said protrusions is in the range 50-90°.

21. Apparatus according to claim 9 wherein the pitch of the protrusions in a row is in the range one protrusion per 200-300 wall units.

22. Operators according to claim 9 wherein the pitch of the protrusions in the direction of flow is in the range one row per 200-400 wall units.

23. Apparatus according to claim 9 wherein the dimension of the protrusions in the direction of flow is in the range 150-250 wall units.